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GERENCIA DE INGENIERÍA Y PROYECTOS
REEMPLAZA A:
REV.
REEMPLAZADO POR:
REV.
ESTE DOCUMENTO ES PROPIEDAD DE STARK INDUSTRIES
TITULO: BALANCE DE MATERIA Y ENERGIA OBRA: MEMORIA DE CÁLCULO
IDENTIFICACIÓN:
ESCALA:
REVISION: 1
N/A CND-FEND-MEXXX
A
MEMORIA DE CÁLCULO
ELABORO
Ing. Jose Maria Ayaa
REVISO
Ing. Jose Maria Ayala
APROBÓ A REV.
PARA APROBACIÓN
29.12.18
DESCRIPCIÓN
FECHA
MPR ELABORO
ACS
HDL
REVISO
APROBÓ
LISTA DE REVISIONES
2
Memoria de Cálculo BALANCE DE MASA Y ENERGIA
Identificación CND-FENDMEXXX
Revisión
Pág. 1
De 22
A
1
OBJETIVO .................................................................................................................... 4
2
ALCANCE ..................................................................................................................... 4
3
DATOS Y CÁLCULOS..................................................................................................... 4
4
CONCLUSIONES ......................................................................................................... 57
3
Memoria de Cálculo BALANCE DE MATERIA Y ENERGÍA
Identificación CND-FENDMEXXX
Revisión A
1
OBJETIVO
Mediante el presente trabajo se pretende simular y validar la planta de amoniaco y urea 2
ALCANCE
El balance de masa y energía adjunto en el presente documento es el resultado de una simulación de una planta de Amoniaco y Urea. Se utilizó el programa Aspen Hysys v8.8. 3. Datos y cálculos Parámetros de las especificaciones técnicas .
Compositions Comp Mole Frac (CO) Comp Mole Frac (H2O) Comp Mole Frac (Oxygen) Comp Mole Frac (Methane) Comp Mole Frac (H2S) Comp Mole Frac (Hydrogen) Comp Mole Frac (Ethane) Comp Mole Frac (Propane) Comp Mole Frac (CO2) Comp Mole Frac (Nitrogen) Comp Mole Frac (Air) Comp Mole Frac (Mercury) Comp Mole Frac (MEAmine) Comp Mole Frac (Ammonia)
Gas de Alimentacion 0 0 0 0.906 10 0 0.074 50 0.001 0.018 4 0 0 0 0
Gas Combustible 0 0 0 0.906 10 0 0.074 50 0.001 0.018 4 0 0 0 0
Vapor 0 1 0 0 0 0 0 0 0 0 0 0 0 0
H2S-1 0 0 0 0.906 10 0 0.074 50 0.001 0.018 4 0 0 0 0
4
Memoria de Cálculo BALANCE DE MATERIA Y ENERGÍA
Identificación CND-FENDMEXXX
Revisión A
Compositions Comp Mole Frac (CO) Comp Mole Frac (H2O) Comp Mole Frac (Oxygen) Comp Mole Frac (Methane) Comp Mole Frac (H2S) Comp Mole Frac (Hydrogen) Comp Mole Frac (Ethane) Comp Mole Frac (Propane) Comp Mole Frac (CO2) Comp Mole Frac (Nitrogen) Comp Mole Frac (Air) Comp Mole Frac (Mercury) Comp Mole Frac (MEAmine) Comp Mole Frac (Ammonia)
H2S-Stand By 0 0 0 0.90 61 0 0 0.07 45 0 0.00 0.01 14 8 0 0 0 0
Gas de Alimentacion
Conditions
gasc 0.43 72 0 0.03 0.02 12 69 0 0.00 0.03 05 09 0 0.42 0.04 65 69 0 0 0 0
Gas Combustible
Temperature (F)
60
60
Pressure (psia)
414. 7 792. 2
414. 7 351. 6
Molar Flow (lbmol/hr)
Compositions Temperature (F) Pressure (psia) Molar Flow (lbmol/hr)
Corrientes de Amoniaco 84 y 85 0 0 0.00 0.00 0.00 73 0.00 73 0.00 15 0.00 15 18 0 18 0 0.00 0.00 0.00 01 0.00 01 69 0 69 0 0.00 0.00 62 0 62 0 0 0 0 0 0.00 0.00 0.97 04 0.97 04 57 57
Vap or
gasc
274. 9 364. 7 191 8
335. 170 3 133. 8
Corrientes de Amoniaco 84 y 85 79.29 79.29 229.7 229.7 203 250.4
5
Memoria de Cálculo BALANCE DE MATERIA Y ENERGÍA
Identificación CND-FENDMEXXX
Revisión A
4. CONCUSIONES
El sistema de producción de amoniaco tiene una producción nominal de 200 toneladas día. Los flujos, composiciones, presiones y temperaturas están presentes en el work book. El presente documento tiene relación con el documento de l
6
Memoria de Cálculo BALANCE DE MATERIA Y ENERGÍA
Identificación CND-FENDMEXXX
Revisión A
WORK BOOK CORRIENTES
7
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 000
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Vapour Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
1983
1983
18
Molar Enthalpy
(Btu/lbmole)
-8118
-8118
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Liquid Phase
1.0000
1.0000
0.0000
(F)
87.00
87.00
87.00
(psia)
4565
4565
4565
865.2
865.2
0.0000
(lbmole/hr) (lb/hr)
1.450e+004
25.54
1.450e+004
25.54
0.0000 0.0000 -2.941e+004 21.07
(Btu/hr)
-7.024e+006
-7.024e+006
0.0000
(barrel/day)
* 1.399e+006
1.399e+006
0.0000
22
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29 30 31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
9.722e+004
9.722e+004
1.394e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.112e+005
1.112e+005
1.649e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41 42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
16.75
16.75
17.77
0.7725
0.7725
2.039
12.94
12.94
36.24
(barrel/day)
4788
4788
0.0000
Mass Enthalpy
(Btu/lb)
-484.6
-484.6
-1655
Mass Entropy
(Btu/lb-F)
1.525
1.525
1.186
9.827
9.827
18.65
0.5866
0.5866
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.049
6635
6635
9277
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
5803
5803
7845
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
358.1
---
---
(psia)
40.73
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
18.67
18.67
---
(lbmole/ft3)
1.865
1.865
2.120
Specific Heat
(Btu/lbmole-F)
9.827
9.827
18.65
Std. Gas Flow
(MMSCFD)
7.864
7.864
0.0000
(lb/ft3)
31.25
31.25
37.68
(USGPS)
---
---
---
---
1.007
0.3816
10.42
10.42
12.17
---
---
---
0.0000
---
---
1.253
1.253
1.119
1.673
1.673
1.907
6063
---
Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP)
9.675e-002
9.675e-002
--0.1651
4.428e-002
4.428e-002
36.15
1.399e+006
1.399e+006
0.0000
0.0000
0.0000
1.000
1.295
1.295
0.4904
361.9
---
---
1.0000
1.0000
0.0000
---
---
4.891e-002
4.891e-002
2.006e-002
2.006e-002
22.44 0.2277 9.584e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 1 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 000 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
7.841
7.841
16.66
0.4680
0.4680
0.9377
5.874
5.874
9.781
0.3506
0.3506
0.5504
5.850
5.850
9.126
0.3492
0.3492
0.5135
1.680
1.680
2.044
---
---
511.5
---
---
1.399e+006 ---
1.399e+006 ---
23
4059 0.0000 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.1829
0.0002
5.1221
0.0004
0.4387
0.0002
30
H2O
0.0111
0.0000
0.1998
0.0000
0.0137
0.0000
31
Oxygen
121.3251
0.1402
3882.4021
0.2678
233.6677
0.1179
32
Methane
71.9227
0.0831
1153.8485
0.0796
263.8906
0.1331
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
318.8737
0.3686
642.8494
0.0443
630.0928
0.3178
35
Ethane
17.5827
0.0203
528.7093
0.0365
101.7823
0.0513
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
7.7207
0.0089
339.7837
0.0234
28.1897
0.0142
38
Nitrogen
215.2337
0.2488
6029.3408
0.4160
511.9783
0.2582
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0003
0.0000
0.0160
0.0000
0.0011
0.0000
42
Ammonia
112.3241
0.1298
1912.8795
0.1320
212.6061
0.1072
43
Total
865.1768
1.0000
14495.1511
1.0000
1982.6611
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.1829
0.0002
5.1221
0.0004
0.4387
0.0002
49
H2O
0.0111
0.0000
0.1998
0.0000
0.0137
0.0000
50
Oxygen
121.3251
0.1402
3882.4021
0.2678
233.6677
0.1179
51
Methane
71.9227
0.0831
1153.8485
0.0796
263.8906
0.1331
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
318.8737
0.3686
642.8494
0.0443
630.0928
0.3178
54
Ethane
17.5827
0.0203
528.7093
0.0365
101.7823
0.0513
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
7.7207
0.0089
339.7837
0.0234
28.1897
0.0142
57
Nitrogen
215.2337
0.2488
6029.3408
0.4160
511.9783
0.2582
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0003
0.0000
0.0160
0.0000
0.0011
0.0000
61
Ammonia
112.3241
0.1298
1912.8795
0.1320
212.6061
0.1072
62
Total
865.1768
1.0000
14495.1511
1.0000
1982.6611
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
0.0000
0.0097
0.0000
0.0098
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000 LIQUID VOLUME FRACTION 0.0000 0.0059
Page 2 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 000 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
Oxygen
0.0000
0.0278
0.0000
0.0501
0.0000
0.0266
16
Methane
0.0000
0.0203
0.0000
0.0183
0.0000
0.0369
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0000
0.0232
0.0000
0.0026
0.0000
0.0228
19
Ethane
0.0000
0.0162
0.0000
0.0274
0.0000
0.0465
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0000
0.0121
0.0000
0.0299
0.0000
0.0218
22
Nitrogen
0.0000
0.0112
0.0000
0.0176
0.0000
0.0132
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0000
0.0006
0.0000
0.0020
0.0000
0.0012
26
Ammonia
0.0000
0.8790
0.0000
0.8423
0.0000
0.8251
27
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
5.037
5.037
---
34
Methane
4.099
4.099
---
---
---
---
35
H2S
12.33
12.33
1.328e-003
---
1.328e-003
---
36
Hydrogen
15.86
15.86
---
37
Ethane
1.255
1.255
---
38
Propane
---
---
---
39
CO2
0.7400
0.7400
---
40
Nitrogen
22.30
22.30
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
45
5.275e-004
0.1477
---
0.1477
---
UNIT OPERATIONS
46 47 48
5.275e-004
FEED TO
PRODUCT FROM
Mixer:
MIX-104 Tee:
49
LOGICAL CONNECTION TEE-104
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
4565 psia 865.2 lbmole/hrMass:
1.450e+004 lb/hrStd Ideal Liq Volume:
1983 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 3 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
60.00
60.00
(psia)
414.7
414.7
440.7*
440.7
7642
7642
(lbmole/hr) (lb/hr)
1676 -3.254e+004 37.34
1676 -3.254e+004 37.34
(Btu/hr)
-1.434e+007
-1.434e+007
(barrel/day)
* 7.114e+005
7.114e+005
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-1876
-1876
30
Mass Entropy
(Btu/lb-F)
2.153
2.153
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
35
HHV Mass Basis (Std)
2.274e+004
2.274e+004
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
1.000
1.000
41
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
(Btu/lb)
201.3
---
44
Partial Pressure of CO2
(psia)
0.5811
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48
17.34 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
8.051e-002 1.396 2.340e+004
17.34 8.051e-002 1.396 2.340e+004
9.668
9.668
0.5575
0.5575
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
(ACFM)
91.23
91.23
(lbmole/ft3)
1.124
1.124
Specific Heat
(Btu/lbmole-F)
9.668
9.668
49
Std. Gas Flow
(MMSCFD)
4.006
4.006
50
Std. Ideal Liq. Mass Density
(lb/ft3)
19.49
19.49
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
0.9237
0.9237
53
Watson K
19.04
19.04
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.258
1.258
1.406
1.406
2673
---
0.5163
0.5163
4.592e-002
4.592e-002
7.114e+005
7.114e+005
0.0000
0.0000
(ft3/lbmole)
12.42
12.42
(Btu/lb)
154.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
1.944e-002
1.944e-002
1.155e-002
1.155e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 4 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 7.682
7.682
0.4430
0.4430
6.876
6.876
0.3965
0.3965
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
7.114e+005
7.114e+005
-38.94
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
399.3043
0.9061
6405.9987
0.8382
1465.0823
0.8741
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
32.8159
0.0745
986.7710
0.1291
189.9641
0.1133
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.6175
0.0014
27.1761
0.0036
2.2546
0.0013
38
Nitrogen
7.9393
0.0180
222.4045
0.0291
18.8854
0.0113
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
440.6770
1.0000
7642.3504
1.0000
1676.1864
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Methane
399.3043
0.9061
6405.9987
0.8382
1465.0823
0.8741
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
32.8159
0.0745
986.7710
0.1291
189.9641
0.1133
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6175
0.0014
27.1761
0.0036
2.2546
0.0013
57
Nitrogen
7.9393
0.0180
222.4045
0.0291
18.8854
0.0113
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
440.6770
1.0000
7642.3504
1.0000
1676.1864
1.0000
63
K VALUE
64 65
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 5 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Valve:
PIC-1
Tee:
LOGICAL CONNECTION TEE-101
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Active)
414.7 psia * Mass: 440.7 lbmole/hr
Molar:
37
7642 lb/hr Std Ideal Liq Volume:
1676 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 2
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
52.59
52.59
(psia)
306.7*
306.7
440.7
440.7
7642
7642
(lbmole/hr) (lb/hr)
1676 -3.254e+004 37.90
1676 -3.254e+004 37.90
(Btu/hr)
-1.434e+007
-1.434e+007
(barrel/day)
* 7.114e+005
7.114e+005
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.34
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
5.934e-002 1.029 3.174e+004 -1876
17.34 5.934e-002 1.029 3.174e+004 -1876
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 6 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 2 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
16
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
17
HHV Mass Basis (Std)
2.274e+004
2.274e+004
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
Phase Fraction [Vol. Basis]
1.000
1.000
23
Phase Fraction [Mass Basis]
1.000
1.000
24
Phase Fraction [Act. Vol. Basis]
1.000
1.000
25
Mass Exergy
(Btu/lb)
184.0
---
26
Partial Pressure of CO2
(psia)
0.4298
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.185
2.185
9.393
9.393
0.5416
0.5416
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
(ACFM)
123.8
123.8
(lbmole/ft3)
1.124
1.124
Specific Heat
(Btu/lbmole-F)
9.393
9.393
31
Std. Gas Flow
(MMSCFD)
4.006
4.006
32
Std. Ideal Liq. Mass Density
(lb/ft3)
19.49
19.49
33
Act. Liq. Flow
(USGPS)
---
---
34
Z Factor
0.9402
0.9402
35
Watson K
19.04
19.04
36
User Property
---
---
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.268
1.268
1.379
1.379
3065
---
0.6811
0.6811
4.592e-002
4.592e-002
7.114e+005
7.114e+005
0.0000
0.0000
(ft3/lbmole)
16.85
16.85
(Btu/lb)
176.7
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.869e-002
1.869e-002
1.123e-002
1.123e-002
7.407
7.407
0.4271
0.4271
6.813
6.813
0.3928
0.3928
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
7.114e+005 -31.43
62
7.114e+005 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
1.0000
LIQUID VOLUME FRACTION 0.0000
Page 7 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 2 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
399.3043
0.9061
6405.9987
0.8382
1465.0823
0.8741
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
32.8159
0.0745
986.7710
0.1291
189.9641
0.1133
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.6175
0.0014
27.1761
0.0036
2.2546
0.0013
23
Nitrogen
7.9393
0.0180
222.4045
0.0291
18.8854
0.0113
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
440.6770
1.0000
7642.3504
1.0000
1676.1864
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Methane
399.3043
0.9061
6405.9987
0.8382
1465.0823
0.8741
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
32.8159
0.0745
986.7710
0.1291
189.9641
0.1133
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.6175
0.0014
27.1761
0.0036
2.2546
0.0013
42
Nitrogen
7.9393
0.0180
222.4045
0.0291
18.8854
0.0113
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
440.6770
1.0000
7642.3504
1.0000
1676.1864
1.0000
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
---
---
---
52
H2O
---
---
---
53
Oxygen
---
---
---
54
Methane
---
---
---
---
---
---
55
H2S
56
Hydrogen
---
---
---
57
Ethane
---
---
---
58
Propane
---
---
---
59
CO2
---
---
---
60
Nitrogen
---
---
---
---
---
---
61
Air
62
Mercury
---
---
---
63
MEAmine
---
---
---
64
Ammonia
---
---
---
65
UNIT OPERATIONS
66 67 68 69
FEED TO Tee:
Aspen Technology Inc. Licensed to: LEGENDS
PRODUCT FROM TEE-102 Valve:
LOGICAL CONNECTION PIC-1
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 8 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 2 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Active):
18
Flow Specification
(Inactive) Molar:
* 306.7 psia
440.7 lbmole/hrMass:
19
7642 lb/hr Std Ideal Liq Volume:
1676 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: 3
28 29 30
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
39
Molar Enthalpy
(Btu/lbmole)
40
Molar Entropy
(Btu/lbmole-F)
41
Heat Flow
42
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
52.59
52.59
(psia)
306.7
306.7
2.635*
2.635
45.70
45.70
(lbmole/hr) (lb/hr)
(Btu/hr)
10.02 -3.254e+004 37.90 -8.576e+004 4255*
(barrel/day)
43
10.02 -3.254e+004 37.90 -8.576e+004 4255
PROPERTIES
44 45
Overall
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Vapour Phase 17.34
(lbmole/ft3)
17.34 5.934e-002
1.029
1.029
(barrel/day)
189.8
189.8
Mass Enthalpy
(Btu/lb)
-1876
-1876
51
Mass Entropy
(Btu/lb-F)
2.185
2.185
52
Heat Capacity
53
Mass Heat Capacity
54
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
55
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
56
HHV Mass Basis (Std)
2.274e+004
2.274e+004
57
CO2 Loading
58
CO2 App ML Con
59
CO2 App WT Con
60
LHV Mass Basis (Std)
61
Phase Fraction [Vol. Basis]
1.000
1.000
62
Phase Fraction [Mass Basis]
1.000
1.000
63
Phase Fraction [Act. Vol. Basis]
1.000
1.000
64
Mass Exergy
(Btu/lb)
184.0
---
65
Partial Pressure of CO2
(psia)
0.4298
---
66
Cost Based on Flow
(Cost/s)
0.0000
0.0000
67
Act. Gas Flow
(ACFM)
0.7402
0.7402
68
Avg. Liq. Density
(lbmole/ft3)
1.124
1.124
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
5.934e-002
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
9.393
9.393
0.5416
0.5416
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 9 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 3 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Specific Heat
(Btu/lbmole-F)
13
Std. Gas Flow
(MMSCFD)
14
Std. Ideal Liq. Mass Density
15
Act. Liq. Flow
16
Z Factor
17
Watson K
18
User Property
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
41
True VP at 37.8 C
42
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
43
Viscosity Index
Vapour Phase 9.393
2.396e-002
9.393 2.396e-002
(lb/ft3)
19.49
(USGPS)
---
---
0.9402
0.9402
19.04
19.04
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
0.0000
---
1.268
1.268
1.379
1.379
3065
---
0.6811
0.6811
4.592e-002
(barrel/day)
19.49
4.592e-002
4255
4255
0.0000
0.0000
(ft3/lbmole)
16.85
16.85
(Btu/lb)
176.7
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.869e-002
1.869e-002
1.123e-002
1.123e-002
7.407
7.407
0.4271
0.4271
6.813
6.813
0.3928
0.3928
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
4255
4255
-31.43
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
44
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
50
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Methane
2.3879
0.9061
38.3088
0.8382
8.7614
0.8741
54
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Ethane
0.1962
0.0745
5.9010
0.1291
1.1360
0.1133
57
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
CO2
0.0037
0.0014
0.1625
0.0036
0.0135
0.0013
59
Nitrogen
0.0475
0.0180
1.3300
0.0291
0.1129
0.0113
60
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Total
2.6353
1.0000
45.7024
1.0000
10.0238
1.0000
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 10 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 3 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
2.3879
0.9061
38.3088
0.8382
8.7614
0.8741
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.1962
0.0745
5.9010
0.1291
1.1360
0.1133
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0037
0.0014
0.1625
0.0036
0.0135
0.0013
24
Nitrogen
0.0475
0.0180
1.3300
0.0291
0.1129
0.0113
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2.6353
1.0000
45.7024
1.0000
10.0238
1.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Component Splitter:
D-4A
51
Tee:
LOGICAL CONNECTION TEE-102
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Active)
61
306.7 psia Molar:
* Mass: 2.635 lbmole/hr
45.70 lb/hr Std Ideal Liq Volume:
10.02 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 11 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 4
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
52.59
52.59
(psia)
306.7
306.7
438.0
438.0
7597
7597
(lbmole/hr) (lb/hr)
1666 -3.254e+004 37.90
1666 -3.254e+004 37.90
(Btu/hr)
-1.425e+007
-1.425e+007
(barrel/day)
* 7.072e+005
7.072e+005
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-1876
-1876
30
Mass Entropy
(Btu/lb-F)
2.185
2.185
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
35
HHV Mass Basis (Std)
2.274e+004
2.274e+004
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
1.000
1.000
41
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
(Btu/lb)
184.0
---
44
Partial Pressure of CO2
(psia)
0.4298
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48
17.34 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
5.934e-002 1.029 3.155e+004
17.34 5.934e-002 1.029 3.155e+004
9.393
9.393
0.5416
0.5416
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
(ACFM)
123.0
123.0
(lbmole/ft3)
1.124
1.124
Specific Heat
(Btu/lbmole-F)
9.393
9.393
49
Std. Gas Flow
(MMSCFD)
3.982
3.982
50
Std. Ideal Liq. Mass Density
(lb/ft3)
19.49
19.49
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
0.9402
0.9402
53
Watson K
19.04
19.04
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.268
1.268
1.379
1.379
3065
---
0.6811
0.6811
4.592e-002
4.592e-002
7.072e+005
7.072e+005
0.0000
0.0000
(ft3/lbmole)
16.85
16.85
(Btu/lb)
176.7
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
1.869e-002
1.869e-002
1.123e-002
1.123e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 12 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 4 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 7.407
7.407
0.4271
0.4271
6.813
6.813
0.3928
0.3928
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
7.072e+005
7.072e+005
-31.43
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
396.9164
0.9061
6367.6899
0.8382
1456.3209
0.8741
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
32.6197
0.0745
980.8700
0.1291
188.8281
0.1133
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.6138
0.0014
27.0136
0.0036
2.2412
0.0013
38
Nitrogen
7.8919
0.0180
221.0745
0.0291
18.7724
0.0113
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
438.0417
1.0000
7596.6480
1.0000
1666.1625
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Methane
396.9164
0.9061
6367.6899
0.8382
1456.3209
0.8741
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
32.6197
0.0745
980.8700
0.1291
188.8281
0.1133
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6138
0.0014
27.0136
0.0036
2.2412
0.0013
57
Nitrogen
7.8919
0.0180
221.0745
0.0291
18.7724
0.0113
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
438.0417
1.0000
7596.6480
1.0000
1666.1625
1.0000
63
K VALUE
64 65
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 13 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 4 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Component Splitter:
D-4B
LOGICAL CONNECTION
Tee:
TEE-102
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
306.7 psia 438.0 lbmole/hrMass:
37
7597 lb/hr Std Ideal Liq Volume:
1666 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 5
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.0067
0.0067
0.9933
(F)
308.1
308.1
308.1
(psia)
414.7*
414.7
414.7
482.2
3.250
479.0
8686
56.74
8629
602.8
10.75
592.1
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-1.182e+005 19.72 -5.698e+007 590.4*
(barrel/day)
61
-4.404e+004 41.52 -1.431e+005 5243
-1.187e+005 19.58 -5.684e+007 582.2
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 18.01
(lbmole/ft3) (lb/ft3)
2.230
17.46 5.158e-002
Aqueous Phase 18.02 3.126
40.17
0.9005
56.31
(barrel/day)
924.4
269.4
655.0
(Btu/lb)
-6560
-2523
-6587
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 14 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 5 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
(Btu/lb-F)
Vapour Phase
Aqueous Phase
1.095
2.378
1.087
19.63
10.41
19.69
(Btu/lb-F)
1.090
0.5965
1.093
LHV Molar Basis (Std)
(Btu/lbmole)
1959
16
HHV Molar Basis (Std)
(Btu/lbmole)
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
(lbmole/ft3)
1.708e-005
20
CO2 App WT Con
(lbmol/lb)
4.252e-007
21
LHV Mass Basis (Std)
22
Phase Fraction [Vol. Basis]
23
Phase Fraction [Mass Basis]
24
Phase Fraction [Act. Vol. Basis]
25
Mass Exergy
26
Partial Pressure of CO2
27
Cost Based on Flow
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
(psia)
59
True VP at 37.8 C
(psia)
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(Btu/lbmole-F)
(Btu/lb)
1.969e+004 1093 ---
(Btu/lb)
2.892e+005 3.216e+005 1.842e+004 ---
108.8
9.484 1.764e+004 979.2 ---
---
8.726e-006
---
1.550e-007
1.657e+004
0.5265
1.783e-002
1.783e-002
0.9822
6.533e-003
6.533e-003
0.9935
0.2914
0.2914
0.7086
(Btu/lb)
43.83
---
---
(psia)
0.3006
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1.050
1.050
---
(lbmole/ft3)
3.420
1.293
3.458
Specific Heat
(Btu/lbmole-F)
19.63
10.41
19.69
Std. Gas Flow
(MMSCFD)
4.384
2.954e-002
4.354
(lb/ft3)
61.59
22.57
62.30
(USGPS)
0.3184
---
0.3184
(psia)
(Btu/lbmole)
---
0.9759
19.04
19.07
15.22
---
---
---
0.0000
---
---
1.113
1.236
1.112
1.003
1.285
1.187
2.549e+004
(cSt)
---
(lb/ft3)
62.88
(barrel/day) (ft3/lbmole) (Btu/lb)
1.610e-002
---
---
1.048
0.1960
4.626e-002
63.35
590.4
5243
0.9933
0.0000
582.2 1.000
0.4484
19.39
0.3199
1415
---
---
0.0067
0.0067
0.9933
(dyne/cm)
47.97
(Btu/hr-ft-F)
---
2.865e-002
0.3964
---
1.512e-002
0.1768
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
47.97
17.64
8.429
17.71
0.9796
0.4828
0.9828
19.57
8.104
16.59
1.086
0.4642
0.9207
20.83
---
16.30
1.156
---
0.9048
0.9425
---
1.208
---
---
---
---
---
---
5826
5243
582.2
---
---
---
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
0.0067
LIQUID VOLUME FRACTION 0.0000
Page 15 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 5 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
0.0067
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
H2O
479.5977
0.9945
8640.0000
0.9947
592.7991
0.9834
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
2.3879
0.0050
38.3088
0.0044
8.7614
0.0145
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
0.1962
0.0004
5.9010
0.0007
1.1360
0.0019
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.0037
0.0000
0.1625
0.0000
0.0135
0.0000
23
Nitrogen
0.0475
0.0001
1.3300
0.0002
0.1129
0.0002
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
482.2330
1.0000
8685.7024
1.0000
602.8230
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
6.740e-003 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
H2O
0.6311
0.1942
11.3702
0.2004
0.7801
0.0726
35
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Methane
2.3750
0.7308
38.1025
0.6715
8.7142
0.8109
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
0.1961
0.0603
5.8959
0.1039
1.1350
0.1056
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0024
0.0007
0.1037
0.0018
0.0086
0.0008
42
Nitrogen
0.0454
0.0140
1.2719
0.0224
0.1080
0.0101
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
3.2500
1.0000
56.7441
1.0000
10.7460
1.0000
48
Aqueous Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9933 LIQUID VOLUME FRACTION
52
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
H2O
478.9665
1.0000
8628.6298
1.0000
592.0190
0.9999
54
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Methane
0.0129
0.0000
0.2063
0.0000
0.0472
0.0001
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Ethane
0.0002
0.0000
0.0051
0.0000
0.0010
0.0000
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
0.0013
0.0000
0.0588
0.0000
0.0049
0.0000
61
Nitrogen
0.0021
0.0000
0.0581
0.0000
0.0049
0.0000
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Total
478.9830
1.0000
8628.9582
1.0000
592.0770
1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 16 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 5 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.1942
---
0.1942
---
---
14
Oxygen
15
Methane
16
2.722e+004
H2S
---
---
---
---
---
---
2.722e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
259.7
---
259.7
21
Nitrogen
3224
---
3224
---
---
---
22
1.689e+005
Air
---
---
1.689e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Mixer:
LOGICAL CONNECTION
MIX-105 Component Splitter:
30
D-4A
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 414.7 psia
482.2 lbmole/hrMass:
40
8686 lb/hr Std Ideal Liq Volume:
602.8 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 6
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.4952
0.4952
0.5048
(F)
209.1
209.1
209.1
(psia)
414.7*
414.7
414.7
917.6
454.5
463.2
(lbmole/hr) (lb/hr)
1.624e+004
(barrel/day)
(Btu/hr)
2259 -7.753e+004 28.36 -7.115e+007 2196*
(barrel/day)
64
7892
8344
1686
572.5
-3.367e+004 40.01 -1.530e+007 7.337e+005
-1.206e+005 16.92 -5.585e+007 563.0
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.69
(lbmole/ft3)
0.1182
17.37 5.963e-002
Aqueous Phase 18.02 3.294
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 17 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 6 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-4382
-1939
-6693
15
Mass Entropy
(Btu/lb-F)
1.603
2.304
0.9393
16
Heat Capacity
14.54
10.12
18.88
17
Mass Heat Capacity
0.8219
0.5829
1.048
18
LHV Molar Basis (Std)
(Btu/lbmole)
1.711e+005
3.455e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
1.974e+005
3.807e+005
20
HHV Mass Basis (Std)
1.116e+004
2.192e+004
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
---
24
LHV Mass Basis (Std)
(Btu/lb)
9670
25
Phase Fraction [Vol. Basis]
0.7466
0.7466
26
Phase Fraction [Mass Basis]
0.4861
0.4861
27
Phase Fraction [Act. Vol. Basis]
0.9819
0.9819
28
Mass Exergy
(Btu/lb)
109.7
---
29
Partial Pressure of CO2
(psia)
0.5576
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.092 3.318e+004
1.036 3.258e+004
59.34 601.1
1.617 1.763e+004 978.8
---
---
---
---
1.994e-005
---
3.361e-007
1.989e+004
---
8.975e-002 0.2534 0.5139 1.812e-002 ---
(ACFM)
127.0
127.0
---
(lbmole/ft3)
1.736
1.152
3.458
Specific Heat
(Btu/lbmole-F)
14.54
10.12
18.88
Std. Gas Flow
(MMSCFD)
8.341
4.131
4.210
(lb/ft3)
30.72
20.00
62.30
(USGPS)
0.2922
---
0.2922
(psia)
(Btu/lbmole)
---
0.9690
19.04
19.04
9.822
---
---
---
0.0000
---
---
1.158
1.244
1.118
1.090
1.309
1.173
1.689e+004
1.754e-002
---
---
0.8425
0.2986
(cSt)
---
(lb/ft3)
31.61
4.598e-002
63.35
2196
7.337e+005
563.0
(barrel/day) (ft3/lbmole) (Btu/lb)
0.5048
0.0000
1.000
8.458
16.77
0.3036
954.4
---
---
0.4952
0.4952
0.5048
(dyne/cm)
58.91
(Btu/hr-ft-F)
---
2.577e-002
0.3929
---
1.398e-002
0.2838
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
58.91
12.56
8.137
16.89
0.7096
0.4686
0.9376
13.35
7.735
16.09
0.7543
0.4454
0.8930
---
---
15.48
---
---
0.8595
---
---
1.219
---
---
---
---
---
7.342e+005 -23.56
7.337e+005 ---
--563.0 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 18 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 6 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.4952
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
479.5977
0.5226
8640.0000
0.5321
592.7991
0.2624
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
396.9164
0.4325
6367.6899
0.3922
1456.3209
0.6447
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
32.6197
0.0355
980.8700
0.0604
188.8281
0.0836
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6138
0.0007
27.0136
0.0017
2.2412
0.0010
24
Nitrogen
7.8919
0.0086
221.0745
0.0136
18.7724
0.0083
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
917.6394
1.0000
1.0000
2258.9617
1.0000
16236.6480
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.4952 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
16.4179
0.0361
295.7705
0.0375
20.2931
0.0120
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
396.9142
0.8734
6367.6555
0.8068
1456.3130
0.8635
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
32.6196
0.0718
980.8696
0.1243
188.8280
0.1120
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6110
0.0013
26.8902
0.0034
2.2309
0.0013
43
Nitrogen
7.8900
0.0174
221.0226
0.0280
18.7680
0.0111
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
454.4528
1.0000
7892.2084
1.0000
1686.4330
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.5048 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
463.1797
1.0000
8344.2295
1.0000
572.5060
1.0000
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0021
0.0000
0.0344
0.0000
0.0079
0.0000
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0028
0.0000
0.1234
0.0000
0.0102
0.0000
62
Nitrogen
0.0019
0.0000
0.0519
0.0000
0.0044
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
463.1866
1.0000
8344.4396
1.0000
572.5286
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 19 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 6 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
CO
13
H2O
HEAVY ---
3.613e-002
14
Oxygen
15
Methane
16
LIGHT -----
3.613e-002
---
1.885e+005
H2S
---
---
---
---
---
---
---
---
1.885e+005 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
222.1
---
222.1
21
Nitrogen
4338
---
4338
---
---
---
22
2.473e+006
Air
---
---
2.473e+006
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Mixer:
LOGICAL CONNECTION
MIX-105 Component Splitter:
30
D-4B
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 414.7 psia
917.6 lbmole/hrMass:
40
1.624e+004 lb/hrStd Ideal Liq Volume:
2259 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 7
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.3364
0.3364
0.6636
(F)
239.7
239.7
239.7
(psia)
414.7
414.7
414.7
1400
471.0
(lbmole/hr) (lb/hr)
(Btu/hr)
2.492e+004 2862 -9.153e+004 25.43 -1.281e+008 2587*
(barrel/day)
64
8188 1714 -3.540e+004 40.53 -1.667e+007 7.603e+005
928.9 1.673e+004 1148 -1.200e+005 17.77 -1.115e+008 1129
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.80
(lbmole/ft3)
0.1631
17.39 5.678e-002
Aqueous Phase 18.02 3.244
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 20 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 7 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
1.128e+005
3.354e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
1.362e+005
3.701e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
---
24
LHV Mass Basis (Std)
(Btu/lb)
6338
25
Phase Fraction [Vol. Basis]
0.5988
0.5988
26
Phase Fraction [Mass Basis]
0.3285
0.3285
27
Phase Fraction [Act. Vol. Basis]
0.9666
0.9666
28
Mass Exergy
(Btu/lb)
85.37
---
29
Partial Pressure of CO2
(psia)
0.5393
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
2.904 3.668e+004
0.9871 3.546e+004
58.44 1224
(Btu/lb)
-5141
-2036
-6660
(Btu/lb-F)
1.428
2.331
0.9863
16.10
10.25
19.07
0.9043
0.5893
1.058
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
7651
2.129e+004
3.015 1.763e+004 978.8
---
---
---
---
1.743e-005
---
2.983e-007
1.929e+004
---
0.1674 0.4012 0.6715 3.337e-002 ---
(ACFM)
138.3
138.3
---
(lbmole/ft3)
2.091
1.175
3.458
Specific Heat
(Btu/lbmole-F)
16.10
10.25
19.07
Std. Gas Flow
(MMSCFD)
12.72
4.281
8.444
(lb/ft3)
37.23
20.43
62.30
(USGPS)
0.5950
---
0.5950
(psia)
(Btu/lbmole)
---
0.9732
19.04
19.04
11.17
---
---
---
0.0000
---
---
1.141
1.240
1.116
1.053
1.297
1.177
1.993e+004
---
---
0.9107
0.2562
(cSt)
---
(lb/ft3)
41.18
4.604e-002
2587
7.603e+005
(barrel/day)
1.703e-002
63.36 1129
0.6636
0.0000
1.000
(ft3/lbmole)
6.130
17.61
0.3083
(Btu/lb)
1119
---
---
0.3364
0.3364
0.6636
(dyne/cm)
55.65
(Btu/hr-ft-F)
---
2.692e-002
0.3962
---
1.440e-002
0.2398
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
55.65
14.11
8.260
17.08
0.7928
0.4751
0.9482
15.29
7.897
16.20
0.8589
0.4542
0.8991
---
---
15.39
---
---
0.8544
---
---
1.239
---
---
---
---
---
7.614e+005 ---
7.603e+005 ---
--1129 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 21 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 7 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
959.1953
0.6852
17
Oxygen
0.0000
0.0000
18
Methane
399.3043
19
H2S
20
Hydrogen
21
Ethane
22
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.3364
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.6934
1185.5983
0.4143
0.0000
0.0000
0.0000
0.0000
0.2852
6405.9987
0.2570
1465.0823
0.5119
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0234
986.7710
0.0396
189.9641
0.0664
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6175
0.0004
27.1761
0.0011
2.2546
0.0008
24
Nitrogen
7.9393
0.0057
222.4045
0.0089
18.8854
0.0066
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1399.8723
1.0000
1.0000
2861.7846
1.0000
17280.0000
24922.3504
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.3364 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
30.3074
0.0644
545.9916
0.0667
37.4610
0.0219
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
399.2963
0.8478
6405.8704
0.7824
1465.0529
0.8550
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
32.8158
0.0697
986.7690
0.1205
189.9637
0.1109
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6125
0.0013
26.9565
0.0033
2.2364
0.0013
43
Nitrogen
7.9355
0.0168
222.2980
0.0271
18.8763
0.0110
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
470.9676
1.0000
8187.8855
1.0000
1713.5904
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
53
CO
0.0000
0.0000
54
H2O
928.8879
1.0000
55
Oxygen
0.0000
0.0000
56
Methane
0.0080
57
H2S
58
MASS FLOW (lb/hr) 0.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.6636 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1148.1372
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.1284
0.0000
0.0294
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0001
0.0000
0.0019
0.0000
0.0004
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0050
0.0000
0.2197
0.0000
0.0182
0.0000
62
Nitrogen
0.0038
0.0000
0.1065
0.0000
0.0090
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
928.9047
1.0000
1.0000
1148.1942
1.0000
16734.0084
16734.4649
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 22 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 7 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
CO
13
H2O Oxygen
15
Methane
---
---
---
6.435e-002
---
9.843e+004
H2S
HEAVY ---
6.435e-002
14
16
LIGHT ---
---
---
---
---
---
---
9.843e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
242.0
---
242.0
21
Nitrogen
4116
---
4116
---
---
---
22
9.999e+005
Air
---
---
9.999e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Mixer:
MIX-106 Mixer:
LOGICAL CONNECTION MIX-105
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
414.7 psia 1400 lbmole/hrMass:
40
2.492e+004 lb/hrStd Ideal Liq Volume:
2862 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 8
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
310.0*
310.0
(psia)
364.7
364.7
(lbmole/hr) (lb/hr)
(Btu/hr)
1918 3.456e+004 2371 -1.186e+005 19.63 -2.276e+008 2332*
(barrel/day)
64
1918 3.456e+004 2371 -1.186e+005 19.63 -2.276e+008 2332
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Aqueous Phase 18.02
18.02
3.122
3.122
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 23 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 8 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
(lb/ft3)
Aqueous Phase 56.24
56.24
(barrel/day)
2627
2627
(Btu/lb)
-6585
-6585
(Btu/lb-F)
1.089
1.089
19.72
19.72
(Btu/lbmole-F) (Btu/lb-F)
1.095
1.095
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
19
HHV Molar Basis (Std)
(Btu/lbmole)
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
26
Phase Fraction [Mass Basis]
0.0000
1.000
27
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
28
Mass Exergy
(Btu/lb)
43.03
---
29
Partial Pressure of CO2
(psia)
0.0000
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
---
---
39
User Property
---
---
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.72
19.72
Std. Gas Flow
(MMSCFD)
17.44
17.44
(lb/ft3)
62.30
62.30
(USGPS)
1.277 1.414e-002
(psia)
(Btu/lbmole)
1.277 1.414e-002
0.0000
---
1.112
1.112
1.188
1.188
1.445e+004
---
(cSt)
0.1949
0.1949
(lb/ft3)
63.35
63.35
(barrel/day)
2332
2332
1.000
1.000
(ft3/lbmole)
0.3203
0.3203
(Btu/lb)
802.3
---
0.0000
1.0000
(dyne/cm)
47.75
47.75
(Btu/hr-ft-F)
0.3962
0.3962
0.1755
0.1755
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
17.73
17.73
0.9844
0.9844
16.60
16.60
0.9216
0.9216
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
2332
2332
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 24 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 8 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
1918.3906
1.0000
17
Oxygen
0.0000
0.0000
18
Methane
0.0000
19
H2S
20
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2371.1965
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1918.3906
1.0000
1.0000
2371.1965
1.0000
30
0.0000
Vapour Fraction
34560.0000
34560.0000
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
34
CO
0.0000
0.0000
35
H2O
1918.3906
1.0000
36
Oxygen
0.0000
0.0000
37
Methane
0.0000
38
H2S
39
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2371.1965
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
1918.3906
1.0000
1.0000
2371.1965
1.0000
49
34560.0000
34560.0000
K VALUE
50 51
0.0000
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
0.0000
---
0.0000
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 25 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 8 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Tee:
TEE-103 LNG:
LOGICAL CONNECTION LNG-101
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
364.7 psia 1918 lbmole/hrMass:
23
3.456e+004 lb/hrStd Ideal Liq Volume:
2371 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 9
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
310.0
310.0
(psia)
364.7
364.7
(lbmole/hr) (lb/hr)
(Btu/hr)
959.2 * 1.728e+004
1186 -1.186e+005 19.63 -1.138e+008 1166*
(barrel/day)
47
959.2 1.728e+004 1186 -1.186e+005 19.63 -1.138e+008 1166
PROPERTIES
48 49
Overall
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
55
Mass Entropy
56
Heat Capacity
57
Mass Heat Capacity
58
(lbmole/ft3) (lb/ft3)
Aqueous Phase 18.02
18.02
3.122
3.122
56.24
56.24
(barrel/day)
1313
1313
(Btu/lb)
-6585
-6585
(Btu/lb-F)
1.089
1.089
19.72
19.72
(Btu/lbmole-F) (Btu/lb-F)
1.095
1.095
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
66
Phase Fraction [Mass Basis]
0.0000
1.000
67
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
68
Mass Exergy
43.03
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 26 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 9 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Aqueous Phase
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
---
---
22
User Property
---
---
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
(psia)
0.0000
---
(Cost/s)
0.0000
0.0000
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.72
19.72
Std. Gas Flow
(MMSCFD)
8.719
8.719
(lb/ft3)
62.30
62.30
(USGPS)
0.6385
0.6385
1.414e-002
(psia)
(Btu/lbmole)
1.414e-002
0.0000
---
1.112
1.112
1.188
1.188
1.445e+004
---
(cSt)
0.1949
0.1949
(lb/ft3)
63.35
63.35
(barrel/day)
1166
1166
1.000
1.000
(ft3/lbmole)
0.3203
0.3203
(Btu/lb)
802.3
---
0.0000
1.0000
(dyne/cm)
47.75
47.75
(Btu/hr-ft-F)
0.3962
0.3962
0.1755
0.1755
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
17.73
17.73
0.9844
0.9844
16.60
16.60
0.9216
0.9216
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
1166
1166
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
54
CO
0.0000
0.0000
55
H2O
959.1953
1.0000
56
Oxygen
0.0000
0.0000
57
Methane
0.0000
58
H2S
59
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1185.5983
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
959.1953
1.0000
1.0000
1185.5983
69
Aspen Technology Inc. Licensed to: LEGENDS
0.0000
Vapour Fraction
17280.0000
17280.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 27 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 9 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Aqueous Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
959.1953
1.0000
17
Oxygen
0.0000
0.0000
18
Methane
0.0000
19
H2S
20
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
0.0000
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1185.5983
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
959.1953
1.0000
1.0000
1185.5983
1.0000
17280.0000
17280.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
0.0000
---
0.0000
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Mixer:
MIX-106 Tee:
51
LOGICAL CONNECTION TEE-103
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Active)
61
364.7 psia Molar:
959.2 lbmole/hrMass:
1.728e+004 *lb/hrStd Ideal Liq Volume:
1186 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 28 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 10
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
310.0
310.0
(psia)
364.7
364.7
(lbmole/hr) (lb/hr)
(Btu/hr)
959.2 1.728e+004 1186 -1.186e+005 19.63 -1.138e+008 1166*
(barrel/day)
22
959.2 1.728e+004 1186 -1.186e+005 19.63 -1.138e+008 1166
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
30
Mass Entropy
31
Heat Capacity
32
Mass Heat Capacity
33
(lbmole/ft3) (lb/ft3)
Aqueous Phase 18.02
18.02
3.122
3.122
56.24
56.24
(barrel/day)
1313
1313
(Btu/lb)
-6585
-6585
(Btu/lb-F)
1.089
1.089
19.72
19.72
(Btu/lbmole-F) (Btu/lb-F)
1.095
1.095
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
34
HHV Molar Basis (Std)
(Btu/lbmole)
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
43.03
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
---
---
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.72
19.72
Std. Gas Flow
(MMSCFD)
8.719
8.719
Licensed to: LEGENDS
(lb/ft3)
62.30
62.30
(USGPS)
0.6385
0.6385
1.414e-002
(psia)
(Btu/lbmole)
1.414e-002
0.0000
---
1.112
1.112
1.188
1.188
1.445e+004
---
(cSt)
0.1949
0.1949
(lb/ft3)
63.35
63.35
(barrel/day)
1166
1166
1.000
1.000
(ft3/lbmole)
0.3203
0.3203
(Btu/lb)
802.3
---
0.0000
1.0000
(dyne/cm)
47.75
47.75
(Btu/hr-ft-F)
0.3962
0.3962
0.1755
0.1755
(cP)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 29 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 10 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Aqueous Phase 17.73
17.73
0.9844
0.9844
16.60
16.60
0.9216
0.9216
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
1166
1166
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
29
CO
0.0000
0.0000
30
H2O
959.1953
1.0000
31
Oxygen
0.0000
0.0000
32
Methane
0.0000
33
H2S
34
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1185.5983
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
959.1953
1.0000
1.0000
1185.5983
1.0000
44
0.0000
Vapour Fraction
17280.0000
17280.0000
Aqueous Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
48
CO
0.0000
0.0000
49
H2O
959.1953
1.0000
50
Oxygen
0.0000
0.0000
51
Methane
0.0000
52
H2S
53
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1185.5983
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
959.1953
1.0000
1.0000
1185.5983
1.0000
63
17280.0000
17280.0000
K VALUE
64 65
0.0000
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
0.0000
---
0.0000
---
---
68 69
Oxygen
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 30 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 10 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Tee:
LOGICAL CONNECTION
TEE-106 Tee:
TEE-103
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
364.7 psia 959.2 lbmole/hrMass:
37
1.728e+004 lb/hrStd Ideal Liq Volume:
1186 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 11
46 47 48
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.2092
0.2092
0.7908
(F)
262.1
262.1
262.1
(psia)
364.7
364.7
364.7
2359
493.5
(lbmole/hr) (lb/hr)
(Btu/hr)
4.220e+004 4047 -1.025e+005 23.15 -2.419e+008 3664*
(barrel/day)
61
8594 1741 -3.824e+004 41.18 -1.887e+007 7.965e+005
1866 3.361e+004 2306 -1.196e+005 18.38 -2.230e+008 2268
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
0.2179 3.898 4.628e+004 -5732
17.41 4.817e-002 0.8388 4.380e+004 -2196
Aqueous Phase 18.02 3.206 57.75 2488 -6637
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 31 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 11 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
3.201e+005
16
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
3.540e+005
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
(lbmole/ft3)
20
CO2 App WT Con
(lbmol/lb)
---
21
LHV Mass Basis (Std)
(Btu/lb)
3743
22
Phase Fraction [Vol. Basis]
0.4303
0.4303
23
Phase Fraction [Mass Basis]
0.2036
0.2036
24
Phase Fraction [Act. Vol. Basis]
0.9463
0.9463
25
Mass Exergy
(Btu/lb)
65.71
---
26
Partial Pressure of CO2
(psia)
0.4503
---
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
(psia)
59
True VP at 37.8 C
(psia)
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.294
2.365
1.020
17.36
10.25
19.24
0.9706
0.5888
1.068
4919
2.033e+004
3.985 1.764e+004 978.9
---
---
---
---
1.394e-005
---
2.414e-007
1.838e+004
---
0.2212 0.5697 0.7964 5.375e-002 ---
(ACFM)
170.8
170.8
---
(lbmole/ft3)
2.492
1.211
3.458
Specific Heat
(Btu/lbmole-F)
17.36
10.25
19.24
Std. Gas Flow
(MMSCFD)
21.44
4.486
16.96
(lb/ft3)
44.57
21.10
62.30
(USGPS)
1.209
---
---
0.9776
19.04
19.04
12.33
---
---
---
0.0000
---
---
1.129
1.240
1.115
1.030
1.287
1.180
(psia)
(Btu/lbmole)
2.234e+004
---
---
1.086
0.2323
(cSt)
---
(lb/ft3)
49.23
4.612e-002
3664
7.965e+005
(barrel/day)
1.209 1.469e-002
63.35 2268
0.7908
0.0000
1.000
(ft3/lbmole)
4.590
20.76
0.3119
(Btu/lb)
1249
---
---
0.2092
0.2092
0.7908
(dyne/cm)
53.19
(Btu/hr-ft-F)
---
2.736e-002
0.3973
---
1.458e-002
0.2149
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
53.19
15.38
8.268
17.26
0.8596
0.4748
0.9580
16.87
7.965
16.30
0.9428
0.4574
0.9050
---
---
14.67
---
---
0.8142
---
---
1.312
---
---
---
---
---
7.988e+005 ---
7.965e+005 ---
62
--2268 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
0.2092
LIQUID VOLUME FRACTION 0.0000
Page 32 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 11 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
0.2092
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
H2O
1918.3906
0.8132
0.8189
2371.1965
0.5859
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
399.3043
0.1693
6405.9987
0.1518
1465.0823
0.3620
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
23
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
34560.0000
42202.3504
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
H2O
52.8597
0.1071
952.2721
0.1108
65.3364
0.0375
35
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Methane
399.2831
0.8091
6405.6590
0.7454
1465.0046
0.8413
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
32.8157
0.0665
986.7648
0.1148
189.9629
0.1091
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.6094
0.0012
26.8191
0.0031
2.2250
0.0013
42
Nitrogen
7.9325
0.0161
222.2130
0.0259
18.8691
0.0108
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
493.5004
1.0000
8593.7281
1.0000
1741.3979
1.0000
48
Aqueous Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
52
CO
0.0000
0.0000
53
H2O
1865.5310
1.0000
54
Oxygen
0.0000
0.0000
55
Methane
0.0212
56
H2S
57
MASS FLOW (lb/hr) 0.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7908 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2305.8602
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.3398
0.0000
0.0777
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Ethane
0.0002
0.0000
0.0062
0.0000
0.0012
0.0000
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
0.0081
0.0000
0.3570
0.0000
0.0296
0.0000
61
Nitrogen
0.0068
0.0000
0.1915
0.0000
0.0163
0.0000
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Total
1865.5673
1.0000
1.0000
2305.9849
1.0000
33607.7279
33608.6223
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 33 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 11 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.1071
---
0.1071
---
---
14
Oxygen
15
Methane
16
7.127e+004
H2S
---
---
---
---
---
---
7.127e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
284.0
---
284.0
21
Nitrogen
4387
---
4387
---
---
---
22
6.040e+005
Air
---
---
6.040e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO Component Splitter:
PRODUCT FROM
LOGICAL CONNECTION
V-080 COBALTO MOLIBDENO Mixer:
MIX-106
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
364.7 psia 2359 lbmole/hrMass:
40
4.220e+004 lb/hrStd Ideal Liq Volume:
4047 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 12
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.2092
0.2092
0.7908
(F)
262.1
262.1
262.1
(psia)
364.7*
364.7
364.7
2359
493.5
(lbmole/hr) (lb/hr)
(Btu/hr)
4.220e+004 4047 -1.025e+005 23.15 -2.419e+008 3664*
(barrel/day)
64
8594 1741 -3.824e+004 41.18 -1.887e+007 7.965e+005
1866 3.361e+004 2306 -1.196e+005 18.38 -2.230e+008 2268
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3)
0.2179
17.41 4.817e-002
Aqueous Phase 18.02 3.206
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 34 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 12 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
3.201e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
3.540e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
---
24
LHV Mass Basis (Std)
(Btu/lb)
3743
25
Phase Fraction [Vol. Basis]
0.4303
0.4303
26
Phase Fraction [Mass Basis]
0.2036
0.2036
27
Phase Fraction [Act. Vol. Basis]
0.9463
0.9463
28
Mass Exergy
(Btu/lb)
65.71
---
29
Partial Pressure of CO2
(psia)
0.4503
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
3.898 4.628e+004
0.8388 4.380e+004
57.75 2488
(Btu/lb)
-5732
-2196
-6637
(Btu/lb-F)
1.294
2.365
1.020
17.36
10.25
19.24
0.9706
0.5888
1.068
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
4919
2.033e+004
3.985 1.764e+004 978.9
---
---
---
---
1.394e-005
---
2.414e-007
1.838e+004
---
0.2212 0.5697 0.7964 5.375e-002 ---
(ACFM)
170.8
170.8
---
(lbmole/ft3)
2.492
1.211
3.458
Specific Heat
(Btu/lbmole-F)
17.36
10.25
19.24
Std. Gas Flow
(MMSCFD)
21.44
4.486
16.96
(lb/ft3)
44.57
21.10
62.30
(USGPS)
1.209
---
---
0.9776
19.04
19.04
12.33
---
---
---
0.0000
---
---
1.129
1.240
1.115
1.030
1.287
1.180
(psia)
(Btu/lbmole)
2.234e+004
---
---
1.086
0.2323
(cSt)
---
(lb/ft3)
49.23
4.612e-002
3664
7.965e+005
(barrel/day)
1.209 1.469e-002
63.35 2268
0.7908
0.0000
1.000
(ft3/lbmole)
4.590
20.76
0.3119
(Btu/lb)
1249
---
---
0.2092
0.2092
0.7908
(dyne/cm)
53.19
(Btu/hr-ft-F)
---
2.736e-002
0.3973
---
1.458e-002
0.2149
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
53.19
15.38
8.268
17.26
0.8596
0.4748
0.9580
16.87
7.965
16.30
0.9428
0.4574
0.9050
---
---
14.67
---
---
0.8142
---
---
1.312
---
---
---
---
---
7.988e+005 ---
7.965e+005 ---
--2268 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 35 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 12 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
1918.3906
0.8132
17
Oxygen
0.0000
0.0000
18
Methane
399.3043
19
H2S
20
Hydrogen
21
Ethane
22
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2371.1965
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6405.9987
0.1518
1465.0823
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
24
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
34560.0000
42202.3504
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
52.8597
0.1071
952.2721
0.1108
65.3364
0.0375
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
399.2831
0.8091
6405.6590
0.7454
1465.0046
0.8413
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
32.8157
0.0665
986.7648
0.1148
189.9629
0.1091
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6094
0.0012
26.8191
0.0031
2.2250
0.0013
43
Nitrogen
7.9325
0.0161
222.2130
0.0259
18.8691
0.0108
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
493.5004
1.0000
8593.7281
1.0000
1741.3979
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
53
CO
0.0000
0.0000
54
H2O
1865.5310
1.0000
55
Oxygen
0.0000
0.0000
56
Methane
0.0212
57
H2S
58
MASS FLOW (lb/hr) 0.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7908 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2305.8602
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.3398
0.0000
0.0777
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0002
0.0000
0.0062
0.0000
0.0012
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0081
0.0000
0.3570
0.0000
0.0296
0.0000
62
Nitrogen
0.0068
0.0000
0.1915
0.0000
0.0163
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
1865.5673
1.0000
1.0000
2305.9849
1.0000
33607.7279
33608.6223
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 36 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 12 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.1071
---
0.1071
---
---
14
Oxygen
15
Methane
16
7.127e+004
H2S
---
---
---
---
---
---
7.127e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
284.0
---
284.0
21
Nitrogen
4387
---
4387
---
---
---
22
6.040e+005
Air
---
---
6.040e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Component Splitter:
V-078 OXIDO DE ZINC Component Splitter:
30
LOGICAL CONNECTION
V-080 COBALTO MOLIBDENO
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
2359 lbmole/hrMass:
40
4047 barrel/day
User Variables
41 42
NOTES
43 44
4.220e+004 lb/hrStd Ideal Liq Volume:
29285
45 46 47
(Last modified Wed Dec 12, 2018, 19:27)
48 49
Description
50 51 52
Material Stream: 13
53 54 55
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
56 57
Overall
58
Vapour / Phase Fraction
59
Temperature:
60
Pressure:
61
Molar Flow
62
Mass Flow
63
Std Ideal Liq Vol Flow
(barrel/day)
64
Molar Enthalpy
(Btu/lbmole)
65
Molar Entropy
(Btu/lbmole-F)
66
Heat Flow
67
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.9586
0.9586
0.0414
(F)
414.1*
414.1
414.1
(psia)
364.7*
364.7
364.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-8.867e+004
-8.747e+004
0.0000 -1.165e+005
39.79
40.55
22.23
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 37 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 13 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Molecular Weight
13
Molar Density
14
Mass Density
15
Act. Volume Flow
16 17 18
Heat Capacity
19
Mass Heat Capacity
20
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.985e+004
21
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
9.104e+004
22
HHV Mass Basis (Std)
23
CO2 Loading
24
CO2 App ML Con
25
CO2 App WT Con
26
LHV Mass Basis (Std)
27 28 29
Phase Fraction [Act. Vol. Basis]
30
Mass Exergy
31
Partial Pressure of CO2
32
Cost Based on Flow
33
Act. Gas Flow
34
Avg. Liq. Density
35
17.89 (lbmole/ft3) (lb/ft3)
4.382e-002
17.88 4.203e-002
Aqueous Phase 18.02 2.914
0.7840
0.7517
52.50
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-4957
-4891
-6466
Mass Entropy
(Btu/lb-F)
2.224
2.267
1.234
10.24
9.751
21.51
0.5723
0.5453
1.194
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
11.46 1.764e+004
4919
5090
979.4
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
3743
3906
0.6362
Phase Fraction [Vol. Basis]
0.9702
0.9702
2.984e-002
Phase Fraction [Mass Basis]
0.9583
0.9583
4.170e-002
---
---
---
342.1
---
---
(Btu/lb) (psia)
9.957e-002
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
0.0000
0.0000
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
10.24
9.751
21.51
36
Std. Gas Flow
(MMSCFD)
0.0000
37
Std. Ideal Liq. Mass Density
38
Act. Liq. Flow
39
Z Factor
40
Watson K
41
User Property
42
Partial Pressure of H2S
43
Cp/(Cp - R)
44
Cp/Cv
45
Heat of Vap.
46
Kinematic Viscosity
47
Liq. Mass Density (Std. Cond)
48
Liq. Vol. Flow (Std. Cond)
49
Liquid Fraction
50
Molar Volume
51
Mass Heat of Vap.
52
Phase Fraction [Molar Basis]
53
Surface Tension
54
Thermal Conductivity
55
Viscosity
56
Cv (Semi-Ideal)
57
Mass Cv (Semi-Ideal)
58
Cv
59
Mass Cv
60
Cv (Ent. Method)
61
Mass Cv (Ent. Method)
62
Cp/Cv (Ent. Method)
63
Reid VP at 37.8 C
(psia)
64
True VP at 37.8 C
(psia)
65 66
0.0000
0.0000
(lb/ft3)
44.57
44.03
62.30
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
0.9253
19.04
19.04
17.57
---
---
---
0.0000
---
---
1.241
1.256
1.102
1.334
1.378
1.214
2.234e+004 ---
(Btu/lb)
---
---
1.140
0.1497
49.23
48.70
63.35
0.0000
0.0000
0.0000
4.141e-002 (ft3/lbmole)
1.335e-002
22.82
0.0000
1.000
23.79
0.3432
1249
---
---
0.9586
0.9586
0.0414
(dyne/cm)
35.00
(Btu/hr-ft-F)
---
2.459e-002
0.3785
---
1.372e-002
0.1259
(cP) (Btu/lbmole-F)
---
35.00
8.252
7.765
19.52
0.4613
0.4342
1.084
7.673
7.078
17.72
0.4289
0.3957
0.9835
---
---
15.78
---
---
0.8758
---
---
1.363
---
---
---
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-20.24
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 38 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 13 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.8132
0.0000
0.8189
0.0000
0.5859
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.1693
0.0000
0.1518
0.0000
0.3620
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0139
0.0000
0.0234
0.0000
0.0469
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0003
0.0000
0.0006
0.0000
0.0006
24
Nitrogen
0.0000
0.0034
0.0000
0.0053
0.0000
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.8051
0.0000
0.8110
0.0000
0.5731
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.1766
0.0000
0.1584
0.0000
0.3731
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0145
0.0000
0.0244
0.0000
0.0484
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0003
0.0000
0.0007
0.0000
0.0006
43
Nitrogen
0.0000
0.0035
0.0000
0.0055
0.0000
0.0048
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
4.141e-002 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
0.0000
1.0000
0.0000
1.0000
0.0000
0.9999
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 39 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 13 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.8052
---
0.8052
14
Oxygen
---
---
---
15
Methane
5547
---
5547
---
---
---
---
---
16
H2S
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
244.5
---
244.5
21
Nitrogen
1872
---
1872
---
---
---
22
1.872e+004
Air
---
---
1.872e+004
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Component Splitter:
30
LOGICAL CONNECTION
V-080 COBALTO MOLIBDENO
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
0.0000 lbmole/hrMass:
40
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 14
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.2092
0.2092
0.7908
(F)
262.1
262.1
262.1
(psia)
364.7*
364.7
364.7
2359
493.5
(lbmole/hr) (lb/hr)
(Btu/hr)
4.220e+004 4047 -1.025e+005 23.15 -2.419e+008 3664*
(barrel/day)
64
8594 1741 -3.824e+004 41.18 -1.887e+007 7.965e+005
1866 3.361e+004 2306 -1.196e+005 18.38 -2.230e+008 2268
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3)
0.2179
17.41 4.817e-002
Aqueous Phase 18.02 3.206
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 40 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 14 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
3.201e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
3.540e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
---
24
LHV Mass Basis (Std)
(Btu/lb)
3743
25
Phase Fraction [Vol. Basis]
0.4303
0.4303
26
Phase Fraction [Mass Basis]
0.2036
0.2036
27
Phase Fraction [Act. Vol. Basis]
0.9463
0.9463
28
Mass Exergy
(Btu/lb)
65.71
---
29
Partial Pressure of CO2
(psia)
0.4503
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
3.898 4.628e+004
0.8388 4.380e+004
57.75 2488
(Btu/lb)
-5732
-2196
-6637
(Btu/lb-F)
1.294
2.365
1.020
17.36
10.25
19.24
0.9706
0.5888
1.068
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
4919
2.033e+004
3.985 1.764e+004 978.9
---
---
---
---
1.394e-005
---
2.414e-007
1.838e+004
---
0.2212 0.5697 0.7964 5.375e-002 ---
(ACFM)
170.8
170.8
---
(lbmole/ft3)
2.492
1.211
3.458
Specific Heat
(Btu/lbmole-F)
17.36
10.25
19.24
Std. Gas Flow
(MMSCFD)
21.44
4.486
16.96
(lb/ft3)
44.57
21.10
62.30
(USGPS)
1.209
---
---
0.9776
19.04
19.04
12.33
---
---
---
0.0000
---
---
1.129
1.240
1.115
1.030
1.287
1.180
(psia)
(Btu/lbmole)
2.234e+004
---
---
1.086
0.2323
(cSt)
---
(lb/ft3)
49.23
4.612e-002
3664
7.965e+005
(barrel/day)
1.209 1.469e-002
63.35 2268
0.7908
0.0000
1.000
(ft3/lbmole)
4.590
20.76
0.3119
(Btu/lb)
1249
---
---
0.2092
0.2092
0.7908
(dyne/cm)
53.19
(Btu/hr-ft-F)
---
2.736e-002
0.3973
---
1.458e-002
0.2149
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
53.19
15.38
8.268
17.26
0.8596
0.4748
0.9580
16.87
7.965
16.30
0.9428
0.4574
0.9050
---
---
14.67
---
---
0.8142
---
---
1.312
---
---
---
---
---
7.988e+005 ---
7.965e+005 ---
--2268 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 41 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 14 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
1918.3906
0.8132
17
Oxygen
0.0000
0.0000
18
Methane
399.3043
19
H2S
20
Hydrogen
21
Ethane
22
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2371.1965
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6405.9987
0.1518
1465.0823
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
24
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
34560.0000
42202.3504
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
52.8597
0.1071
952.2721
0.1108
65.3364
0.0375
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
399.2831
0.8091
6405.6590
0.7454
1465.0046
0.8413
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
32.8157
0.0665
986.7648
0.1148
189.9629
0.1091
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6094
0.0012
26.8191
0.0031
2.2250
0.0013
43
Nitrogen
7.9325
0.0161
222.2130
0.0259
18.8691
0.0108
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
493.5004
1.0000
8593.7281
1.0000
1741.3979
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
53
CO
0.0000
0.0000
54
H2O
1865.5310
1.0000
55
Oxygen
0.0000
0.0000
56
Methane
0.0212
57
H2S
58
MASS FLOW (lb/hr) 0.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7908 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2305.8602
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.3398
0.0000
0.0777
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0002
0.0000
0.0062
0.0000
0.0012
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0081
0.0000
0.3570
0.0000
0.0296
0.0000
62
Nitrogen
0.0068
0.0000
0.1915
0.0000
0.0163
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
1865.5673
1.0000
1.0000
2305.9849
1.0000
33607.7279
33608.6223
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 42 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 14 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.1071
---
0.1071
---
---
14
Oxygen
15
Methane
16
7.127e+004
H2S
---
---
---
---
---
---
7.127e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
284.0
---
284.0
21
Nitrogen
4387
---
4387
---
---
---
22
6.040e+005
Air
---
---
6.040e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Component Splitter:
V-079 OXIDO DE ZINC Component Splitter:
30
LOGICAL CONNECTION
V-078 OXIDO DE ZINC
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
2359 lbmole/hrMass:
40
4047 barrel/day
User Variables
41 42
NOTES
43 44
4.220e+004 lb/hrStd Ideal Liq Volume:
29285
45 46 47
(Last modified Mon Dec 17, 2018, 15:01)
48 49
Description
50 51 52
Material Stream: 15
53 54 55
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
56 57
Overall
58
Vapour / Phase Fraction
59
Temperature:
60
Pressure:
61
Molar Flow
62
Mass Flow
63
Std Ideal Liq Vol Flow
(barrel/day)
64
Molar Enthalpy
(Btu/lbmole)
65
Molar Entropy
(Btu/lbmole-F)
66
Heat Flow
67
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.9586
0.9586
0.0414
(F)
414.1*
414.1
414.1
(psia)
364.7*
364.7
364.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-8.867e+004
-8.747e+004
0.0000 -1.165e+005
39.79
40.55
22.23
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 43 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 15 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Molecular Weight
13
Molar Density
14
Mass Density
15
Act. Volume Flow
16 17 18
Heat Capacity
19
Mass Heat Capacity
20
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.985e+004
21
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
9.104e+004
22
HHV Mass Basis (Std)
23
CO2 Loading
24
CO2 App ML Con
25
CO2 App WT Con
26
LHV Mass Basis (Std)
27 28 29
Phase Fraction [Act. Vol. Basis]
30
Mass Exergy
31
Partial Pressure of CO2
32
Cost Based on Flow
33
Act. Gas Flow
34
Avg. Liq. Density
35
17.89 (lbmole/ft3) (lb/ft3)
4.382e-002
17.88 4.203e-002
Aqueous Phase 18.02 2.914
0.7840
0.7517
52.50
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-4957
-4891
-6466
Mass Entropy
(Btu/lb-F)
2.224
2.267
1.234
10.24
9.751
21.51
0.5723
0.5453
1.194
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
11.46 1.764e+004
4919
5090
979.4
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
3743
3906
0.6362
Phase Fraction [Vol. Basis]
0.9702
0.9702
2.984e-002
Phase Fraction [Mass Basis]
0.9583
0.9583
4.170e-002
---
---
---
342.1
---
---
(Btu/lb) (psia)
9.957e-002
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
0.0000
0.0000
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
10.24
9.751
21.51
36
Std. Gas Flow
(MMSCFD)
0.0000
37
Std. Ideal Liq. Mass Density
38
Act. Liq. Flow
39
Z Factor
40
Watson K
41
User Property
42
Partial Pressure of H2S
43
Cp/(Cp - R)
44
Cp/Cv
45
Heat of Vap.
46
Kinematic Viscosity
47
Liq. Mass Density (Std. Cond)
48
Liq. Vol. Flow (Std. Cond)
49
Liquid Fraction
50
Molar Volume
51
Mass Heat of Vap.
52
Phase Fraction [Molar Basis]
53
Surface Tension
54
Thermal Conductivity
55
Viscosity
56
Cv (Semi-Ideal)
57
Mass Cv (Semi-Ideal)
58
Cv
59
Mass Cv
60
Cv (Ent. Method)
61
Mass Cv (Ent. Method)
62
Cp/Cv (Ent. Method)
63
Reid VP at 37.8 C
(psia)
64
True VP at 37.8 C
(psia)
65 66
0.0000
0.0000
(lb/ft3)
44.57
44.03
62.30
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
0.9253
19.04
19.04
17.57
---
---
---
0.0000
---
---
1.241
1.256
1.102
1.334
1.378
1.214
2.234e+004 ---
(Btu/lb)
---
---
1.140
0.1497
49.23
48.70
63.35
0.0000
0.0000
0.0000
4.141e-002 (ft3/lbmole)
1.335e-002
22.82
0.0000
1.000
23.79
0.3432
1249
---
---
0.9586
0.9586
0.0414
(dyne/cm)
35.00
(Btu/hr-ft-F)
---
2.459e-002
0.3785
---
1.372e-002
0.1259
(cP) (Btu/lbmole-F)
---
35.00
8.252
7.765
19.52
0.4613
0.4342
1.084
7.673
7.078
17.72
0.4289
0.3957
0.9835
---
---
15.78
---
---
0.8758
---
---
1.363
---
---
---
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-20.24
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 44 of 336 * Specified by user.
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LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 15 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.8132
0.0000
0.8189
0.0000
0.5859
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.1693
0.0000
0.1518
0.0000
0.3620
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0139
0.0000
0.0234
0.0000
0.0469
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0003
0.0000
0.0006
0.0000
0.0006
24
Nitrogen
0.0000
0.0034
0.0000
0.0053
0.0000
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.8051
0.0000
0.8110
0.0000
0.5731
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.1766
0.0000
0.1584
0.0000
0.3731
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0145
0.0000
0.0244
0.0000
0.0484
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0003
0.0000
0.0007
0.0000
0.0006
43
Nitrogen
0.0000
0.0035
0.0000
0.0055
0.0000
0.0048
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
4.141e-002 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
0.0000
1.0000
0.0000
1.0000
0.0000
0.9999
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 45 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 15 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.8052
---
0.8052
14
Oxygen
---
---
---
15
Methane
5547
---
5547
---
---
---
---
---
16
H2S
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
244.5
---
244.5
21
Nitrogen
1872
---
1872
---
---
---
22
1.872e+004
Air
---
---
1.872e+004
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Component Splitter:
30
LOGICAL CONNECTION
V-078 OXIDO DE ZINC
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
0.0000 lbmole/hrMass:
40
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 16
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.2092
0.2092
0.7908
(F)
262.1
262.1
262.1
(psia)
364.7*
364.7
364.7
2359
493.5
(lbmole/hr) (lb/hr)
(Btu/hr)
4.220e+004 4047 -1.025e+005 23.15 -2.419e+008 3664*
(barrel/day)
64
8594 1741 -3.824e+004 41.18 -1.887e+007 7.965e+005
1866 3.361e+004 2306 -1.196e+005 18.38 -2.230e+008 2268
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3)
0.2179
17.41 4.817e-002
Aqueous Phase 18.02 3.206
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 46 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 16 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
3.201e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
3.540e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
---
24
LHV Mass Basis (Std)
(Btu/lb)
3743
25
Phase Fraction [Vol. Basis]
0.4303
0.4303
26
Phase Fraction [Mass Basis]
0.2036
0.2036
27
Phase Fraction [Act. Vol. Basis]
0.9463
0.9463
28
Mass Exergy
(Btu/lb)
65.71
---
29
Partial Pressure of CO2
(psia)
0.4503
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
3.898 4.628e+004
0.8388 4.380e+004
57.75 2488
(Btu/lb)
-5732
-2196
-6637
(Btu/lb-F)
1.294
2.365
1.020
17.36
10.25
19.24
0.9706
0.5888
1.068
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
4919
2.033e+004
3.985 1.764e+004 978.9
---
---
---
---
1.394e-005
---
2.414e-007
1.838e+004
---
0.2212 0.5697 0.7964 5.375e-002 ---
(ACFM)
170.8
170.8
---
(lbmole/ft3)
2.492
1.211
3.458
Specific Heat
(Btu/lbmole-F)
17.36
10.25
19.24
Std. Gas Flow
(MMSCFD)
21.44
4.486
16.96
(lb/ft3)
44.57
21.10
62.30
(USGPS)
1.209
---
---
0.9776
19.04
19.04
12.33
---
---
---
0.0000
---
---
1.129
1.240
1.115
1.030
1.287
1.180
(psia)
(Btu/lbmole)
2.234e+004
---
---
1.086
0.2323
(cSt)
---
(lb/ft3)
49.23
4.612e-002
3664
7.965e+005
(barrel/day)
1.209 1.469e-002
63.35 2268
0.7908
0.0000
1.000
(ft3/lbmole)
4.590
20.76
0.3119
(Btu/lb)
1249
---
---
0.2092
0.2092
0.7908
(dyne/cm)
53.19
(Btu/hr-ft-F)
---
2.736e-002
0.3973
---
1.458e-002
0.2149
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
53.19
15.38
8.268
17.26
0.8596
0.4748
0.9580
16.87
7.965
16.30
0.9428
0.4574
0.9050
---
---
14.67
---
---
0.8142
---
---
1.312
---
---
---
---
---
7.988e+005 ---
7.965e+005 ---
--2268 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 47 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 16 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
1918.3906
0.8132
17
Oxygen
0.0000
0.0000
18
Methane
399.3043
19
H2S
20
Hydrogen
21
Ethane
22
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2371.1965
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6405.9987
0.1518
1465.0823
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
24
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
34560.0000
42202.3504
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
52.8597
0.1071
952.2721
0.1108
65.3364
0.0375
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
399.2831
0.8091
6405.6590
0.7454
1465.0046
0.8413
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
32.8157
0.0665
986.7648
0.1148
189.9629
0.1091
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6094
0.0012
26.8191
0.0031
2.2250
0.0013
43
Nitrogen
7.9325
0.0161
222.2130
0.0259
18.8691
0.0108
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
493.5004
1.0000
8593.7281
1.0000
1741.3979
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
53
CO
0.0000
0.0000
54
H2O
1865.5310
1.0000
55
Oxygen
0.0000
0.0000
56
Methane
0.0212
57
H2S
58
MASS FLOW (lb/hr) 0.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7908 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2305.8602
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.3398
0.0000
0.0777
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0002
0.0000
0.0062
0.0000
0.0012
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0081
0.0000
0.3570
0.0000
0.0296
0.0000
62
Nitrogen
0.0068
0.0000
0.1915
0.0000
0.0163
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
1865.5673
1.0000
1.0000
2305.9849
1.0000
33607.7279
33608.6223
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 48 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 16 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.1071
---
0.1071
---
---
14
Oxygen
15
Methane
16
7.127e+004
H2S
---
---
---
---
---
---
7.127e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
284.0
---
284.0
21
Nitrogen
4387
---
4387
---
---
---
22
6.040e+005
Air
---
---
6.040e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO LNG:
PRODUCT FROM
E-1 PRECALENTADOR DE GAS-VAPOR DE Component PROCESO Splitter:
30
LOGICAL CONNECTION
V-079 OXIDO DE ZINC
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
2359 lbmole/hrMass:
40
4.220e+004 lb/hrStd Ideal Liq Volume:
4047 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 17
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.9586
0.9586
0.0414
(F)
414.1*
414.1
414.1
(psia)
364.7*
364.7
364.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-8.867e+004
-8.747e+004
0.0000 -1.165e+005
39.79
40.55
22.23
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3)
4.382e-002
17.88 4.203e-002
Aqueous Phase 18.02 2.914
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 49 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 17 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Density
13
Act. Volume Flow
14 15 16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.985e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
9.104e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26 27
Phase Fraction [Act. Vol. Basis]
28
Mass Exergy
29
Partial Pressure of CO2
30
Cost Based on Flow
31
Act. Gas Flow
32
Avg. Liq. Density
33
(lb/ft3)
Aqueous Phase
0.7840
0.7517
52.50
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-4957
-4891
-6466
Mass Entropy
(Btu/lb-F)
2.224
2.267
1.234
10.24
9.751
21.51
0.5723
0.5453
1.194
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
11.46 1.764e+004
4919
5090
979.4
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
3743
3906
0.6362
Phase Fraction [Vol. Basis]
0.9702
0.9702
2.984e-002
Phase Fraction [Mass Basis]
0.9583
0.9583
4.170e-002
---
---
---
342.1
---
---
(Btu/lb) (psia)
9.957e-002
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
0.0000
0.0000
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
10.24
9.751
21.51
34
Std. Gas Flow
(MMSCFD)
0.0000
35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63 64
0.0000
0.0000
(lb/ft3)
44.57
44.03
62.30
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
0.9253
19.04
19.04
17.57
---
---
---
0.0000
---
---
1.241
1.256
1.102
1.334
1.378
1.214
2.234e+004 ---
(Btu/lb)
---
---
1.140
0.1497
49.23
48.70
63.35
0.0000
0.0000
0.0000
4.141e-002 (ft3/lbmole)
1.335e-002
22.82
0.0000
1.000
23.79
0.3432
1249
---
---
0.9586
0.9586
0.0414
(dyne/cm)
35.00
(Btu/hr-ft-F)
---
2.459e-002
0.3785
---
1.372e-002
0.1259
(cP) (Btu/lbmole-F)
---
35.00
8.252
7.765
19.52
0.4613
0.4342
1.084
7.673
7.078
17.72
0.4289
0.3957
0.9835
---
---
15.78
---
---
0.8758
---
---
1.363
---
---
---
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-20.24
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 50 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 17 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.8132
0.0000
0.8189
0.0000
0.5859
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.1693
0.0000
0.1518
0.0000
0.3620
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0139
0.0000
0.0234
0.0000
0.0469
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0003
0.0000
0.0006
0.0000
0.0006
24
Nitrogen
0.0000
0.0034
0.0000
0.0053
0.0000
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.8051
0.0000
0.8110
0.0000
0.5731
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.1766
0.0000
0.1584
0.0000
0.3731
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0145
0.0000
0.0244
0.0000
0.0484
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0003
0.0000
0.0007
0.0000
0.0006
43
Nitrogen
0.0000
0.0035
0.0000
0.0055
0.0000
0.0048
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
4.141e-002 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
0.0000
1.0000
0.0000
1.0000
0.0000
0.9999
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 51 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 17 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.8052
---
0.8052
14
Oxygen
---
---
---
15
Methane
5547
---
5547
---
---
---
---
---
16
H2S
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
244.5
---
244.5
21
Nitrogen
1872
---
1872
---
---
---
22
1.872e+004
Air
---
---
1.872e+004
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Component Splitter:
30
LOGICAL CONNECTION
V-079 OXIDO DE ZINC
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
0.0000 lbmole/hrMass:
40
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 18
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
825.0*
825.0
(psia)
254.7*
254.7
(lbmole/hr) (lb/hr)
(Btu/hr)
2359 4.220e+004 4047 -8.389e+004 45.08 -1.979e+008 3664*
(barrel/day)
64
2359 4.220e+004 4047 -8.389e+004 45.08 -1.979e+008 3664
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3)
1.874e-002
17.89 1.874e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 52 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 18 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-4689
-4689
15
Mass Entropy
(Btu/lb-F)
2.520
2.520
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.696e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
8.800e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.3352 5.382e+005
0.3352 5.382e+005
10.31
10.31
0.5763
0.5763
4919
4919
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
3743
3743
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
27
Phase Fraction [Act. Vol. Basis]
1.000
1.000
28
Mass Exergy
450.6
---
29
Partial Pressure of CO2
30
Cost Based on Flow
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(Btu/lb) (psia) (Cost/s)
6.667e-002 0.0000
--0.0000
(ACFM)
2099
2099
(lbmole/ft3)
2.492
2.492
Specific Heat
(Btu/lbmole-F)
10.31
10.31
Std. Gas Flow
(MMSCFD)
21.44
21.44
(lb/ft3)
44.57
44.57
(USGPS)
---
---
0.9861
0.9861
19.04
19.04
---
---
(psia)
(Btu/lbmole)
0.0000
---
1.239
1.239
1.263
1.263
2.254e+004
---
(cSt)
3.896
3.896
(lb/ft3)
49.23
49.23
(barrel/day)
3664
3664
0.0000
0.0000
(ft3/lbmole)
53.37
53.37
(Btu/lb)
1260
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
3.947e-002
3.947e-002
2.092e-002
2.092e-002
8.324
8.324
0.4653
0.4653
8.161
8.161
0.4562
0.4562
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
3664
3664
-3.959
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 53 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 18 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
1918.3906
0.8132
17
Oxygen
0.0000
0.0000
18
Methane
399.3043
19
H2S
20
Hydrogen
21
Ethane
22
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2371.1965
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6405.9987
0.1518
1465.0823
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
24
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
30
0.0000
Vapour Fraction
34560.0000
42202.3504
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
34
CO
0.0000
0.0000
35
H2O
1918.3906
0.8132
36
Oxygen
0.0000
0.0000
37
Methane
399.3043
38
H2S
39
Hydrogen
40
Ethane
41
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2371.1965
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6405.9987
0.1518
1465.0823
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
43
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
49
34560.0000
42202.3504
K VALUE
50 51
0.0000
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 54 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 18 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Tee:
TEE-100 LNG:
LOGICAL CONNECTION
E-1 PRECALENTADOR DE GAS-VAPOR DE PROCESO
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 254.7 psia
2359 lbmole/hrMass:
23
4.220e+004 lb/hrStd Ideal Liq Volume:
4047 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 19
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
825.0
825.0
(psia)
254.7
254.7
26.35*
26.35
471.4
471.4
(lbmole/hr) (lb/hr)
(Btu/hr)
45.21 -8.389e+004 45.08 -2.211e+006 40.93*
(barrel/day)
47
45.21 -8.389e+004 45.08 -2.211e+006 40.93
PROPERTIES
48 49
Overall
Vapour Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
55
Mass Entropy
56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.696e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
8.800e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66
17.89 (lbmole/ft3) (lb/ft3)
1.874e-002 0.3352
17.89 1.874e-002 0.3352
(barrel/day)
6013
6013
(Btu/lb)
-4689
-4689
(Btu/lb-F)
2.520
2.520
(Btu/lbmole-F) (Btu/lb-F)
10.31
0.5763
0.5763
4919
4919
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
3743
3743
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
67
Phase Fraction [Act. Vol. Basis]
1.000
1.000
68
Mass Exergy
450.6
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
10.31
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 55 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 19 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
(psia)
Vapour Phase
6.667e-002
---
(Cost/s)
0.0000
0.0000
(ACFM)
23.44
23.44
(lbmole/ft3)
2.492
2.492
Specific Heat
(Btu/lbmole-F)
10.31
10.31
17
Std. Gas Flow
(MMSCFD)
0.2396
0.2396
18
Std. Ideal Liq. Mass Density
(lb/ft3)
44.57
44.57
19
Act. Liq. Flow
(USGPS)
---
---
20
Z Factor
0.9861
0.9861
21
Watson K
19.04
19.04
22
User Property
---
---
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46 47
(psia)
(Btu/lbmole)
0.0000
---
1.239
1.239
1.263
1.263
2.254e+004
---
(cSt)
3.896
3.896
(lb/ft3)
49.23
49.23
(barrel/day)
40.93
40.93
0.0000
0.0000
(ft3/lbmole)
53.37
53.37
(Btu/lb)
1260
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
3.947e-002
3.947e-002
2.092e-002
2.092e-002
8.324
8.324
0.4653
0.4653
8.161
8.161
0.4562
0.4562
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
40.93
40.93
Viscosity Index
-3.959
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
H2O
21.4303
0.8132
386.0695
0.8189
26.4886
0.5859
56
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Methane
4.4606
0.1693
71.5614
0.1518
16.3664
0.3620
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Ethane
0.3666
0.0139
11.0232
0.0234
2.1221
0.0469
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0069
0.0003
0.3036
0.0006
0.0252
0.0006
63
Nitrogen
0.0887
0.0034
2.4845
0.0053
0.2110
0.0047
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
26.3531
1.0000
471.4422
1.0000
45.2133
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 56 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 19 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
21.4303
0.8132
386.0695
0.8189
26.4886
0.5859
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
4.4606
0.1693
71.5614
0.1518
16.3664
0.3620
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.3666
0.0139
11.0232
0.0234
2.1221
0.0469
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0069
0.0003
0.3036
0.0006
0.0252
0.0006
24
Nitrogen
0.0887
0.0034
2.4845
0.0053
0.2110
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
26.3531
1.0000
471.4422
1.0000
45.2133
1.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Conversion Reactor:
H-1
51
Tee:
LOGICAL CONNECTION TEE-100
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Active)
61
254.7 psia Molar:
* Mass: 26.35 lbmole/hr
471.4 lb/hr Std Ideal Liq Volume:
45.21 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 57 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 20
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
825.0
825.0
(psia)
254.7
254.7
(lbmole/hr) (lb/hr)
(Btu/hr)
2333 4.173e+004 4002 -8.389e+004 45.08 -1.957e+008 3623*
(barrel/day)
22
2333 4.173e+004 4002 -8.389e+004 45.08 -1.957e+008 3623
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-4689
-4689
30
Mass Entropy
(Btu/lb-F)
2.520
2.520
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.696e+004
34
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
8.800e+004
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41
17.89 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.874e-002 0.3352 5.322e+005
17.89 1.874e-002 0.3352 5.322e+005
10.31
10.31
0.5763
0.5763
4919
4919
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
3743
3743
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
450.6
---
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lb) (psia) (Cost/s)
6.667e-002 0.0000
--0.0000
(ACFM)
2075
2075
(lbmole/ft3)
2.492
2.492
Specific Heat
(Btu/lbmole-F)
10.31
10.31
Std. Gas Flow
(MMSCFD)
21.20
21.20
(lb/ft3)
44.57
44.57
(USGPS)
---
---
0.9861
0.9861
19.04
19.04
---
---
Licensed to: LEGENDS
(psia)
(Btu/lbmole)
0.0000
---
1.239
1.239
1.263
1.263
2.254e+004
---
(cSt)
3.896
3.896
(lb/ft3)
49.23
49.23
(barrel/day)
3623
3623
0.0000
0.0000
(ft3/lbmole)
53.37
53.37
(Btu/lb)
1260
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
3.947e-002
3.947e-002
2.092e-002
2.092e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 58 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 20 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 8.324
8.324
0.4653
0.4653
8.161
8.161
0.4562
0.4562
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
3623
3623
-3.959
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
29
CO
0.0000
0.0000
30
H2O
1896.9603
0.8132
31
Oxygen
0.0000
0.0000
32
Methane
394.8437
33
H2S
34
Hydrogen
35
Ethane
36
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2344.7079
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6334.4374
0.1518
1448.7158
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.4493
0.0139
975.7478
0.0234
187.8420
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.6106
0.0003
26.8726
0.0006
2.2294
0.0006
38
Nitrogen
7.8506
0.0034
219.9200
0.0053
18.6744
0.0047
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
2332.7145
1.0000
1.0000
4002.1696
1.0000
44
0.0000
Vapour Fraction
34173.9305
41730.9082
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
48
CO
0.0000
0.0000
49
H2O
1896.9603
0.8132
50
Oxygen
0.0000
0.0000
51
Methane
394.8437
52
H2S
53
Hydrogen
54
Ethane
55
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2344.7079
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6334.4374
0.1518
1448.7158
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.4493
0.0139
975.7478
0.0234
187.8420
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6106
0.0003
26.8726
0.0006
2.2294
0.0006
57
Nitrogen
7.8506
0.0034
219.9200
0.0053
18.6744
0.0047
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
2332.7145
1.0000
1.0000
4002.1696
1.0000
63
34173.9305
41730.9082
K VALUE
64 65
0.0000
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 59 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 20 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Conversion Reactor:
H-1
LOGICAL CONNECTION
Tee:
TEE-100
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
254.7 psia 2333 lbmole/hrMass:
37
4.173e+004 lb/hrStd Ideal Liq Volume:
4002 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 21
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
1.0000
1.0000
(F)
1385*
1385
1385
(psia)
254.7
254.7
254.7
3006
0.0000
(lbmole/hr) (lb/hr)
(Btu/hr)
3006 4.220e+004 5520 -5.149e+004 43.74 -1.548e+008 5900*
(barrel/day)
61
4.220e+004 5520 -5.149e+004 43.74 -1.548e+008 5900
0.0000
0.0000 0.0000 -5.149e+004 43.74 0.0000 0.0000
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 14.04
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
1.285e-002 0.1804 9.999e+005 -3668
14.04 1.285e-002 0.1804 9.999e+005 -3668
Aqueous Phase 14.04 1.285e-002 0.1804 0.0000 -3667
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 60 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 21 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
6.100e+004
6.100e+004
6.100e+004
16
HHV Molar Basis (Std)
(Btu/lbmole)
7.752e+004
7.752e+004
7.752e+004
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22 23 24
Phase Fraction [Act. Vol. Basis]
25
Mass Exergy
26
Partial Pressure of CO2
27
Cost Based on Flow
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.115
3.115
9.448
9.448
3.115 9.448
0.6729
0.6729
0.6729
5521
5521
5521
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
4345
4345
4345
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
688.8
---
---
(psia)
15.62
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
3899
3899
---
(lbmole/ft3)
2.328
2.328
2.328
Specific Heat
(Btu/lbmole-F)
9.448
9.448
9.448
Std. Gas Flow
(MMSCFD)
27.32
27.32
0.0000
(lb/ft3)
32.68
32.68
32.68
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole)
---
1.001
1.001
14.99
14.99
14.99
---
---
---
0.0000
---
---
1.266
1.266
1.266
1.271
1.271
1.271
1.910e+004
---
--0.8475
(cSt)
9.500
9.500
(lb/ft3)
30.58
30.58
30.57
5900
5900
0.0000
(barrel/day)
0.0000
0.0000
1.000
(ft3/lbmole)
77.82
77.82
77.82
(Btu/lb)
1360
---
---
1.0000
1.0000
0.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
0.0000
9.446e-002
9.446e-002
9.529e-002
2.746e-002
2.746e-002
2.449e-003
7.462
7.462
7.462
0.5315
0.5315
0.5315
7.434
7.434
7.434
0.5295
0.5295
0.5295
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
---
5900
5900
0.0000
0.8786
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 139.7565
MOLE FRACTION 0.0465
MASS FLOW (lb/hr) 3914.7054
Vapour Fraction MASS FRACTION 0.0928
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 335.3202
1.0000
LIQUID VOLUME FRACTION 0.0607
Page 61 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 21 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
H2O
1411.2742
0.4695
0.6024
1744.3832
0.3160
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
75.8678
0.0252
1217.1398
0.0288
278.3656
0.0504
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
1153.9894
0.3839
2326.4426
0.0551
2280.2771
0.4131
20
Ethane
32.8159
0.0109
986.7710
0.0234
189.9641
0.0344
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
184.2975
0.0613
8110.8767
0.1922
672.9082
0.1219
23
Nitrogen
7.9393
0.0026
222.4045
0.0053
18.8854
0.0034
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
3005.9406
1.0000
1.0000
5520.1038
1.0000
25424.2464
42202.5863
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
33
CO
139.7565
0.0465
3914.7054
0.0928
335.3202
0.0607
34
H2O
1411.2742
0.4695
25424.2464
0.6024
1744.3832
0.3160
35
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Methane
75.8678
0.0252
1217.1398
0.0288
278.3656
0.0504
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
1153.9894
0.3839
2326.4426
0.0551
2280.2771
0.4131
39
Ethane
32.8159
0.0109
986.7710
0.0234
189.9641
0.0344
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
184.2975
0.0613
8110.8767
0.1922
672.9082
0.1219
42
Nitrogen
7.9393
0.0026
222.4045
0.0053
18.8854
0.0034
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
3005.9406
1.0000
1.0000
5520.1038
1.0000
48
42202.5863
Aqueous Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
52
CO
0.0000
0.0465
0.0000
0.0928
0.0000
0.0607
53
H2O
0.0000
0.4695
0.0000
0.6024
0.0000
0.3160
54
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Methane
0.0000
0.0252
0.0000
0.0288
0.0000
0.0504
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
0.0000
0.3839
0.0000
0.0551
0.0000
0.4131
58
Ethane
0.0000
0.0109
0.0000
0.0234
0.0000
0.0344
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
0.0000
0.0613
0.0000
0.1922
0.0000
0.1219
61
Nitrogen
0.0000
0.0026
0.0000
0.0053
0.0000
0.0034
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 62 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 21 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
1.000
---
1.000
13
H2O
1.000
---
1.000
14
Oxygen
---
---
---
15
Methane
1.000
---
1.000
16
---
---
---
Hydrogen
H2S
1.000
---
1.000
18
Ethane
1.000
---
1.000
19
Propane
---
---
---
20
CO2
1.000
---
1.000
21
Nitrogen
1.000
---
1.000
---
---
---
17
22
Air
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Mixer:
LOGICAL CONNECTION
MIX-100 Conversion Reactor:
30
H-1
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
254.7 psia 3006 lbmole/hrMass:
40
4.220e+004 lb/hrStd Ideal Liq Volume:
5520 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 22
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.0000
0.0000
(F)
1385
1385
1385
(psia)
254.7
254.7
254.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-5.149e+004
-5.149e+004
1.0000
0.0000 -5.149e+004
43.74
43.74
43.74
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 14.04
(lbmole/ft3)
1.285e-002
14.04 1.285e-002
Aqueous Phase 14.04 1.285e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 63 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 22 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Density
13
Act. Volume Flow
14
(lb/ft3)
Vapour Phase
Aqueous Phase
0.1804
0.1804
0.1804
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-3667
-3668
-3667
15
Mass Entropy
(Btu/lb-F)
3.115
3.115
3.115
16
Heat Capacity
9.448
9.448
9.448
17
Mass Heat Capacity
0.6729
0.6729
0.6729
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.100e+004
6.100e+004
6.100e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
7.752e+004
7.752e+004
7.752e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
Phase Fraction [Vol. Basis]
26
Phase Fraction [Mass Basis]
27
Phase Fraction [Act. Vol. Basis]
28
Mass Exergy
29
Partial Pressure of CO2
30
Cost Based on Flow
31
Act. Gas Flow
32
Avg. Liq. Density
33
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
5521
5521
5521
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
4345
4345
4345
---
---
1.000
0.0000
0.0000
1.000
---
---
---
(Btu/lb)
688.8
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
9.448
9.448
9.448
34
Std. Gas Flow
(MMSCFD)
0.0000
35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63 64
0.0000
0.0000
(lb/ft3)
32.68
32.68
32.68
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
1.001
1.001
14.99
14.99
14.99
---
---
---
0.0000
---
---
1.266
1.266
1.266
1.271
1.271
1.271
1.910e+004 0.8475
---
---
9.500
0.8475
30.57
30.58
30.57
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
77.82
77.82
77.82
(Btu/lb)
1360
---
---
0.0000
0.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
---
9.529e-002
9.446e-002
9.529e-002
2.449e-003
2.746e-002
2.449e-003
7.462
7.462
7.462
0.5315
0.5315
0.5315
7.434
7.434
7.434
0.5295
0.5295
0.5295
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
0.8786
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 64 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 22 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0465
0.0000
0.0928
0.0000
0.0607
16
H2O
0.0000
0.4695
0.0000
0.6024
0.0000
0.3160
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0252
0.0000
0.0288
0.0000
0.0504
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.3839
0.0000
0.0551
0.0000
0.4131
21
Ethane
0.0000
0.0109
0.0000
0.0234
0.0000
0.0344
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0613
0.0000
0.1922
0.0000
0.1219
24
Nitrogen
0.0000
0.0026
0.0000
0.0053
0.0000
0.0034
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0465
0.0000
0.0928
0.0000
0.0607
35
H2O
0.0000
0.4695
0.0000
0.6024
0.0000
0.3160
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.0252
0.0000
0.0288
0.0000
0.0504
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.3839
0.0000
0.0551
0.0000
0.4131
40
Ethane
0.0000
0.0109
0.0000
0.0234
0.0000
0.0344
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0613
0.0000
0.1922
0.0000
0.1219
43
Nitrogen
0.0000
0.0026
0.0000
0.0053
0.0000
0.0034
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0465
0.0000
0.0928
0.0000
0.0607
54
H2O
0.0000
0.4695
0.0000
0.6024
0.0000
0.3160
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0252
0.0000
0.0288
0.0000
0.0504
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.3839
0.0000
0.0551
0.0000
0.4131
59
Ethane
0.0000
0.0109
0.0000
0.0234
0.0000
0.0344
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0000
0.0613
0.0000
0.1922
0.0000
0.1219
62
Nitrogen
0.0000
0.0026
0.0000
0.0053
0.0000
0.0034
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 65 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 22 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
1.000
---
1.000
13
H2O
1.000
---
1.000
14
Oxygen
---
---
---
15
Methane
1.000
---
1.000
16
---
---
---
Hydrogen
H2S
1.000
---
1.000
18
Ethane
1.000
---
1.000
19
Propane
---
---
---
20
CO2
1.000
---
1.000
21
Nitrogen
1.000
---
1.000
---
---
---
17
22
Air
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Conversion Reactor:
30
LOGICAL CONNECTION H-1
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
254.7 psia 0.0000 lbmole/hrMass:
40
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 23
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
1223
1223
(psia)
254.7
254.7
(lbmole/hr) (lb/hr)
(Btu/hr)
3650 6.078e+004 6990 -4.216e+004 43.09 -1.539e+008 9896*
(barrel/day)
64
3650 6.078e+004 6990 -4.216e+004 43.09 -1.539e+008 9896
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 16.65
(lbmole/ft3)
1.409e-002
16.65 1.409e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 66 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 23 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-2532
-2532
15
Mass Entropy
(Btu/lb-F)
2.587
2.587
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
5.024e+004
5.024e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
6.384e+004
6.384e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.2346 1.108e+006
0.2346 1.108e+006
9.008
9.008
0.5409
0.5409
3834
3834
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
3017
3017
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
27
Phase Fraction [Act. Vol. Basis]
1.000
1.000
28
Mass Exergy
(Btu/lb)
494.8
---
29
Partial Pressure of CO2
(psia)
12.86
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
(ACFM)
4318
4318
(lbmole/ft3)
2.232
2.232
Specific Heat
(Btu/lbmole-F)
9.008
9.008
Std. Gas Flow
(MMSCFD)
33.18
33.18
(lb/ft3)
37.17
37.17
(USGPS)
---
---
Z Factor
1.002
1.002
38
Watson K
10.31
10.31
39
User Property
---
---
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(psia)
(Btu/lbmole)
0.0000
---
1.283
1.283
1.288
1.288
1.879e+004
---
(cSt)
7.488
7.488
(lb/ft3)
26.25
26.25
(barrel/day)
9896
9896
0.0000
0.0000
(ft3/lbmole)
70.99
70.99
(Btu/lb)
1129
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
7.588e-002
7.588e-002
2.814e-002
2.814e-002
7.022
7.022
0.4217
0.4217
6.994
6.994
0.4200
0.4200
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
9896
9896
-1.779
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 67 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 23 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
CO
139.7565
0.0383
3914.7054
0.0644
335.3202
0.0480
16
H2O
1411.2742
0.3867
25424.2464
0.4183
1744.3832
0.2495
17
Oxygen
135.2105
0.0370
4326.7368
0.0712
260.4106
0.0373
18
Methane
75.8678
0.0208
1217.1398
0.0200
278.3656
0.0398
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1153.9894
0.3162
2326.4426
0.0383
2280.2771
0.3262
21
Ethane
32.8159
0.0090
986.7710
0.0162
189.9641
0.0272
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
184.2975
0.0505
8110.8767
0.1335
672.9082
0.0963
24
Nitrogen
516.5885
0.1415
14471.1926
0.2381
1228.8138
0.1758
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
3649.8002
1.0000
1.0000
6990.4428
1.0000
30
60778.1113
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
34
CO
139.7565
0.0383
3914.7054
0.0644
335.3202
0.0480
35
H2O
1411.2742
0.3867
25424.2464
0.4183
1744.3832
0.2495
36
Oxygen
135.2105
0.0370
4326.7368
0.0712
260.4106
0.0373
37
Methane
75.8678
0.0208
1217.1398
0.0200
278.3656
0.0398
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1153.9894
0.3162
2326.4426
0.0383
2280.2771
0.3262
40
Ethane
32.8159
0.0090
986.7710
0.0162
189.9641
0.0272
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
184.2975
0.0505
8110.8767
0.1335
672.9082
0.0963
43
Nitrogen
516.5885
0.1415
14471.1926
0.2381
1228.8138
0.1758
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
3649.8002
1.0000
1.0000
6990.4428
1.0000
49
K VALUE
50 51
60778.1113
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 68 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 23 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO Conversion Reactor:
PRODUCT FROM
H-1 REFORMADOR SECUNDARIO Mixer:
LOGICAL CONNECTION MIX-100
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
254.7 psia 3650 lbmole/hrMass:
23
6990 barrel/day
User Variables
24 25
NOTES
26 27
6.078e+004 lb/hrStd Ideal Liq Volume:
29285
28 29 30
(Last modified Mon Dec 17, 2018, 15:07)
31 32
Description
33 34 35
Material Stream: 24
36 37 38
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
39 40
Overall
41
Vapour / Phase Fraction
42
Temperature:
43
Pressure:
44
Molar Flow
45
Mass Flow
46
Std Ideal Liq Vol Flow
(barrel/day)
47
Molar Enthalpy
(Btu/lbmole)
48
Molar Entropy
(Btu/lbmole-F)
49
Heat Flow
50
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
982.0
982.0
982.0
(psia)
248.7
248.7
248.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-9.511e+004
-9.511e+004
0.0000 -9.511e+004
44.26
44.26
44.26
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
51
PROPERTIES
52 53
Overall
54
Molecular Weight
55
Molar Density
56
Mass Density
57
Act. Volume Flow
58
Vapour Phase 18.00
(lbmole/ft3)
1.629e-002
Liquid Phase 18.00 1.629e-002
0.2933
0.2933
0.2933
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-5284
-5284
-5284
59
Mass Entropy
(Btu/lb-F)
2.459
2.459
2.459
60
Heat Capacity
9.493
9.493
9.493
61
Mass Heat Capacity
0.5274
0.5274
0.5274
62
LHV Molar Basis (Std)
(Btu/lbmole)
63
HHV Molar Basis (Std)
(Btu/lbmole)
64
HHV Mass Basis (Std)
65
CO2 Loading
66
CO2 App ML Con
67
CO2 App WT Con
68
LHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
1.629e-002
18.00
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1217 1.874e+004
1217 1.874e+004
1217 1.874e+004
1041
1041
1041
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
67.59
67.59
67.59
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 69 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 24 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Phase Fraction [Vol. Basis]
13
Phase Fraction [Mass Basis]
14
Phase Fraction [Act. Vol. Basis]
15
Mass Exergy
16
Partial Pressure of CO2
17
Cost Based on Flow
18
Act. Gas Flow
19
Avg. Liq. Density
20
Vapour Phase
Liquid Phase
---
---
1.000
0.0000
0.0000
1.000
---
---
---
(Btu/lb)
541.7
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
9.493
9.493
9.493
21
Std. Gas Flow
(MMSCFD)
0.0000
22
Std. Ideal Liq. Mass Density
23
Act. Liq. Flow
24
Z Factor
25
Watson K
26
User Property
27
Partial Pressure of H2S
28
Cp/(Cp - R)
29
Cp/Cv
30
Heat of Vap.
31
Kinematic Viscosity
32
Liq. Mass Density (Std. Cond)
33
Liq. Vol. Flow (Std. Cond)
34
Liquid Fraction
35
Molar Volume
36
Mass Heat of Vap.
37
Phase Fraction [Molar Basis]
38
Surface Tension
39
Thermal Conductivity
40
Viscosity
41
Cv (Semi-Ideal)
42
Mass Cv (Semi-Ideal)
43
Cv
44
Mass Cv
45
Cv (Ent. Method)
46
Mass Cv (Ent. Method)
47
Cp/Cv (Ent. Method)
48
Reid VP at 37.8 C
49
True VP at 37.8 C
50 51
0.0000
0.0000
(lb/ft3)
61.35
61.35
61.35
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt)
---
0.9866
0.9866
10.10
10.10
10.10
---
---
---
0.0000
---
---
1.265
1.265
1.265
1.292
1.292
1.292
3.131e+004 0.7088
(lb/ft3) (barrel/day)
---
---
4.806
0.7088
62.38
62.38
62.38
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
61.37
61.37
61.37
(Btu/lb)
1739
---
---
0.0000
0.0000
1.0000
(dyne/cm)
---
(Btu/hr-ft-F)
0.1877
(cP)
---
3.330e-003
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
4.057e-002 2.258e-002
--0.1877 3.330e-003
7.507
7.507
7.507
0.4171
0.4171
0.4171
7.350
7.350
7.350
0.4083
0.4083
0.4083
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-1.939
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
52
COMPOSITION
53 54
Overall Phase
55 56
COMPONENTS
57
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
58
CO
0.0000
0.0009
0.0000
0.0014
0.0000
0.0018
59
H2O
0.0000
0.9844
0.0000
0.9853
0.0000
0.9702
60
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
61
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
62
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Hydrogen
0.0000
0.0077
0.0000
0.0009
0.0000
0.0121
64
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
65
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
CO2
0.0000
0.0019
0.0000
0.0047
0.0000
0.0056
67
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
68
Air
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 70 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 24 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
19
Vapour Phase
20 21
COMPONENTS
22
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
23
CO
0.0000
0.0009
0.0000
0.0014
0.0000
0.0018
24
H2O
0.0000
0.9844
0.0000
0.9853
0.0000
0.9702
25
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
26
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
27
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Hydrogen
0.0000
0.0077
0.0000
0.0009
0.0000
0.0121
29
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
30
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
CO2
0.0000
0.0019
0.0000
0.0047
0.0000
0.0056
32
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
33
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
38
Liquid Phase
39 40
COMPONENTS
41
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
42
CO
0.0000
0.0009
0.0000
0.0014
0.0000
0.0018
43
H2O
0.0000
0.9844
0.0000
0.9853
0.0000
0.9702
44
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
45
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
46
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Hydrogen
0.0000
0.0077
0.0000
0.0009
0.0000
0.0121
48
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
49
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
CO2
0.0000
0.0019
0.0000
0.0047
0.0000
0.0056
51
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
52
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
57
K VALUE
58 59
COMPONENTS
MIXED
LIGHT
HEAVY
60
CO
1.000
1.000
---
61
H2O
1.000
1.000
---
62
Oxygen
1.000
1.000
---
63
Methane
1.000
1.000
---
---
---
---
64
H2S
65
Hydrogen
1.000
1.000
---
66
Ethane
1.000
1.000
---
67
Propane
---
---
---
68
CO2
1.000
1.000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 71 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 24 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
LIGHT
Nitrogen
13
Air
HEAVY
1.000
1.000
---
---
---
---
14
Mercury
---
---
---
15
MEAmine
---
---
---
16
Ammonia
---
---
---
17
UNIT OPERATIONS
18 19
FEED TO
PRODUCT FROM
20
Conversion Reactor:
21
LOGICAL CONNECTION
H-1 REFORMADOR SECUNDARIO
UTILITIES
22 23
( No utilities reference this stream )
24
PROCESS UTILITY
25 26 27
DYNAMICS
28 29
Pressure Specification
(Inactive):
30
Flow Specification
(Inactive) Molar:
248.7 psia 0.0000 lbmole/hrMass:
31
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
32 33
NOTES
34 35 36
Description
37 38 39
Material Stream: 25
40 41 42
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
43 44
Overall
45
Vapour / Phase Fraction
46
Temperature:
47
Pressure:
48
Molar Flow
49
Mass Flow
50
Std Ideal Liq Vol Flow
(barrel/day)
51
Molar Enthalpy
(Btu/lbmole)
52
Molar Entropy
(Btu/lbmole-F)
53
Heat Flow
54
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
1.0000
1.0000
0.0000
(F)
982.0*
982.0
982.0
(psia)
248.7
248.7
(lbmole/hr) (lb/hr)
248.7
1.509e+005
1.509e+005
0.0000
2.717e+006
2.717e+006
0.0000
1.893e+005
1.893e+005
-9.511e+004
-9.511e+004
44.26
44.26
0.0000 -9.511e+004 44.26
(Btu/hr)
-1.436e+010
-1.436e+010
0.0000
(barrel/day)
* 1.862e+005
1.862e+005
0.0000
55
PROPERTIES
56 57
Overall
Vapour Phase
Liquid Phase
58
Molecular Weight
59
Molar Density
60
Mass Density
61
Act. Volume Flow
62
Mass Enthalpy
(Btu/lb)
-5284
-5284
-5284
63
Mass Entropy
(Btu/lb-F)
2.459
2.459
2.459
64
Heat Capacity
9.493
9.493
9.493
65
Mass Heat Capacity
0.5274
0.5274
0.5274
66
LHV Molar Basis (Std)
(Btu/lbmole)
67
HHV Molar Basis (Std)
(Btu/lbmole)
68
HHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.629e-002 0.2933 3.960e+007
1217 1.874e+004 1041
18.00 1.629e-002 0.2933 3.960e+007
1217 1.874e+004 1041
18.00 1.629e-002 0.2933 0.0000
1217 1.874e+004 1041
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 72 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 25 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
CO2 Loading
13
CO2 App ML Con
14
CO2 App WT Con
15
LHV Mass Basis (Std)
16 17 18
Phase Fraction [Act. Vol. Basis]
19
Mass Exergy
20
Partial Pressure of CO2
21
Cost Based on Flow
22
Act. Gas Flow
23
Avg. Liq. Density
24 25 26
Std. Ideal Liq. Mass Density
27
Act. Liq. Flow
28
Z Factor
29
Watson K
30
User Property
31
Partial Pressure of H2S
32
Cp/(Cp - R)
33
Cp/Cv
34
Heat of Vap.
35
Kinematic Viscosity
36
Liq. Mass Density (Std. Cond)
37
Liq. Vol. Flow (Std. Cond)
38
Liquid Fraction
39
Molar Volume
40
Mass Heat of Vap.
41
Phase Fraction [Molar Basis]
42
Surface Tension
43
Thermal Conductivity
44
Viscosity
45
Cv (Semi-Ideal)
46
Mass Cv (Semi-Ideal)
47
Cv
48
Mass Cv
49
Cv (Ent. Method)
50
Mass Cv (Ent. Method)
51
Cp/Cv (Ent. Method)
52
Reid VP at 37.8 C
53
True VP at 37.8 C
54
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
55
Viscosity Index
Vapour Phase
Liquid Phase
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
67.59
67.59
67.59
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
541.7
---
---
(psia)
0.4746
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1.544e+005
1.544e+005
---
(lbmole/ft3)
3.408
3.408
Specific Heat
(Btu/lbmole-F)
9.493
9.493
9.493
Std. Gas Flow
(MMSCFD)
1372
1372
0.0000
(lb/ft3)
61.35
61.35
61.35
(USGPS)
---
---
---
---
0.9866
0.9866
10.10
10.10
10.10
---
---
---
0.0000
---
---
1.265
1.265
1.265
1.292
1.292
1.292
(psia)
(Btu/lbmole) (cSt)
3.131e+004 4.806
(lb/ft3)
62.38
(barrel/day)
1.862e+005
3.408
---
---
4.806
0.7088
62.38 1.862e+005
62.38 0.0000
0.0000
0.0000
1.000
(ft3/lbmole)
61.37
61.37
61.37
(Btu/lb)
1739
---
---
1.0000
1.0000
0.0000
---
0.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
--4.057e-002
4.057e-002
2.258e-002
2.258e-002
0.1877 3.330e-003
7.507
7.507
7.507
0.4171
0.4171
0.4171
7.350
7.350
7.350
0.4083
0.4083
0.4083
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
1.862e+005 -1.939
56
1.862e+005 ---
--0.0000 ---
COMPOSITION
57 58
Overall Phase
59 60
COMPONENTS
61
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0014
335.6551
0.0018
0.9853
183673.4882
0.9702
62
CO
139.8961
0.0009
63
H2O
148599.0282
0.9844
64
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
65
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
66
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Hydrogen
1156.4711
0.0077
2331.4459
0.0009
2285.1811
0.0121
68
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
69
Aspen Technology Inc. Licensed to: LEGENDS
3918.6150 2.677026425e+06
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0010
Page 73 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 25 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
16
CO2
288.0576
0.0019
12677.3302
0.0047
1051.7579
0.0056
17
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
18
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Total
150949.1460
0.0000
1.0000
23
2.717102502e+06
1.0000
189315.9286
Vapour Phase
24 25
COMPONENTS
26
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
1.0000
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0014
335.6551
0.0018
0.9853
183673.4882
0.9702
27
CO
139.8961
0.0009
28
H2O
148599.0282
0.9844
29
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
30
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
31
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Hydrogen
1156.4711
0.0077
2331.4459
0.0009
2285.1811
0.0121
33
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
34
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
CO2
288.0576
0.0019
12677.3302
0.0047
1051.7579
0.0056
36
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
37
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Total
150949.1460
3918.6150 2.677026425e+06
1.0000
42
2.717102502e+06
1.0000
189315.9286
Liquid Phase
43 44
COMPONENTS
45
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
46
CO
0.0000
0.0009
0.0000
0.0014
0.0000
0.0018
47
H2O
0.0000
0.9844
0.0000
0.9853
0.0000
0.9702
48
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
49
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
50
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Hydrogen
0.0000
0.0077
0.0000
0.0009
0.0000
0.0121
52
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
53
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
CO2
0.0000
0.0019
0.0000
0.0047
0.0000
0.0056
55
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
56
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
61
K VALUE
62 63
COMPONENTS
MIXED
LIGHT
HEAVY
64
CO
1.000
1.000
---
65
H2O
1.000
1.000
---
66
Oxygen
1.000
1.000
---
67
Methane
1.000
1.000
---
---
---
68 69
H2S
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 74 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 25 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
Hydrogen
1.000
1.000
---
13
Ethane
1.000
1.000
---
14
Propane
---
---
---
15
CO2
1.000
1.000
---
16
Nitrogen
1.000
1.000
---
---
---
---
17
Air
18
Mercury
---
---
---
19
MEAmine
---
---
---
20
Ammonia
---
---
---
21
UNIT OPERATIONS
22 23 24
FEED TO LNG:
PRODUCT FROM
E-1 PRECALENTADOR DE GAS-VAPOR DE Conversion PROCESO Reactor:
25
LOGICAL CONNECTION
H-1 REFORMADOR SECUNDARIO
UTILITIES
26 27
( No utilities reference this stream )
28
PROCESS UTILITY
29 30 31
DYNAMICS
32 33
Pressure Specification
(Inactive):
34
Flow Specification
(Inactive) Molar:
248.7 psia 1.509e+005 lbmole/hr Mass:
35
2.717e+006 lb/hrStd Ideal Liq Volume: 1.893e+005 barrel/day
User Variables
36 37
NOTES
38 39 40
Description
41 42 43
Material Stream: 26
44 45 46
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
47 48
Overall
Vapour Phase
49
Vapour / Phase Fraction
50
Temperature:
51
Pressure:
52
Molar Flow
53
Mass Flow
54
Std Ideal Liq Vol Flow
(barrel/day)
1.893e+005
1.893e+005
55
Molar Enthalpy
(Btu/lbmole)
-9.540e+004
-9.540e+004
56
Molar Entropy
(Btu/lbmole-F)
57
Heat Flow
58
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
951.0
951.0
(psia)
244.7
(lbmole/hr) (lb/hr)
244.7
1.509e+005
1.509e+005
2.717e+006
2.717e+006
44.08
44.08
(Btu/hr)
-1.440e+010
-1.440e+010
(barrel/day)
* 1.862e+005
1.862e+005
59
PROPERTIES
60 61
Overall
Vapour Phase
62
Molecular Weight
63
Molar Density
64
Mass Density
65
Act. Volume Flow
66
Mass Enthalpy
(Btu/lb)
-5300
-5300
67
Mass Entropy
(Btu/lb-F)
2.449
2.449
68
Heat Capacity
9.451
9.451
69
Aspen Technology Inc. Licensed to: LEGENDS
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F)
1.640e-002 0.2952 3.934e+007
18.00 1.640e-002 0.2952 3.934e+007
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 75 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 26 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Heat Capacity
13
Vapour Phase
(Btu/lb-F)
0.5250
LHV Molar Basis (Std)
(Btu/lbmole)
1217
14
HHV Molar Basis (Std)
(Btu/lbmole)
15
HHV Mass Basis (Std)
16
CO2 Loading
17
CO2 App ML Con
18
CO2 App WT Con
19
LHV Mass Basis (Std)
20 21
(Btu/lb)
1.874e+004
0.5250 1217 1.874e+004
1041
1041
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
67.59
67.59
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
22
Phase Fraction [Act. Vol. Basis]
1.000
1.000
23
Mass Exergy
(Btu/lb)
530.7
---
24
Partial Pressure of CO2
(psia)
0.4670
---
25
Cost Based on Flow
(Cost/s)
0.0000
0.0000
26
Act. Gas Flow
27
Avg. Liq. Density
28
(ACFM)
1.534e+005
1.534e+005
(lbmole/ft3)
3.408
3.408
Specific Heat
(Btu/lbmole-F)
9.451
9.451
29
Std. Gas Flow
(MMSCFD)
1372
1372
30
Std. Ideal Liq. Mass Density
61.35
61.35
31
Act. Liq. Flow
32
Z Factor
33
Watson K
34
User Property
35
Partial Pressure of H2S
36
Cp/(Cp - R)
37
Cp/Cv
38
Heat of Vap.
39
Kinematic Viscosity
40
Liq. Mass Density (Std. Cond)
41
Liq. Vol. Flow (Std. Cond)
42
Liquid Fraction
43
Molar Volume
44
Mass Heat of Vap.
45
Phase Fraction [Molar Basis]
46
Surface Tension
47
Thermal Conductivity
48
Viscosity
49
Cv (Semi-Ideal)
50
Mass Cv (Semi-Ideal)
51
Cv
52
Mass Cv
53
Cv (Ent. Method)
54
Mass Cv (Ent. Method)
55
Cp/Cv (Ent. Method)
56
Reid VP at 37.8 C
57
True VP at 37.8 C
58
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
59
Viscosity Index
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
---
0.9856
0.9856
10.10
10.10
---
---
0.0000
---
1.266
1.266
1.295
1.295
3.130e+004 4.652 62.38 1.862e+005
--4.652 62.38 1.862e+005
0.0000
0.0000
(ft3/lbmole)
60.98
60.98
(Btu/lb)
1739
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
3.954e-002
3.954e-002
2.200e-002
2.200e-002
7.465
7.465
0.4147
0.4147
7.300
7.300
0.4056
0.4056
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.862e+005 -2.091
60
1.862e+005 ---
COMPOSITION
61 62
Overall Phase
63 64
COMPONENTS
65
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
66
CO
139.8961
0.0009
67
H2O
148599.0282
0.9844
68
Oxygen
135.4346
0.0009
69
Aspen Technology Inc. Licensed to: LEGENDS
MASS FLOW (lb/hr) 3918.6150 2.677026425e+06 4333.9059
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0014
335.6551
0.0018
0.9853
183673.4882
0.9702
0.0016
260.8421
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0014
Page 76 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 26 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14 15
Methane
16
H2S
17
Hydrogen
18
Ethane
19
Propane
20
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
1156.4711
0.0077
2331.4459
0.0009
2285.1811
0.0121
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
CO2
288.0576
0.0019
12677.3302
0.0047
1051.7579
0.0056
21
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
22
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Total
150949.1460
1.0000
27
2.717102502e+06
1.0000
189315.9286
Vapour Phase
28 29
COMPONENTS
30
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
1.0000
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0014
335.6551
0.0018
0.9853
183673.4882
0.9702
31
CO
139.8961
0.0009
32
H2O
148599.0282
0.9844
33
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
34
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
35
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Hydrogen
1156.4711
0.0077
2331.4459
0.0009
2285.1811
0.0121
37
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
38
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
CO2
288.0576
0.0019
12677.3302
0.0047
1051.7579
0.0056
40
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
41
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Total
150949.1460
3918.6150 2.677026425e+06
1.0000
2.717102502e+06
46
189315.9286
1.0000
K VALUE
47 48
1.0000
COMPONENTS
MIXED
LIGHT
HEAVY
49
CO
---
---
---
50
H2O
---
---
---
51
Oxygen
---
---
---
52
Methane
---
---
---
---
---
---
53
H2S
54
Hydrogen
---
---
---
55
Ethane
---
---
---
56
Propane
---
---
---
57
CO2
---
---
---
58
Nitrogen
---
---
---
---
---
---
59
Air
60
Mercury
---
---
---
61
MEAmine
---
---
---
62
Ammonia
---
---
---
63
UNIT OPERATIONS
64 65 66
FEED TO Conversion Reactor:
PRODUCT FROM D-2 Convertidor de CO2-1 LNG:
LOGICAL CONNECTION
E-1 PRECALENTADOR DE GAS-VAPOR DE PROCESO
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 77 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 26 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Inactive):
18
Flow Specification
(Inactive) Molar:
244.7 psia 1.509e+005 lbmole/hr Mass:
19
2.717e+006 lb/hrStd Ideal Liq Volume: 1.893e+005 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: 27
28 29 30
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
39
Molar Enthalpy
(Btu/lbmole)
40
Molar Entropy
(Btu/lbmole-F)
41
Heat Flow
42
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
700.0
700.0
700.0
(psia)
241.7
241.7
241.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-9.774e+004
-9.774e+004
0.0000 -9.774e+004
42.29
42.29
42.29
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
43
PROPERTIES
44 45
Overall
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Vapour Phase 18.00
(lbmole/ft3)
1.999e-002
Liquid Phase 18.00 1.999e-002
0.3599
0.3599
0.3599
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-5430
-5430
-5430
51
Mass Entropy
(Btu/lb-F)
2.349
2.349
2.349
52
Heat Capacity
9.167
9.167
9.167
53
Mass Heat Capacity
0.5092
0.5092
0.5092
54
LHV Molar Basis (Std)
(Btu/lbmole)
55
HHV Molar Basis (Std)
(Btu/lbmole)
56
HHV Mass Basis (Std)
57
CO2 Loading
58
CO2 App ML Con
59
CO2 App WT Con
60
LHV Mass Basis (Std)
61
Phase Fraction [Vol. Basis]
62
Phase Fraction [Mass Basis]
63
Phase Fraction [Act. Vol. Basis]
64
Mass Exergy
65
Partial Pressure of CO2
66
Cost Based on Flow
67
Act. Gas Flow
68
Avg. Liq. Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
1.999e-002
18.00
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1211 1.873e+004
1211 1.873e+004
1211 1.873e+004
1041
1041
1041
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
67.27
67.27
67.27
---
---
1.000
0.0000
0.0000
1.000
---
---
---
(Btu/lb)
454.5
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
---
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 78 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 27 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Specific Heat
(Btu/lbmole-F)
9.167
9.167
9.167
13
Std. Gas Flow
(MMSCFD)
0.0000
0.0000
0.0000
14
Std. Ideal Liq. Mass Density
(lb/ft3)
61.32
61.32
61.32
15
Act. Liq. Flow
(USGPS)
0.0000
---
0.0000
16
Z Factor
17
Watson K
18
User Property
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
41
True VP at 37.8 C
42 43
(psia)
(Btu/lbmole) (cSt)
---
0.9715
0.9715
10.22
10.22
10.22
---
---
---
0.0000
---
---
1.277
1.277
1.277
1.328
1.328
1.328
3.129e+004 0.6239
(lb/ft3) (barrel/day)
---
---
3.029
0.6239
62.37
62.37
62.37
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
50.02
50.02
50.02
(Btu/lb)
1739
---
---
0.0000
0.0000
1.0000
---
0.3093
(dyne/cm)
0.3093
(Btu/hr-ft-F)
0.1928
(cP)
3.597e-003
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
3.103e-002 1.746e-002
0.1928 3.597e-003
7.181
7.181
7.181
0.3989
0.3989
0.3989
6.905
6.905
6.905
0.3836
0.3836
0.3836
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-4.143
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
44
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
50
CO
0.0000
0.0006
0.0000
0.0009
0.0000
0.0012
51
H2O
0.0000
0.9841
0.0000
0.9849
0.0000
0.9694
52
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
53
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
54
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Hydrogen
0.0000
0.0080
0.0000
0.0009
0.0000
0.0126
56
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
57
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
CO2
0.0000
0.0022
0.0000
0.0055
0.0000
0.0065
59
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
60
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 79 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 27 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0006
0.0000
0.0009
0.0000
0.0012
16
H2O
0.0000
0.9841
0.0000
0.9849
0.0000
0.9694
17
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
18
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0080
0.0000
0.0009
0.0000
0.0126
21
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0022
0.0000
0.0055
0.0000
0.0065
24
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0006
0.0000
0.0009
0.0000
0.0012
35
H2O
0.0000
0.9841
0.0000
0.9849
0.0000
0.9694
36
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
37
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0080
0.0000
0.0009
0.0000
0.0126
40
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0022
0.0000
0.0055
0.0000
0.0065
43
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
1.000
1.000
---
53
H2O
1.000
1.000
---
54
Oxygen
1.000
1.000
---
55
Methane
1.000
1.000
---
---
---
---
56
H2S
57
Hydrogen
1.000
1.000
---
58
Ethane
1.000
1.000
---
59
Propane
---
---
---
60
CO2
1.000
1.000
---
61
Nitrogen
1.000
1.000
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 80 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 27 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Conversion Reactor:
13
LOGICAL CONNECTION
D-2 Convertidor de CO2-1
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
241.7 psia 0.0000 lbmole/hrMass:
23
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 28
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
1.0000
1.0000
0.0000
(F)
700.0*
700.0
700.0
(psia)
241.7
241.7
(lbmole/hr) (lb/hr)
241.7
1.509e+005
1.509e+005
0.0000
2.717e+006
2.717e+006
0.0000
1.894e+005
1.894e+005
-9.774e+004
-9.774e+004
42.29
42.29
0.0000 -9.774e+004 42.29
(Btu/hr)
-1.475e+010
-1.475e+010
0.0000
(barrel/day)
* 1.862e+005
1.862e+005
0.0000
47
PROPERTIES
48 49
Overall
Vapour Phase
Liquid Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-5430
-5430
-5430
55
Mass Entropy
(Btu/lb-F)
2.349
2.349
2.349
56
Heat Capacity
9.167
9.167
9.167
57
Mass Heat Capacity
0.5092
0.5092
0.5092
58
LHV Molar Basis (Std)
(Btu/lbmole)
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66 67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
0.3599 3.228e+007
1211 1.873e+004
1.999e-002 0.3599 3.228e+007
1211 1.873e+004
18.00 1.999e-002 0.3599 0.0000
1211 1.873e+004
1041
1041
1041
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
67.27
67.27
67.27
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
454.5
---
---
Licensed to: LEGENDS
(Btu/lb)
1.999e-002
18.00
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 81 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 28 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Liquid Phase
(psia)
0.5396
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1.258e+005
1.258e+005
---
(lbmole/ft3)
3.407
3.407
Specific Heat
(Btu/lbmole-F)
9.167
9.167
9.167
Std. Gas Flow
(MMSCFD)
1372
1372
0.0000
(lb/ft3)
61.32
61.32
61.32
(USGPS)
---
---
---
---
0.9715
0.9715
10.22
10.22
10.22
---
---
---
0.0000
---
---
1.277
1.277
1.277
1.328
1.328
1.328
(psia)
(Btu/lbmole) (cSt)
3.129e+004 3.029
(lb/ft3)
62.37
(barrel/day)
1.862e+005
3.407
---
---
3.029
0.6239
62.37 1.862e+005
62.37 0.0000
0.0000
0.0000
1.000
(ft3/lbmole)
50.02
50.02
50.02
(Btu/lb)
1739
---
---
1.0000
1.0000
0.0000
---
0.3093
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
--3.103e-002
3.103e-002
1.746e-002
1.746e-002
0.1928 3.597e-003
7.181
7.181
7.181
0.3989
0.3989
0.3989
6.905
6.905
6.905
0.3836
0.3836
0.3836
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
1.862e+005 -4.143
48
1.862e+005 ---
--0.0000 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53 54
CO
55
H2O
56
MOLAR FLOW (lbmole/hr) 90.9324
MOLE FRACTION 0.0006
MASS FLOW (lb/hr) 2547.0997
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
57
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
60
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
63
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
69
Aspen Technology Inc. Licensed to: LEGENDS
150949.1460
1.0000
2.676144340e+06
Vapour Fraction
2.717102487e+06
1.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
189413.4567
1.0000
Page 82 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 28 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14 15
CO
16
H2O
17
MOLAR FLOW (lbmole/hr) 90.9324
MOLE FRACTION
MASS FLOW (lb/hr)
0.0006
2547.0997
MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
18
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
21
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
24
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
150949.1460
2.676144340e+06
Phase Fraction
1.0000
30
2.717102487e+06
1.0000
189413.4567
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0006
0.0000
0.0009
0.0000
0.0012
35
H2O
0.0000
0.9841
0.0000
0.9849
0.0000
0.9694
36
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
37
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0080
0.0000
0.0009
0.0000
0.0126
40
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0022
0.0000
0.0055
0.0000
0.0065
43
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
1.000
1.000
---
53
H2O
1.000
1.000
---
54
Oxygen
1.000
1.000
---
55
Methane
1.000
1.000
---
---
---
---
56
H2S
57
Hydrogen
1.000
1.000
---
58
Ethane
1.000
1.000
---
59
Propane
---
---
---
60
CO2
1.000
1.000
---
61
Nitrogen
1.000
1.000
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 83 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 28 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
LNG:
LNG-100 Conversion Reactor:
13
LOGICAL CONNECTION
D-2 Convertidor de CO2-1
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
241.7 psia 1.509e+005 lbmole/hr Mass:
23
2.717e+006 lb/hrStd Ideal Liq Volume: 1.894e+005 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 29
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
1.894e+005
1.894e+005
43
Molar Enthalpy
(Btu/lbmole)
-9.778e+004
-9.778e+004
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
695.0
695.0
(psia)
241.7
(lbmole/hr) (lb/hr)
241.7
1.509e+005
1.509e+005
2.717e+006
2.717e+006
42.25
42.25
(Btu/hr)
-1.476e+010
-1.476e+010
(barrel/day)
* 1.862e+005
1.862e+005
47
PROPERTIES
48 49
Overall
Vapour Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-5432
-5432
55
Mass Entropy
(Btu/lb-F)
2.347
2.347
56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
0.3616 3.212e+007
18.00 2.009e-002 0.3616 3.212e+007
9.162
9.162
0.5090
0.5090
1211 1.873e+004
1211 1.873e+004
1041
1041
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
67.27
67.27
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
67
Phase Fraction [Act. Vol. Basis]
1.000
1.000
68
Mass Exergy
453.1
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
2.009e-002
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 84 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 29 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Vapour Phase
(psia)
0.5396
---
(Cost/s)
0.0000
0.0000
(ACFM)
1.253e+005
1.253e+005
(lbmole/ft3)
3.407
3.407
Specific Heat
(Btu/lbmole-F)
9.162
9.162
17
Std. Gas Flow
(MMSCFD)
1372
1372
18
Std. Ideal Liq. Mass Density
61.32
61.32
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt)
---
---
0.9711
0.9711
10.22
10.22
---
---
0.0000
---
1.277
1.277
1.328
1.328
3.129e+004 3.000
(lb/ft3)
62.37
(barrel/day)
1.862e+005
--3.000 62.37 1.862e+005
0.0000
0.0000
(ft3/lbmole)
49.79
49.79
(Btu/lb)
1739
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
3.086e-002
3.086e-002
1.737e-002
1.737e-002
7.176
7.176
0.3987
0.3987
6.897
6.897
0.3832
0.3832
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.862e+005 -4.197
48
1.862e+005 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53 54
CO
55
H2O
56
MOLAR FLOW (lbmole/hr) 90.9324
MOLE FRACTION 0.0006
MASS FLOW (lb/hr) 2547.0997
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
57
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
60
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
63
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
69
Aspen Technology Inc. Licensed to: LEGENDS
150949.1460
1.0000
2.676144340e+06
Vapour Fraction
2.717102487e+06
1.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
189413.4567
1.0000
Page 85 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 29 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14 15
CO
16
H2O
17
MOLE FRACTION
90.9324
MASS FLOW (lb/hr)
0.0006
Phase Fraction MASS FRACTION
2547.0997
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
18
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
21
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
24
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
150949.1460
2.676144340e+06
1.000
1.0000
2.717102487e+06
30
1.0000
189413.4567
1.0000
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Cooler:
E-100
51
LNG:
LOGICAL CONNECTION LNG-100
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Inactive) Molar:
61
241.7 psia 1.509e+005 lbmole/hr Mass:
2.717e+006 lb/hrStd Ideal Liq Volume: 1.894e+005 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 86 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 30
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Vapour Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
1.894e+005
1.894e+005
18
Molar Enthalpy
(Btu/lbmole)
-9.980e+004
-9.980e+004
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
473.0*
473.0
(psia)
241.7
(lbmole/hr) (lb/hr)
241.7
1.509e+005
1.509e+005
2.717e+006
2.717e+006
40.31
40.31
(Btu/hr)
-1.506e+010
-1.506e+010
(barrel/day)
* 1.862e+005
1.862e+005
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-5544
-5544
30
Mass Entropy
(Btu/lb-F)
2.240
2.240
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
34
HHV Molar Basis (Std)
(Btu/lbmole)
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.563e-002 0.4614 2.517e+007
18.00 2.563e-002 0.4614 2.517e+007
9.047
9.047
0.5026
0.5026
1211 1.873e+004
1211 1.873e+004
1041
1041
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
67.27
67.27
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
(Btu/lb)
398.9
---
44
Partial Pressure of CO2
(psia)
0.5396
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48
(ACFM)
9.815e+004
9.815e+004
(lbmole/ft3)
3.407
3.407
Specific Heat
(Btu/lbmole-F)
9.047
9.047
49
Std. Gas Flow
(MMSCFD)
1372
1372
50
Std. Ideal Liq. Mass Density
61.32
61.32
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
---
0.9421
0.9421
10.22
10.22
---
---
0.0000
---
1.281
1.281
1.379
1.379
3.129e+004 1.844 62.37 1.862e+005
--1.844 62.37 1.862e+005
0.0000
0.0000
(ft3/lbmole)
39.01
39.01
(Btu/lb)
1739
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
2.346e-002
2.346e-002
1.363e-002
1.363e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 87 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 30 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 7.062
7.062
0.3923
0.3923
6.563
6.563
0.3646
0.3646
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.862e+005
1.862e+005
---
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28 29
CO
30
H2O
31
MOLAR FLOW (lbmole/hr) 90.9324
MOLE FRACTION
MASS FLOW (lb/hr)
0.0006
2547.0997
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
32
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
35
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
38
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
150949.1460
2.676144340e+06
Vapour Fraction
1.0000
44
2.717102487e+06
1.0000
189413.4567
Vapour Phase
45 46
COMPONENTS
47 48
CO
49
H2O
50
MOLAR FLOW (lbmole/hr) 90.9324
MOLE FRACTION 0.0006
MASS FLOW (lb/hr) 2547.0997
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
51
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
54
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
57
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
150949.1460
1.0000
63
2.717102487e+06
1.0000
189413.4567
1.0000
K VALUE
64 65
2.676144340e+06
1.0000
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 88 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 30 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO Conversion Reactor:
PRODUCT FROM
LOGICAL CONNECTION
D-2B Convertidor de CO2 Cooler:
E-100
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
241.7 psia 1.509e+005 lbmole/hr Mass:
37
2.717e+006 lb/hrStd Ideal Liq Volume: 1.894e+005 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 31
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.0000
0.0000
1.0000
(F)
472.5
472.5
472.5
(psia)
235.7
235.7
235.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-1.152e+005
-9.980e+004
0.0000 -1.152e+005
23.69
40.36
23.69
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 18.02
(lbmole/ft3) (lb/ft3)
2.265
18.00 2.497e-002
Aqueous Phase 18.02 2.265
40.80
0.4495
40.80
(barrel/day)
0.0000
0.0000
0.0000
(Btu/lb)
-6394
-5544
-6394
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 89 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 31 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
(Btu/lb-F)
Vapour Phase
Aqueous Phase
1.315
2.242
1.315
23.44
9.031
23.44
(Btu/lb-F)
1.301
0.5017
1.301
LHV Molar Basis (Std)
(Btu/lbmole)
2.104
1207
16
HHV Molar Basis (Std)
(Btu/lbmole)
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
Phase Fraction [Vol. Basis]
23
Phase Fraction [Mass Basis]
24
Phase Fraction [Act. Vol. Basis]
25
Mass Exergy
26
Partial Pressure of CO2
27
Cost Based on Flow
28
Act. Gas Flow
29
Avg. Liq. Density
30
(Btu/lbmole-F)
(Btu/lb)
1.763e+004
1.873e+004
2.104 1.763e+004
978.8
1040
978.8
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
0.1168
67.07
0.1168
---
---
1.000
0.0000
0.0000
1.000
---
---
---
(Btu/lb)
113.2
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
23.44
9.031
23.44
31
Std. Gas Flow
(MMSCFD)
0.0000
32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
0.0000
0.0000
(lb/ft3)
62.30
61.30
62.30
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt)
---
0.9435
9.468
10.30
9.468
---
---
---
0.0000
---
---
1.093
1.282
1.093
1.093
1.377
1.093
1.529e+004 0.1672
(lb/ft3)
1.040e-002
---
---
1.891
0.1672
63.35
62.36
63.35
(barrel/day)
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
0.4415
40.04
0.4415
(Btu/lb)
848.5
---
---
0.0000
0.0000
1.0000
(dyne/cm)
27.39
(Btu/hr-ft-F)
0.3597
2.343e-002
0.3597
0.1093
1.362e-002
0.1093
(cP) (Btu/lbmole-F)
---
27.39
21.46
7.045
21.46
1.191
0.3914
1.191
21.46
6.561
21.46
1.191
0.3645
1.191
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
253.6
---
253.6
0.0000
0.0000
0.0000
---
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
0.0000
LIQUID VOLUME FRACTION 0.0000
Page 90 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 31 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
H2O
0.0000
1.0000
0.0000
0.9999
0.0000
0.9999
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0004
0.0000
0.0006
0.0000
0.0007
34
H2O
0.0000
0.9839
0.0000
0.9847
0.0000
0.9688
35
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
36
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0082
0.0000
0.0009
0.0000
0.0129
39
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0000
0.0024
0.0000
0.0060
0.0000
0.0071
42
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0065
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
48
Aqueous Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
52
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
H2O
0.0000
1.0000
0.0000
0.9999
0.0000
0.9999
54
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 91 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 31 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
572.4
---
572.4
13
H2O
0.9839
---
0.9839
14
Oxygen
309.2
---
309.2
15
Methane
1890
---
1890
---
---
---
Hydrogen
448.4
---
448.4
18
Ethane
4838
---
4838
19
Propane
---
---
---
20
CO2
150.1
---
150.1
21
Nitrogen
912.9
---
912.9
---
---
---
16
H2S
17
22
Air
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Conversion Reactor:
30
LOGICAL CONNECTION
D-2B Convertidor de CO2
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
235.7 psia 0.0000 lbmole/hrMass:
40
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 32
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
1.0000
1.0000
0.0000
(F)
472.5
472.5
472.5
(psia)
235.7
235.7
(lbmole/hr) (lb/hr)
235.7
1.509e+005
1.509e+005
0.0000
2.717e+006
2.717e+006
0.0000
1.895e+005
1.895e+005
-9.980e+004
-9.980e+004
40.36
40.36
0.0000 -1.152e+005 23.69
(Btu/hr)
-1.506e+010
-1.506e+010
0.0000
(barrel/day)
* 1.863e+005
1.863e+005
0.0000
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 18.00
(lbmole/ft3)
2.497e-002
18.00 2.497e-002
Aqueous Phase 18.02 2.265
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 92 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 32 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-5544
-5544
-6394
15
Mass Entropy
(Btu/lb-F)
2.242
2.242
1.315
16
Heat Capacity
9.031
9.031
23.44
17
Mass Heat Capacity
(Btu/lb-F)
0.5017
0.5017
1.301
18
LHV Molar Basis (Std)
(Btu/lbmole)
1207
1207
19
HHV Molar Basis (Std)
(Btu/lbmole)
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26 27
Phase Fraction [Act. Vol. Basis]
28
Mass Exergy
29
Partial Pressure of CO2
30
Cost Based on Flow
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
(Btu/lbmole-F)
(Btu/lb)
0.4495 2.584e+007
1.873e+004
0.4495 2.584e+007
1.873e+004
40.80 0.0000
2.104 1.763e+004
1040
1040
978.8
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
67.07
67.07
0.1168
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
397.5
---
---
(psia)
0.5759
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1.007e+005
1.007e+005
---
(lbmole/ft3)
3.405
3.405
Specific Heat
(Btu/lbmole-F)
9.031
9.031
23.44
Std. Gas Flow
(MMSCFD)
1372
1372
0.0000
(lb/ft3)
61.30
61.30
62.30
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F)
3.458
---
0.9435
10.30
10.30
9.468
---
---
---
0.0000
---
---
1.282
1.282
1.093
1.377
1.377
1.093
3.004e+004 1.891 62.36 1.863e+005
1.040e-002
---
---
1.891
0.1672
62.36 1.863e+005
63.35 0.0000
0.0000
0.0000
1.000
40.04
40.04
0.4415
1669
---
---
1.0000
1.0000
0.0000
---
---
27.39
2.343e-002
2.343e-002
0.3597
1.362e-002
1.362e-002
0.1093
7.045
7.045
21.46
0.3914
0.3914
1.191
6.561
6.561
21.46
0.3645
0.3645
1.191
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
253.6
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
1.863e+005 ---
1.863e+005 ---
0.0000 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 93 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 32 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14 15
CO
16
H2O
17
MOLAR FLOW (lbmole/hr) 59.1061
MOLE FRACTION 0.0004
MASS FLOW (lb/hr) 1655.6148
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0006
141.8143
0.0007
0.9847
183573.6290
0.9688
148518.2382
0.9839
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
18
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1237.2611
0.0082
2494.3185
0.0009
2444.8217
0.0129
21
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
368.8476
0.0024
16232.8731
0.0060
1346.7389
0.0071
24
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0065
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
150949.1460
2.675570985e+06
Vapour Fraction
1.0000
2.717102478e+06
30
1.0000
Vapour Phase
31 32
COMPONENTS
33 34
CO
35
H2O
36
MOLAR FLOW (lbmole/hr) 59.1061
MOLE FRACTION 0.0004
MASS FLOW (lb/hr) 1655.6148
Phase Fraction MASS FRACTION
1.0000 1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0006
141.8143
0.0007
0.9847
183573.6290
0.9688
148518.2382
0.9839
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
37
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1237.2611
0.0082
2494.3185
0.0009
2444.8217
0.0129
40
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
368.8476
0.0024
16232.8731
0.0060
1346.7389
0.0071
43
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0065
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
150949.1460
2.675570985e+06
189476.8501
1.0000
49
2.717102478e+06
1.0000
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
189476.8501 Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000 0.0000 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
0.0000
1.0000
0.0000
0.9999
0.0000
0.9999
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 94 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 32 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
572.4
---
572.4
13
H2O
0.9839
---
0.9839
14
Oxygen
309.2
---
309.2
15
Methane
1890
---
1890
---
---
---
Hydrogen
448.4
---
448.4
18
Ethane
4838
---
4838
19
Propane
---
---
---
20
CO2
150.1
---
150.1
21
Nitrogen
912.9
---
912.9
---
---
---
16
H2S
17
22
Air
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Valve:
VLV-100 Conversion Reactor:
30
LOGICAL CONNECTION
D-2B Convertidor de CO2
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
235.7 psia 1.509e+005 lbmole/hr Mass:
40
2.717e+006 lb/hrStd Ideal Liq Volume: 1.895e+005 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 33
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
1.895e+005
1.895e+005
60
Molar Enthalpy
(Btu/lbmole)
-9.980e+004
-9.980e+004
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
471.9
471.9
(psia)
231.7*
(lbmole/hr) (lb/hr)
231.7
1.509e+005
1.509e+005
2.717e+006
2.717e+006
40.39
40.39
(Btu/hr)
-1.506e+010
-1.506e+010
(barrel/day)
* 1.863e+005
1.863e+005
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 18.00
(lbmole/ft3)
2.454e-002
18.00 2.454e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 95 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 33 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-5544
-5544
15
Mass Entropy
(Btu/lb-F)
2.244
2.244
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
19
HHV Molar Basis (Std)
(Btu/lbmole)
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.4417 2.629e+007
0.4417 2.629e+007
9.020
9.020
0.5011
0.5011
1207 1.873e+004
1207 1.873e+004
1040
1040
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
67.07
67.07
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
27
Phase Fraction [Act. Vol. Basis]
1.000
1.000
28
Mass Exergy
(Btu/lb)
396.6
---
29
Partial Pressure of CO2
(psia)
0.5662
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33
(ACFM)
1.025e+005
1.025e+005
(lbmole/ft3)
3.405
3.405
Specific Heat
(Btu/lbmole-F)
9.020
9.020
34
Std. Gas Flow
(MMSCFD)
1372
1372
35
Std. Ideal Liq. Mass Density
61.30
61.30
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
---
0.9444
0.9444
10.30
10.30
---
---
0.0000
---
1.282
1.282
1.375
1.375
3.012e+004 1.922 62.36 1.863e+005
--1.922 62.36 1.863e+005
0.0000
0.0000
(ft3/lbmole)
40.75
40.75
(Btu/lb)
1673
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
2.339e-002
2.339e-002
1.360e-002
1.360e-002
7.034
7.034
0.3908
0.3908
6.559
6.559
0.3644
0.3644
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.863e+005 ---
1.863e+005 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 96 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 33 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14 15
CO
16
H2O
17
MOLAR FLOW (lbmole/hr) 59.1061
MOLE FRACTION
MASS FLOW (lb/hr)
0.0004
1655.6148
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0006
141.8143
0.0007
0.9847
183573.6290
0.9688
148518.2382
0.9839
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
18
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1237.2611
0.0082
2494.3185
0.0009
2444.8217
0.0129
21
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
368.8476
0.0024
16232.8731
0.0060
1346.7389
0.0071
24
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0065
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
150949.1460
2.675570985e+06
Vapour Fraction
1.0000
30
2.717102478e+06
1.0000
189476.8501
Vapour Phase
31 32
COMPONENTS
33 34
CO
35
H2O
36
MOLAR FLOW (lbmole/hr) 59.1061
MOLE FRACTION 0.0004
MASS FLOW (lb/hr) 1655.6148
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0006
141.8143
0.0007
0.9847
183573.6290
0.9688
148518.2382
0.9839
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
37
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1237.2611
0.0082
2494.3185
0.0009
2444.8217
0.0129
40
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
368.8476
0.0024
16232.8731
0.0060
1346.7389
0.0071
43
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0065
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
150949.1460
1.0000
49
2.717102478e+06
1.0000
189476.8501
1.0000
K VALUE
50 51
2.675570985e+06
1.0000
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 97 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 33 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Cooler:
E-102
LOGICAL CONNECTION
Valve:
VLV-100
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 231.7 psia
1.509e+005 lbmole/hr Mass:
23
2.717e+006 lb/hrStd Ideal Liq Volume: 1.895e+005 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 34
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
1.895e+005
43
Molar Enthalpy
(Btu/lbmole)
-1.209e+005
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Aqueous Phase
0.0156
0.0156
0.9844
(F)
110.0*
110.0
110.0
(psia)
231.7
231.7
(lbmole/hr) (lb/hr)
1.509e+005 2.717e+006
14.21
2349 3.772e+004 5579 -2.337e+004 31.06
231.7 1.486e+005 2.679e+006 1.839e+005 -1.225e+005 13.95
(Btu/hr)
-1.825e+010
-5.490e+007
-1.820e+010
(barrel/day)
* 1.863e+005
3.801e+006
1.807e+005
47
PROPERTIES
48 49
Overall
Vapour Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-6717
-1455
-6791
55
Mass Entropy
(Btu/lb-F)
0.7896
1.934
0.7735
56
Heat Capacity
57
Mass Heat Capacity
58
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
25.88 4.488e+005
3.799e-002 0.6102 2.642e+005
18.03 3.442 62.06 1.846e+005
18.39
7.432
18.57
(Btu/lb-F)
1.022
0.4628
1.030
LHV Molar Basis (Std)
(Btu/lbmole)
1207
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
(lbmole/ft3)
63
CO2 App WT Con
(lbmol/lb)
64
LHV Mass Basis (Std)
(Btu/lb)
65
Phase Fraction [Vol. Basis]
2.945e-002
2.945e-002
0.9706
66
Phase Fraction [Mass Basis]
1.388e-002
1.388e-002
0.9861
67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lbmole-F)
1.438
16.06
(Btu/lb)
(Btu/lb)
1.873e+004
7.748e+004 8.874e+004
1.714 1.762e+004
1040
5525
---
---
977.3
---
---
2.053e-003
---
---
3.308e-005
67.07
4824
9.508e-002
---
0.5888
0.5888
0.4112
4.357
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 98 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 34 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Aqueous Phase
(psia)
27.64
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1030
1030
---
(lbmole/ft3)
3.405
1.799
3.454
Specific Heat
(Btu/lbmole-F)
18.39
7.432
18.57
Std. Gas Flow
(MMSCFD)
1372
21.35
1351
(lb/ft3)
61.30
28.90
62.28
(USGPS)
89.72
---
---
0.9975
10.30
10.51
8.466
---
---
---
0.0000
---
---
1.121
1.365
1.120
1.002
1.391
1.157
(psia)
(Btu/lbmole) (cSt)
3.012e+004 ---
(lb/ft3)
62.36
(barrel/day) (ft3/lbmole) (Btu/lb)
1.863e+005
89.72 1.101e-002
---
---
1.395
0.6158
4.242e-002 3.801e+006
63.37 1.807e+005
0.9844
0.0000
1.000
0.6955
26.32
0.2905
1673
---
---
0.0156
0.0156
0.9844
(dyne/cm)
68.86
(Btu/hr-ft-F)
---
4.305e-002
0.3672
---
1.363e-002
0.6121
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
68.86
16.41
5.447
16.58
0.9116
0.3391
0.9197
18.35
5.345
16.05
1.019
0.3328
0.8900
---
---
15.85
---
---
0.8789
---
---
1.172
---
---
---
---
---
232.7
3.982e+006 -4.417
48
3.801e+006 ---
1.807e+005 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53 54
CO
55
H2O
56
MOLAR FLOW (lbmole/hr) 59.1061
MOLE FRACTION 0.0004
MASS FLOW (lb/hr) 1655.6148
MASS FRACTION
0.0156
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0006
141.8143
0.0007
0.9847
183573.6290
0.9688
148518.2382
0.9839
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
57
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1237.2611
0.0082
2494.3185
0.0009
2444.8217
0.0129
60
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
368.8476
0.0024
16232.8731
0.0060
1346.7389
0.0071
63
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0065
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
69
Aspen Technology Inc. Licensed to: LEGENDS
150949.1460
1.0000
2.675570985e+06
Vapour Fraction
2.717102478e+06
1.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
189476.8501
1.0000
Page 99 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 34 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.556e-002
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
16
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
17
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
18
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
21
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
24
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
30
37720.7641
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9844 LIQUID VOLUME FRACTION
34
CO
35
H2O
36
Oxygen
0.6059
0.0000
19.3875
0.0000
1.1669
0.0000
37
Methane
0.0012
0.0000
0.0186
0.0000
0.0043
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
2.2934
0.0000
4.6235
0.0000
4.5317
0.0000
40
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
88.6369
0.0006
3900.8838
0.0015
323.6317
0.0018
43
Nitrogen
5.0873
0.0000
142.5111
0.0001
12.1013
0.0001
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.1299 148503.7872
148600.5418
0.0000 0.9993
1.0000
49
2.679381713e+06
0.0000
0.3118
0.9985
0.0000
183555.7671
1.0000
0.9981
183897.5147
1.0000
K VALUE
50 51
3.6398 2.675310649e+06
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
2.872e+004
---
53
H2O
6.157e-003
---
6.157e-003
54
Oxygen
1.408e+004
---
1.408e+004
55
Methane
4.136e+006
---
4.136e+006
56
H2S
57
---
---
2.872e+004
---
Hydrogen
3.407e+004
---
3.407e+004
58
Ethane
1.389e+008
---
1.389e+008
59
Propane
---
---
---
60
CO2
200.0
---
200.0
61
Nitrogen
6424
---
6424
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 100 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 34 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Separator:
D-10
LOGICAL CONNECTION
Cooler:
E-102
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
231.7 psia 1.509e+005 lbmole/hr Mass:
23
2.717e+006 lb/hrStd Ideal Liq Volume: 1.895e+005 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 35
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
1.0000
1.0000
0.0000
(F)
110.0
110.0
110.0
(psia)
231.7
231.7
231.7
2349
2349
0.0000
(lbmole/hr) (lb/hr)
3.772e+004 5579 -2.337e+004 31.06
3.772e+004 5579 -2.337e+004 31.06
0.0000 0.0000 -1.225e+005 13.95
(Btu/hr)
-5.490e+007
-5.490e+007
0.0000
(barrel/day)
* 3.801e+006
3.801e+006
0.0000
47
PROPERTIES
48 49
Overall
Vapour Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-1455
-1455
-6791
55
Mass Entropy
(Btu/lb-F)
1.934
1.934
0.7735
56
Heat Capacity
7.432
7.432
18.57
57
Mass Heat Capacity
0.4628
0.4628
1.030
58
LHV Molar Basis (Std)
(Btu/lbmole)
7.748e+004
7.748e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
8.874e+004
8.874e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66 67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
16.06 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
0.6102 2.642e+005
3.799e-002 0.6102 2.642e+005
18.03 3.442 62.06 0.0000
1.714 1.762e+004
5525
5525
977.3
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
(Btu/lb)
4824
4824
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
183.2
---
---
Licensed to: LEGENDS
(Btu/lb)
3.799e-002
16.06
(Btu/lb)
--9.508e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 101 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 35 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Aqueous Phase
(psia)
27.64
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1030
1030
---
(lbmole/ft3)
1.799
1.799
3.454
Specific Heat
(Btu/lbmole-F)
7.432
7.432
18.57
Std. Gas Flow
(MMSCFD)
21.35
21.35
0.0000
(lb/ft3)
28.90
28.90
62.28
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
0.9975
10.51
10.51
1.101e-002 8.466
---
---
---
0.0000
---
---
1.365
1.365
1.120
1.391
1.391
1.157
5706
---
---
1.395
1.395
0.6158
4.242e-002
4.242e-002
63.37
3.801e+006
3.801e+006
0.0000
0.0000
0.0000
1.000
26.32
26.32
0.2905
355.3
---
---
1.0000
1.0000
0.0000
---
---
68.86
4.305e-002
4.305e-002
0.3672
1.363e-002
1.363e-002
0.6121
5.447
5.447
16.58
0.3391
0.3391
0.9197
5.345
5.345
16.05
0.3328
0.3328
0.8900
---
---
15.85
---
---
0.8789
---
---
1.172
---
---
---
---
---
232.7
3.801e+006 -30.38
48
3.801e+006 ---
0.0000 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
54
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
55
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
56
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
57
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
60
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
63
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
2348.6041
1.0000
1.0000
5579.3353
69
Aspen Technology Inc. Licensed to: LEGENDS
37720.7641
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 102 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 35 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
16
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
17
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
18
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
21
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
24
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
30
37720.7641
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.9993
0.0000
0.9985
0.0000
0.9981
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0006
0.0000
0.0015
0.0000
0.0018
43
Nitrogen
0.0000
0.0000
0.0000
0.0001
0.0000
0.0001
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
2.872e+004
---
53
H2O
6.157e-003
---
6.157e-003
54
Oxygen
1.408e+004
---
1.408e+004
55
Methane
4.136e+006
---
4.136e+006
56
H2S
57
---
---
2.872e+004
---
Hydrogen
3.407e+004
---
3.407e+004
58
Ethane
1.389e+008
---
1.389e+008
59
Propane
---
---
---
60
CO2
200.0
---
200.0
61
Nitrogen
6424
---
6424
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 103 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 35 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Cooler:
Cooler
LOGICAL CONNECTION
Separator:
13
D-10
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
231.7 psia 2349 lbmole/hrMass:
23
3.772e+004 lb/hrStd Ideal Liq Volume:
5579 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 36
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
-1.225e+005
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Aqueous Phase
0.0000
0.0000
1.0000
(F)
110.0
110.0
110.0
(psia)
231.7
231.7
(lbmole/hr) (lb/hr)
231.7
1.486e+005
0.0000
1.486e+005
2.679e+006
0.0000
2.679e+006
1.839e+005
0.0000
13.95
-2.337e+004 31.06
1.839e+005 -1.225e+005 13.95
(Btu/hr)
-1.820e+010
0.0000
-1.820e+010
(barrel/day)
* 1.807e+005
0.0000
1.807e+005
47
PROPERTIES
48 49
Overall
Vapour Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-6791
-1455
-6791
55
Mass Entropy
(Btu/lb-F)
0.7735
1.934
0.7735
56
Heat Capacity
57
Mass Heat Capacity
58
18.03 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F)
3.442 62.06 1.846e+005
16.06 3.799e-002 0.6102 0.0000
18.03 3.442 62.06 1.846e+005
18.57
7.432
18.57
(Btu/lb-F)
1.030
0.4628
1.030
LHV Molar Basis (Std)
(Btu/lbmole)
1.714
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
(lbmole/ft3)
2.053e-003
63
CO2 App WT Con
(lbmol/lb)
64
LHV Mass Basis (Std)
(Btu/lb)
65
Phase Fraction [Vol. Basis]
66
(Btu/lb)
1.762e+004
7.748e+004 8.874e+004
977.3
5525
---
---
1.714 1.762e+004 977.3 ---
---
2.053e-003
3.308e-005
---
3.308e-005
9.508e-002
4824
9.508e-002
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
67
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
68
Mass Exergy
1.785
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 104 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 36 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Aqueous Phase
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
3.454
1.799
3.454
Specific Heat
(Btu/lbmole-F)
18.57
7.432
18.57
Std. Gas Flow
(MMSCFD)
1351
0.0000
1351
(lb/ft3)
62.28
28.90
62.28
(USGPS)
89.72
---
---
0.9975
8.466
10.51
8.466
---
---
---
0.0000
---
---
1.120
1.365
1.120
1.157
1.391
1.157
(psia)
(Btu/lbmole) (cSt)
1.631e+004 0.6158
(lb/ft3)
63.37
(barrel/day) (ft3/lbmole) (Btu/lb)
1.807e+005
89.72 1.101e-002
---
---
1.395
0.6158
4.242e-002 0.0000
63.37 1.807e+005
1.000
0.0000
1.000
0.2905
26.32
0.2905
904.5
---
---
0.0000
0.0000
1.0000
(dyne/cm)
68.86
(Btu/hr-ft-F)
0.3672
4.305e-002
0.3672
0.6121
1.363e-002
0.6121
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
68.86
16.58
5.447
16.58
0.9197
0.3391
0.9197
16.05
5.345
16.05
0.8900
0.3328
0.8900
15.85
---
15.85
0.8789
---
0.8789
1.172
---
1.172
---
---
---
232.7
---
232.7
1.807e+005 -4.382
48
0.0000 ---
1.807e+005 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
54
CO
55
H2O
56
Oxygen
0.6059
0.0000
19.3875
0.0000
1.1669
0.0000
57
Methane
0.0012
0.0000
0.0186
0.0000
0.0043
0.0000
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
2.2934
0.0000
4.6235
0.0000
4.5317
0.0000
60
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
88.6369
0.0006
3900.8838
0.0015
323.6317
0.0018
63
Nitrogen
5.0873
0.0000
142.5111
0.0001
12.1013
0.0001
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
69
Aspen Technology Inc. Licensed to: LEGENDS
0.1299 148503.7872
148600.5418
0.0000 0.9993
1.0000
3.6398 2.675310649e+06
2.679381713e+06
0.0000 0.9985
1.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.3118 183555.7671
183897.5147
0.0000 0.9981
1.0000
Page 105 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 36 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0251
0.0000
0.0438
0.0000
0.0254
16
H2O
0.0000
0.0062
0.0000
0.0069
0.0000
0.0032
17
Oxygen
0.0000
0.0574
0.0000
0.1144
0.0000
0.0465
18
Methane
0.0000
0.0323
0.0000
0.0323
0.0000
0.0499
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.5258
0.0000
0.0660
0.0000
0.4374
21
Ethane
0.0000
0.0140
0.0000
0.0262
0.0000
0.0340
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.1193
0.0000
0.3269
0.0000
0.1834
24
Nitrogen
0.0000
0.2199
0.0000
0.3836
0.0000
0.2202
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
35
H2O
36
Oxygen
0.6059
0.0000
19.3875
0.0000
1.1669
0.0000
37
Methane
0.0012
0.0000
0.0186
0.0000
0.0043
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
2.2934
0.0000
4.6235
0.0000
4.5317
0.0000
40
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
88.6369
0.0006
3900.8838
0.0015
323.6317
0.0018
43
Nitrogen
5.0873
0.0000
142.5111
0.0001
12.1013
0.0001
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.1299 148503.7872
148600.5418
0.0000 0.9993
1.0000
49
2.679381713e+06
0.0000
0.3118
0.9985
0.0000
183555.7671
1.0000
0.9981
183897.5147
1.0000
K VALUE
50 51
3.6398 2.675310649e+06
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
2.872e+004
---
53
H2O
6.157e-003
---
6.157e-003
54
Oxygen
1.408e+004
---
1.408e+004
55
Methane
4.136e+006
---
4.136e+006
56
H2S
57
---
---
2.872e+004
---
Hydrogen
3.407e+004
---
3.407e+004
58
Ethane
1.389e+008
---
1.389e+008
59
Propane
---
---
---
60
CO2
200.0
---
200.0
61
Nitrogen
6424
---
6424
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 106 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 36 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Pump:
P-100
Separator:
13
LOGICAL CONNECTION D-10
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
231.7 psia 1.486e+005 lbmole/hr Mass:
23
User Variables
24 25
NOTES
26 27
2.679e+006 lb/hrStd Ideal Liq Volume: 1.839e+005 barrel/day
29285
28 29 30
(Last modified Mon Dec 17, 2018, 16:57)
31 32
Description
33 34 35
Material Stream: 37
36 37 38
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
39 40
Overall
41
Vapour / Phase Fraction
42
Temperature:
43
Pressure:
44
Molar Flow
45
Mass Flow
46
Std Ideal Liq Vol Flow
(barrel/day)
47
Molar Enthalpy
(Btu/lbmole)
48
Molar Entropy
(Btu/lbmole-F)
49
Heat Flow
50
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
110.0*
110.0
(psia)
229.7*
229.7
(lbmole/hr) (lb/hr)
2349 3.772e+004 5579 -2.337e+004 31.08
2349 3.772e+004 5579 -2.337e+004 31.08
(Btu/hr)
-5.489e+007
-5.489e+007
(barrel/day)
* 3.801e+006
3.801e+006
51
PROPERTIES
52 53
Overall
Vapour Phase
54
Molecular Weight
55
Molar Density
56
Mass Density
57
Act. Volume Flow
58
Mass Enthalpy
(Btu/lb)
-1455
-1455
59
Mass Entropy
(Btu/lb-F)
1.935
1.935
60
Heat Capacity
61
Mass Heat Capacity
62
LHV Molar Basis (Std)
(Btu/lbmole)
7.748e+004
7.748e+004
63
HHV Molar Basis (Std)
(Btu/lbmole)
8.874e+004
8.874e+004
64
HHV Mass Basis (Std)
65
CO2 Loading
66
CO2 App ML Con
67
CO2 App WT Con
68
LHV Mass Basis (Std)
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
16.06 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.767e-002 0.6049 2.665e+005
16.06 3.767e-002 0.6049 2.665e+005
7.431
7.431
0.4627
0.4627
5525
5525
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
4824
4824
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 107 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 37 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Phase Fraction [Vol. Basis]
1.000
1.000
13
Phase Fraction [Mass Basis]
1.000
1.000
14
Phase Fraction [Act. Vol. Basis]
1.000
1.000
15
Mass Exergy
(Btu/lb)
182.6
---
16
Partial Pressure of CO2
(psia)
27.40
---
17
Cost Based on Flow
(Cost/s)
0.0000
0.0000
18
Act. Gas Flow
19
Avg. Liq. Density
20 21 22
Std. Ideal Liq. Mass Density
23
Act. Liq. Flow
24
Z Factor
25
Watson K
26
User Property
27
Partial Pressure of H2S
28
Cp/(Cp - R)
29
Cp/Cv
30
Heat of Vap.
31
Kinematic Viscosity
32
Liq. Mass Density (Std. Cond)
33
Liq. Vol. Flow (Std. Cond)
34
Liquid Fraction
35
Molar Volume
36
Mass Heat of Vap.
37
Phase Fraction [Molar Basis]
38
Surface Tension
39
Thermal Conductivity
40
Viscosity
41
Cv (Semi-Ideal)
42
Mass Cv (Semi-Ideal)
43
Cv
44
Mass Cv
45
Cv (Ent. Method)
46
Mass Cv (Ent. Method)
47
Cp/Cv (Ent. Method)
48
Reid VP at 37.8 C
49
True VP at 37.8 C
50
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
51
Viscosity Index
(ACFM)
1039
1039
(lbmole/ft3)
1.799
1.799
Specific Heat
(Btu/lbmole-F)
7.431
7.431
Std. Gas Flow
(MMSCFD)
21.35
21.35
(lb/ft3)
28.90
28.90
(USGPS)
---
---
0.9975
0.9975
10.51
10.51
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.365
1.365
1.390
1.390
5705
---
1.407
1.407
4.242e-002
4.242e-002
3.801e+006
3.801e+006
0.0000
0.0000
(ft3/lbmole)
26.55
26.55
(Btu/lb)
355.2
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
4.304e-002
4.304e-002
1.363e-002
1.363e-002
5.445
5.445
0.3391
0.3391
5.344
5.344
0.3328
0.3328
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.801e+006 -30.27
52
3.801e+006 ---
COMPOSITION
53 54
Overall Phase
55 56
COMPONENTS
57
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
58
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
59
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
60
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
61
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
62
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
64
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
65
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
67
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
68
Air
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 108 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 37 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
19
37720.7641
Vapour Phase
20 21
COMPONENTS
MOLAR FLOW (lbmole/hr)
22
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
23
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
24
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
25
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
26
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
27
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
29
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
30
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
32
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
33
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
37720.7641
38
K VALUE
39 40
COMPONENTS
MIXED
LIGHT
HEAVY
41
CO
---
---
---
42
H2O
---
---
---
43
Oxygen
---
---
---
44
Methane
---
---
---
---
---
---
45
H2S
46
Hydrogen
---
---
---
47
Ethane
---
---
---
48
Propane
---
---
---
49
CO2
---
---
---
50
Nitrogen
---
---
---
---
---
---
51
Air
52
Mercury
---
---
---
53
MEAmine
---
---
---
54
Ammonia
---
---
---
55
UNIT OPERATIONS
56 57 58
FEED TO Separator:
PRODUCT FROM
D-15 SEPARADOR DE CONDENSADO Cooler:
59
LOGICAL CONNECTION Cooler
UTILITIES
60 61
( No utilities reference this stream )
62
PROCESS UTILITY
63 64 65
DYNAMICS
66 67
Pressure Specification
(Active):
68
Flow Specification
(Inactive) Molar:
69
Aspen Technology Inc. Licensed to: LEGENDS
* 229.7 psia
2349 lbmole/hrMass:
3.772e+004 lb/hrStd Ideal Liq Volume:
Aspen HYSYS Version 8.8 (34.0.0.8909)
5579 barrel/day
Page 109 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 37 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
User Variables
10 11
NOTES
12 13 14
Description
15 16 17
Material Stream: 38
18 19 20
CONDITIONS
21 22
Overall
23
Vapour / Phase Fraction
24
Temperature:
25
Pressure:
26
Molar Flow
27
Mass Flow
28
Std Ideal Liq Vol Flow
(barrel/day)
29
Molar Enthalpy
(Btu/lbmole)
30
Molar Entropy
(Btu/lbmole-F)
31
Heat Flow
32
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
1.0000
1.0000
0.0000
(F)
110.0
110.0
110.0
(psia)
229.7
229.7
229.7
2349
2349
0.0000
(lbmole/hr) (lb/hr)
3.772e+004 5579 -2.337e+004 31.08
3.772e+004 5579 -2.337e+004 31.08
0.0000 0.0000 -1.225e+005 13.95
(Btu/hr)
-5.489e+007
-5.489e+007
0.0000
(barrel/day)
* 3.801e+006
3.801e+006
0.0000
33
PROPERTIES
34 35
Overall
Vapour Phase
Aqueous Phase
36
Molecular Weight
37
Molar Density
38
Mass Density
39
Act. Volume Flow
40
Mass Enthalpy
(Btu/lb)
-1455
-1455
-6791
41
Mass Entropy
(Btu/lb-F)
1.935
1.935
0.7735
42
Heat Capacity
7.431
7.431
18.57
43
Mass Heat Capacity
0.4627
0.4627
1.030
44
LHV Molar Basis (Std)
(Btu/lbmole)
7.748e+004
7.748e+004
45
HHV Molar Basis (Std)
(Btu/lbmole)
8.874e+004
8.874e+004
46
HHV Mass Basis (Std)
47
CO2 Loading
48
CO2 App ML Con
49
CO2 App WT Con
50
LHV Mass Basis (Std)
51 52 53
Phase Fraction [Act. Vol. Basis]
54
Mass Exergy
55
Partial Pressure of CO2
56
Cost Based on Flow
57
Act. Gas Flow
58
Avg. Liq. Density
59 60 61
Std. Ideal Liq. Mass Density
62
Act. Liq. Flow
63
Z Factor
64
Watson K
65
User Property
66
Partial Pressure of H2S
67
16.06 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.767e-002 0.6049 2.665e+005
16.06 3.767e-002 0.6049 2.665e+005
18.03 2.906 52.39 0.0000
1.851 1.762e+004
5525
5525
977.3
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
4824
4824
0.1027
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
182.6
---
---
(psia)
27.40
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1039
1039
---
(lbmole/ft3)
1.799
1.799
3.454
Specific Heat
(Btu/lbmole-F)
7.431
7.431
18.57
Std. Gas Flow
(MMSCFD)
21.35
21.35
0.0000
(lb/ft3)
28.90
28.90
62.28
(USGPS)
0.0000
---
0.0000
---
0.9975
10.51
10.51
8.465
---
---
---
0.0000
---
---
Cp/(Cp - R)
1.365
1.365
1.120
68
Cp/Cv
1.390
1.390
1.157
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
1.293e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 110 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 38 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Heat of Vap.
13
Kinematic Viscosity
14
Liq. Mass Density (Std. Cond)
15
Liq. Vol. Flow (Std. Cond)
16
Liquid Fraction
17
Molar Volume
18
Mass Heat of Vap.
19
Phase Fraction [Molar Basis]
20
Surface Tension
21
Thermal Conductivity
22
Viscosity
23
Cv (Semi-Ideal)
24
Mass Cv (Semi-Ideal)
25
Cv
26
Mass Cv
27
Cv (Ent. Method)
28
Mass Cv (Ent. Method)
29
Cp/Cv (Ent. Method)
30
Reid VP at 37.8 C
31
True VP at 37.8 C
32
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
33
Viscosity Index
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Aqueous Phase
5705
---
---
1.407
1.407
0.7294
4.242e-002
4.242e-002
63.37
3.801e+006
3.801e+006
0.0000
0.0000
0.0000
1.000
26.55
26.55
0.3442
355.2
---
---
1.0000
1.0000
0.0000
---
---
68.86
4.304e-002
4.304e-002
0.3672
1.363e-002
1.363e-002
0.6121
5.445
5.445
16.58
0.3391
0.3391
0.9196
5.344
5.344
16.05
0.3328
0.3328
0.8900
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
248.8
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
3.801e+006 -30.27
34
3.801e+006 ---
0.0000 ---
COMPOSITION
35 36
Overall Phase
37 38
COMPONENTS
39
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
40
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
41
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
42
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
43
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
44
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
46
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
47
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
49
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
50
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
55
37720.7641
Vapour Phase
56 57
COMPONENTS
58
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
59
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
60
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
61
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
62
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
63
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
65
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
66
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
68
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.2202
Page 111 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 38 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
20
37720.7641
Aqueous Phase
21 22
COMPONENTS
MOLAR FLOW (lbmole/hr)
23
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
24
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
H2O
0.0000
0.9993
0.0000
0.9985
0.0000
0.9981
26
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
CO2
0.0000
0.0006
0.0000
0.0015
0.0000
0.0018
33
Nitrogen
0.0000
0.0000
0.0000
0.0001
0.0000
0.0001
34
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
39
K VALUE
40 41
COMPONENTS
MIXED
LIGHT
HEAVY
42
CO
2.727e+004
---
43
H2O
6.157e-003
---
6.157e-003
44
Oxygen
1.333e+004
---
1.333e+004
45
Methane
3.988e+006
---
3.988e+006
46
H2S
47
---
2.727e+004
---
---
Hydrogen
3.150e+004
---
3.150e+004
48
Ethane
1.392e+008
---
1.392e+008
49
Propane
---
---
---
50
CO2
196.7
---
196.7
51
Nitrogen
6090
---
6090
---
---
---
52
Air
53
Mercury
---
---
---
54
MEAmine
---
---
---
55
Ammonia
---
---
---
56
UNIT OPERATIONS
57 58 59
FEED TO Recycle:
PRODUCT FROM RCY-4
60
Separator:
LOGICAL CONNECTION
D-15 SEPARADOR DE CONDENSADO
UTILITIES
61 62
( No utilities reference this stream )
63
PROCESS UTILITY
64 65 66
DYNAMICS
67 68
Pressure Specification
69
Aspen Technology Inc. Licensed to: LEGENDS
(Inactive):
229.7 psia
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 112 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 38 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
DYNAMICS
10 11
Fluid Package:
Flow Specification
(Inactive) Molar:
2349 lbmole/hrMass:
12
3.772e+004 lb/hrStd Ideal Liq Volume:
5579 barrel/day
User Variables
13 14
NOTES
15 16 17
Description
18 19 20
Material Stream: 39
21 22 23
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
24 25
Overall
26
Vapour / Phase Fraction
27
Temperature:
28
Pressure:
29
Molar Flow
30
Mass Flow
31
Std Ideal Liq Vol Flow
(barrel/day)
32
Molar Enthalpy
(Btu/lbmole)
33
Molar Entropy
(Btu/lbmole-F)
34
Heat Flow
35
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.0000
0.0000
1.0000
(F)
110.0
110.0
110.0
(psia)
229.7
229.7
229.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-1.225e+005
-2.337e+004
0.0000 -1.225e+005
13.95
31.08
13.95
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
36
PROPERTIES
37 38
Overall
39
Molecular Weight
40
Molar Density
41
Mass Density
42
Act. Volume Flow
43
Mass Enthalpy
44
Mass Entropy
45
Heat Capacity
46
Mass Heat Capacity
47
Vapour Phase 18.03
(lbmole/ft3) (lb/ft3)
2.906
16.06 3.767e-002
Aqueous Phase 18.03 2.906
52.39
0.6049
52.39
0.0000
0.0000
0.0000
(Btu/lb)
-6791
-1455
-6791
(Btu/lb-F)
0.7735
1.935
0.7735
(barrel/day)
(Btu/lbmole-F)
18.57
7.431
18.57
(Btu/lb-F)
1.030
0.4627
1.030
LHV Molar Basis (Std)
(Btu/lbmole)
1.851
48
HHV Molar Basis (Std)
(Btu/lbmole)
49
HHV Mass Basis (Std)
50
CO2 Loading
51
CO2 App ML Con
52
CO2 App WT Con
53
LHV Mass Basis (Std)
54
Phase Fraction [Vol. Basis]
55
Phase Fraction [Mass Basis]
56
Phase Fraction [Act. Vol. Basis]
57
Mass Exergy
58
Partial Pressure of CO2
59
Cost Based on Flow
60
Act. Gas Flow
61
Avg. Liq. Density
62
(Btu/lb)
1.762e+004
7.748e+004 8.874e+004
1.851 1.762e+004
977.3
5525
977.3
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
0.1027
4824
0.1027
---
---
1.000
0.0000
0.0000
1.000
---
---
---
(Btu/lb)
1.779
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
18.57
7.431
18.57
63
Std. Gas Flow
(MMSCFD)
0.0000
64
Std. Ideal Liq. Mass Density
65
Act. Liq. Flow
66
Z Factor
67
Watson K
68
User Property
69
Aspen Technology Inc. Licensed to: LEGENDS
0.0000
0.0000
(lb/ft3)
62.28
28.90
62.28
(USGPS)
0.0000
---
0.0000
---
0.9975
8.465
10.51
1.293e-002 8.465
---
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 113 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 39 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of H2S
13
Cp/(Cp - R)
14
Cp/Cv
15
Heat of Vap.
16
Kinematic Viscosity
17
Liq. Mass Density (Std. Cond)
18
Liq. Vol. Flow (Std. Cond)
19
Liquid Fraction
20
Molar Volume
21
Mass Heat of Vap.
22
Phase Fraction [Molar Basis]
23
Surface Tension
24
Thermal Conductivity
25
Viscosity
26
Cv (Semi-Ideal)
27
Mass Cv (Semi-Ideal)
28
Cv
29
Mass Cv
30
Cv (Ent. Method)
31
Mass Cv (Ent. Method)
32
Cp/Cv (Ent. Method)
33
Reid VP at 37.8 C
34
True VP at 37.8 C
35 36
(psia)
(Btu/lbmole) (cSt)
Vapour Phase ---
---
1.120
1.365
1.120
1.157
1.390
1.157
1.641e+004 0.7294
(lb/ft3)
Aqueous Phase
0.0000
63.37
---
---
1.407
0.7294
4.242e-002
63.37
(barrel/day)
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
0.3442
26.55
0.3442
(Btu/lb)
0.0000
910.1
---
---
0.0000
0.0000
1.0000
(dyne/cm)
68.86
(Btu/hr-ft-F)
0.3672
4.304e-002
0.3672
0.6121
1.363e-002
0.6121
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
68.86
16.58
5.445
16.58
0.9196
0.3391
0.9196
16.05
5.344
16.05
0.8900
0.3328
0.8900
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
248.8
---
248.8
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-4.382
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
37
COMPOSITION
38 39
Overall Phase
40 41
COMPONENTS
42
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
43
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
H2O
0.0000
0.9993
0.0000
0.9985
0.0000
0.9981
45
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
CO2
0.0000
0.0006
0.0000
0.0015
0.0000
0.0018
52
Nitrogen
0.0000
0.0000
0.0000
0.0001
0.0000
0.0001
53
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
58
Vapour Phase
59 60
COMPONENTS
61
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
62
CO
0.0000
0.0251
0.0000
0.0438
0.0000
0.0254
63
H2O
0.0000
0.0062
0.0000
0.0069
0.0000
0.0032
64
Oxygen
0.0000
0.0574
0.0000
0.1144
0.0000
0.0465
65
Methane
0.0000
0.0323
0.0000
0.0323
0.0000
0.0499
66
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Hydrogen
0.0000
0.5258
0.0000
0.0660
0.0000
0.4374
68
Ethane
0.0000
0.0140
0.0000
0.0262
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0340
Page 114 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 39 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
CO2
0.0000
0.1193
0.0000
0.3269
0.0000
0.1834
17
Nitrogen
0.0000
0.2199
0.0000
0.3836
0.0000
0.2202
18
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
23
Aqueous Phase
24 25
COMPONENTS
26
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
27
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
H2O
0.0000
0.9993
0.0000
0.9985
0.0000
0.9981
29
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
CO2
0.0000
0.0006
0.0000
0.0015
0.0000
0.0018
36
Nitrogen
0.0000
0.0000
0.0000
0.0001
0.0000
0.0001
37
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
42
K VALUE
43 44
COMPONENTS
MIXED
LIGHT
HEAVY
45
CO
2.727e+004
---
46
H2O
6.157e-003
---
6.157e-003
47
Oxygen
1.333e+004
---
1.333e+004
48
Methane
3.988e+006
---
3.988e+006
49
H2S
50
---
2.727e+004
---
---
Hydrogen
3.150e+004
---
3.150e+004
51
Ethane
1.392e+008
---
1.392e+008
52
Propane
---
---
---
53
CO2
196.7
---
196.7
54
Nitrogen
6090
---
6090
---
---
---
55
Air
56
Mercury
---
---
---
57
MEAmine
---
---
---
58
Ammonia
---
---
---
59
UNIT OPERATIONS
60 61
FEED TO
62
PRODUCT FROM Separator:
63
LOGICAL CONNECTION
D-15 SEPARADOR DE CONDENSADO
UTILITIES
64 65
( No utilities reference this stream )
66
PROCESS UTILITY
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 115 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 39 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
DYNAMICS
10 11
Pressure Specification
(Inactive):
12
Flow Specification
(Inactive) Molar:
229.7 psia 0.0000 lbmole/hrMass:
13
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
14 15
NOTES
16 17 18
Description
19 20 21
Material Stream: 40
22 23 24
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
25 26
Overall
27
Vapour / Phase Fraction
28
Temperature:
29
Pressure:
30
Molar Flow
31
Mass Flow
32
Std Ideal Liq Vol Flow
(barrel/day)
33
Molar Enthalpy
(Btu/lbmole)
34
Molar Entropy
(Btu/lbmole-F)
35
Heat Flow
36
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
111.8
111.8
(psia)
229.7
229.7
(lbmole/hr) (lb/hr)
2205 3.254e+004 5101 -1.658e+004 30.47
2205 3.254e+004 5101 -1.658e+004 30.47
(Btu/hr)
-3.657e+007
-3.657e+007
(barrel/day)
* 3.569e+006
3.569e+006
37
PROPERTIES
38 39
Overall
Vapour Phase
40
Molecular Weight
41
Molar Density
42
Mass Density
43
Act. Volume Flow
44
Mass Enthalpy
(Btu/lb)
-1124
-1124
45
Mass Entropy
(Btu/lb-F)
2.065
2.065
46
Heat Capacity
47
Mass Heat Capacity
48
LHV Molar Basis (Std)
(Btu/lbmole)
7.899e+004
7.899e+004
49
HHV Molar Basis (Std)
(Btu/lbmole)
9.052e+004
9.052e+004
50
HHV Mass Basis (Std)
51
CO2 Loading
52
CO2 App ML Con
53
CO2 App WT Con
54
LHV Mass Basis (Std)
55 56
14.76 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.746e-002 0.5528 2.516e+005
14.76 3.746e-002 0.5528 2.516e+005
7.300
7.300
0.4947
0.4947
6134
6134
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
5353
5353
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
57
Phase Fraction [Act. Vol. Basis]
1.000
1.000
58
Mass Exergy
(Btu/lb)
199.0
---
59
Partial Pressure of CO2
(psia)
19.12
---
60
Cost Based on Flow
(Cost/s)
0.0000
0.0000
61
Act. Gas Flow
62
Avg. Liq. Density
63
(ACFM)
981.0
981.0
(lbmole/ft3)
1.848
1.848
Specific Heat
(Btu/lbmole-F)
7.300
7.300
64
Std. Gas Flow
(MMSCFD)
20.04
20.04
65
Std. Ideal Liq. Mass Density
(lb/ft3)
27.27
27.27
66
Act. Liq. Flow
(USGPS)
---
---
67
Z Factor
0.9998
0.9998
68
Watson K
10.71
10.71
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 116 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 40 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
User Property
13
Partial Pressure of H2S
14
Cp/(Cp - R)
15
Cp/Cv
16
Heat of Vap.
17
Kinematic Viscosity
18
Liq. Mass Density (Std. Cond)
19
Liq. Vol. Flow (Std. Cond)
20
Liquid Fraction
21
Molar Volume
22
Mass Heat of Vap.
23
Phase Fraction [Molar Basis]
24
Surface Tension
25
Thermal Conductivity
26
Viscosity
27
Cv (Semi-Ideal)
28
Mass Cv (Semi-Ideal)
29
Cv
30
Mass Cv
31
Cv (Ent. Method)
32
Mass Cv (Ent. Method)
33
Cp/Cv (Ent. Method)
34
Reid VP at 37.8 C
35
True VP at 37.8 C
36
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
37
Viscosity Index
Vapour Phase ---
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
0.0000
---
1.374
1.374
1.395
1.395
5610
---
1.500
1.500
3.897e-002
3.897e-002
3.569e+006
3.569e+006
0.0000
0.0000
(ft3/lbmole)
26.69
26.69
(Btu/lb)
380.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
4.605e-002
4.605e-002
1.329e-002
1.329e-002
5.314
5.314
0.3601
0.3601
5.232
5.232
0.3546
0.3546
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.569e+006 -28.38
38
3.569e+006 ---
COMPOSITION
39 40
Overall Phase
41 42
COMPONENTS
43
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
44
CO
58.2972
0.0264
1632.9560
0.0502
139.8734
0.0274
45
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Oxygen
130.6356
0.0592
4180.3394
0.1285
251.5994
0.0493
47
Methane
72.2034
0.0327
1158.3525
0.0356
264.9207
0.0519
48
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Hydrogen
1226.5292
0.5562
2472.6829
0.0760
2423.6154
0.4752
50
Ethane
23.3595
0.0106
702.4180
0.0216
135.2231
0.0265
51
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
CO2
183.5713
0.0832
8078.9173
0.2483
670.2567
0.1314
53
Nitrogen
510.1373
0.2313
14290.4765
0.4391
1213.4684
0.2379
54
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
MEAmine
0.4159
0.0002
25.4075
0.0008
1.7107
0.0003
57
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Total
2205.1494
1.0000
1.0000
5100.6678
1.0000
59
32541.5499
Vapour Phase
60 61
COMPONENTS
62
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
63
CO
58.2972
0.0264
1632.9560
0.0502
139.8734
0.0274
64
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Oxygen
130.6356
0.0592
4180.3394
0.1285
251.5994
0.0493
66
Methane
72.2034
0.0327
1158.3525
0.0356
264.9207
0.0519
67
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Hydrogen
1226.5292
0.5562
2472.6829
0.0760
2423.6154
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.4752
Page 117 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 40 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14 15
Ethane
16
Propane
17
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
23.3595
0.0106
702.4180
0.0216
135.2231
0.0265
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
CO2
183.5713
0.0832
8078.9173
0.2483
670.2567
0.1314
18
Nitrogen
510.1373
0.2313
14290.4765
0.4391
1213.4684
0.2379
19
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
MEAmine
0.4159
0.0002
25.4075
0.0008
1.7107
0.0003
22
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Total
2205.1494
1.0000
1.0000
5100.6678
1.0000
32541.5499
24
K VALUE
25 26
COMPONENTS
MIXED
LIGHT
HEAVY
27
CO
---
---
---
28
H2O
---
---
---
29
Oxygen
---
---
---
30
Methane
---
---
---
---
---
---
31
H2S
32
Hydrogen
---
---
---
33
Ethane
---
---
---
34
Propane
---
---
---
35
CO2
---
---
---
36
Nitrogen
---
---
---
---
---
---
37
Air
38
Mercury
---
---
---
39
MEAmine
---
---
---
40
Ammonia
---
---
---
41
UNIT OPERATIONS
42 43 44
FEED TO
PRODUCT FROM
Component Splitter:
X-100
45
Absorber:
LOGICAL CONNECTION T-100
UTILITIES
46 47
( No utilities reference this stream )
48
PROCESS UTILITY
49 50 51
DYNAMICS
52 53
Pressure Specification
(Inactive):
54
Flow Specification
(Inactive) Molar:
55
229.7 psia 2205 lbmole/hrMass:
3.254e+004 lb/hrStd Ideal Liq Volume:
5101 barrel/day
User Variables
56 57
NOTES
58 59 60
Description
61 62 63 64 65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 118 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 41
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
134.1
134.1
(psia)
228.7*
228.7
223.2
223.2
(lbmole/hr) (lb/hr) (barrel/day)
8896
8896
742.4
742.4
-1.373e+005 36.71
-1.373e+005 36.71
(Btu/hr)
-3.066e+007
-3.066e+007
(barrel/day)
* 3.598e+005
3.598e+005
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-3446
-3446
30
Mass Entropy
(Btu/lb-F)
0.9212
0.9212
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
3.162e+004
3.162e+004
34
HHV Molar Basis (Std)
(Btu/lbmole)
3.162e+004
3.162e+004
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41
39.85 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.751e-002 1.495 2.544e+004
39.85 3.751e-002 1.495 2.544e+004
9.315
9.315
0.2337
0.2337
793.3
793.3
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
793.3
793.3
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
(Btu/lb)
72.54
---
44
Partial Pressure of CO2
(psia)
169.3
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48
(ACFM)
99.19
99.19
(lbmole/ft3)
1.285
1.285
Specific Heat
(Btu/lbmole-F)
9.315
9.315
49
Std. Gas Flow
(MMSCFD)
2.029
2.029
50
Std. Ideal Liq. Mass Density
(lb/ft3)
51.22
51.22
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
0.9569
0.9569
53
Watson K
8.145
8.145
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.271
1.271
1.359
1.359
8471
---
0.7497
0.7497
0.1057 3.598e+005
0.1057 3.598e+005
0.0000
0.0000
(ft3/lbmole)
26.66
26.66
(Btu/lb)
212.6
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
1.295e-002
1.295e-002
1.795e-002
1.795e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 119 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 41 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 7.329
7.329
0.1839
0.1839
6.855
6.855
0.1720
0.1720
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.598e+005
3.598e+005
-44.10
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
29
CO
58.0057
0.2599
1624.7912
0.1826
139.1740
0.1875
30
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
165.2142
0.7401
7271.0256
0.8174
603.2310
0.8125
38
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
223.2198
1.0000
8895.8168
1.0000
742.4051
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
48
CO
58.0057
0.2599
1624.7912
0.1826
139.1740
0.1875
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
165.2142
0.7401
7271.0256
0.8174
603.2310
0.8125
57
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
223.2198
1.0000
8895.8168
1.0000
742.4051
1.0000
63
K VALUE
64 65
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 120 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 41 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Mixer:
MIX-101 Component Splitter:
27
LOGICAL CONNECTION X-100
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Inactive) Molar:
* 228.7 psia
223.2 lbmole/hrMass:
37
8896 lb/hr Std Ideal Liq Volume:
742.4 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 42
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
Vapour Phase
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
2.117e+004
57
Molar Enthalpy
(Btu/lbmole)
-1.143e+005
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Liquid Phase
0.0167
0.0167
0.9833
(F)
116.8
116.8
116.8
(psia)
228.7
228.7
228.7
5218
87.07
(lbmole/hr) (lb/hr)
3.104e+005
6.450
2665 243.1 -7.565e+004 35.79
5131 3.077e+005 2.093e+004 -1.149e+005 5.952
(Btu/hr)
-5.964e+008
-6.586e+006
-5.898e+008
(barrel/day)
* 2.102e+004
1.407e+005
2.074e+004
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 59.49
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
0.7091 42.18 3.145e+004 -1921
30.60 3.761e-002 1.151 9896 -2472
Liquid Phase 59.98 1.017 61.02 2.156e+004 -1916
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 121 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 42 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
5.477e+005
8.452e+004
5.555e+005
16
HHV Molar Basis (Std)
(Btu/lbmole)
6.052e+005
8.728e+004
6.140e+005
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
Phase Fraction [Vol. Basis]
1.148e-002
1.148e-002
0.9885
23
Phase Fraction [Mass Basis]
8.584e-003
8.584e-003
0.9914
24
Phase Fraction [Act. Vol. Basis]
25
Mass Exergy
26
Partial Pressure of CO2
27
Cost Based on Flow
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.1084
1.170
41.50
8.070
42.07
0.6976
0.2637
0.7014
1.017e+004
9.923e-002
2852
1.024e+004
---
---
4.862e-002
(lbmole/ft3)
---
---
4.676e-002
(lbmol/lb)
---
---
7.663e-004
(Btu/lb)
9206
2762
9262
0.3146
0.3146
0.6854
(Btu/lb)
3.691
---
---
(psia)
68.33
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
38.59
38.59
---
(lbmole/ft3)
1.053
1.531
1.048
Specific Heat
(Btu/lbmole-F)
41.50
8.070
42.07
Std. Gas Flow
(MMSCFD)
47.43
0.7914
46.64
(lb/ft3)
62.67
46.86
62.85
(USGPS)
10.48
---
---
0.9830
9.085
7.836
9.096
---
---
---
0.0000
---
---
1.050
1.326
1.050
1.003
1.383
2.745
(psia)
(Btu/lbmole) (cSt)
5.317e+004 ---
(lb/ft3)
63.12
(barrel/day) (ft3/lbmole) (Btu/lb)
2.102e+004
10.48 3.634e-002
---
---
0.9974
8.933
8.094e-002 1.407e+005
63.43 2.074e+004
0.9833
0.0000
1.000
1.410
26.59
0.9829
893.8
---
---
0.0167
0.0167
0.9833
(dyne/cm)
43.51
(Btu/hr-ft-F)
---
1.751e-002
0.1022
---
1.839e-002
8.732
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
43.51
39.52
6.084
40.08
0.6643
0.1988
0.6683
41.38
5.834
15.33
0.6956
0.1906
0.2555
---
---
18.71
(Btu/lb-F)
---
---
0.3119
---
---
2.249
Reid VP at 37.8 C
(psia)
60.63
---
39.43
59
True VP at 37.8 C
(psia)
782.2
---
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
1.615e+005 22.64
62
1.407e+005 ---
225.9 2.074e+004 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 58.6847
MOLE FRACTION 0.0112
MASS FLOW (lb/hr) 1643.8102
Vapour Fraction MASS FRACTION 0.0053
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 140.8031
0.0167
LIQUID VOLUME FRACTION 0.0066
Page 122 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 42 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0167
LIQUID VOLUME FRACTION
15
H2O
14.4510
0.0028
260.3363
0.0008
17.8619
0.0008
16
Oxygen
4.1931
0.0008
134.1791
0.0004
8.0757
0.0004
17
Methane
3.6632
0.0007
58.7686
0.0002
13.4407
0.0006
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
8.4386
0.0016
17.0122
0.0001
16.6746
0.0008
20
Ethane
9.4564
0.0018
284.3530
0.0009
54.7410
0.0026
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
261.8536
0.0502
11524.0976
0.0371
956.0815
0.0452
23
Nitrogen
6.3500
0.0012
177.8814
0.0006
15.1047
0.0007
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
4850.9181
0.9296
27
Ammonia
0.0000
0.0000
28
Total
5218.0085
1.0000
29
296312.9955 0.0000 310413.4339
0.9546 0.0000 1.0000
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
19950.8243 0.0000 21173.6077 Phase Fraction
MASS FRACTION
0.9422 0.0000 1.0000 1.669e-002
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
33
CO
44.3154
0.5090
1241.3140
0.4659
106.3267
0.4374
34
H2O
0.0130
0.0001
0.2344
0.0001
0.0161
0.0001
35
Oxygen
2.2520
0.0259
72.0642
0.0270
4.3373
0.0178
36
Methane
1.5760
0.0181
25.2828
0.0095
5.7823
0.0238
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
7.0584
0.0811
14.2298
0.0053
13.9474
0.0574
39
Ethane
1.1015
0.0127
33.1231
0.0124
6.3766
0.0262
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
26.0140
0.2988
1144.8694
0.4297
94.9826
0.3908
42
Nitrogen
4.7155
0.0542
132.0943
0.0496
11.2167
0.0461
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0222
0.0003
1.3572
0.0005
0.0914
0.0004
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
87.0680
1.0000
2664.5692
1.0000
243.0770
1.0000
48
Liquid Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9833 LIQUID VOLUME FRACTION
52
CO
14.3693
0.0028
402.4962
0.0013
34.4764
0.0016
53
H2O
14.4380
0.0028
260.1019
0.0008
17.8459
0.0009
54
Oxygen
1.9411
0.0004
62.1148
0.0002
3.7385
0.0002
55
Methane
2.0873
0.0004
33.4858
0.0001
7.6584
0.0004
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
1.3802
0.0003
2.7824
0.0000
2.7272
0.0001
58
Ethane
8.3549
0.0016
251.2299
0.0008
48.3645
0.0023
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
235.8396
0.0460
10379.2282
0.0337
861.0990
0.0411
61
Nitrogen
1.6345
0.0003
45.7871
0.0001
3.8880
0.0002
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
4850.8958
0.9454
65
Ammonia
0.0000
0.0000
66
Total
5130.9405
1.0000
296311.6383 0.0000 307748.8647
0.9628 0.0000 1.0000
19950.7329 0.0000 20930.5307
0.9532 0.0000 1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 123 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 42 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
13
H2O
14
Oxygen
68.37
68.37
---
15
Methane
44.49
44.49
---
---
---
---
16
181.7
181.7
5.311e-002
H2S
---
5.311e-002
---
17
Hydrogen
301.4
301.4
---
18
Ethane
7.770
7.770
---
19
Propane
---
---
---
20
CO2
6.500
6.500
---
21
Nitrogen
170.0
170.0
---
---
---
---
---
---
---
22
Air
23
Mercury
24
MEAmine
25
Ammonia
2.699e-004 ---
26
---
---
---
UNIT OPERATIONS
27 28 29
2.699e-004
FEED TO
PRODUCT FROM
Heater:
E-108
Mixer:
LOGICAL CONNECTION MIX-101
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
228.7 psia 5218 lbmole/hrMass:
40
3.104e+005 lb/hrStd Ideal Liq Volume: 2.117e+004 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 43
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
2.117e+004
60
Molar Enthalpy
(Btu/lbmole)
-1.107e+005
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Liquid Phase
0.0227
0.0227
0.9773
(F)
200.0*
200.0
200.0
(psia)
225.7
225.7
225.7
5218
118.6
(lbmole/hr) (lb/hr)
3.104e+005
12.21
4012 357.8 -9.611e+004 37.69
5099 3.064e+005 2.082e+004 -1.111e+005 11.62
(Btu/hr)
-5.778e+008
-1.140e+007
-5.664e+008
(barrel/day)
* 2.102e+004
1.915e+005
2.065e+004
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 59.49
(lbmole/ft3)
0.5799
33.82 3.240e-002
Liquid Phase 60.09 0.9555
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 124 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 43 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-1861
-2842
-1849
15
Mass Entropy
(Btu/lb-F)
0.2053
1.114
0.1934
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
5.477e+005
7.104e+004
5.588e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
6.052e+005
7.378e+004
6.176e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
Phase Fraction [Vol. Basis]
1.690e-002
1.690e-002
0.9831
26
Phase Fraction [Mass Basis]
1.293e-002
1.293e-002
0.9871
27
Phase Fraction [Act. Vol. Basis]
28
Mass Exergy
29
Partial Pressure of CO2
30
Cost Based on Flow
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
34.50 3.846e+004
1.096 1.565e+004
57.41 2.281e+004
43.47
8.715
44.28
0.7308
0.2577
0.7369
1.017e+004
2181
1.028e+004
---
---
4.284e-002
(lbmole/ft3)
---
---
3.893e-002
(lbmol/lb)
---
---
6.781e-004
(Btu/lb)
9206
2100
9299
0.4069
0.4069
0.5931
(Btu/lb)
11.50
---
---
(psia)
102.9
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
61.02
61.02
---
(lbmole/ft3)
1.053
1.417
1.047
Specific Heat
(Btu/lbmole-F)
43.47
8.715
44.28
Std. Gas Flow
(MMSCFD)
47.43
1.078
46.35
(lb/ft3)
62.67
47.94
62.92
(USGPS)
11.09
---
---
0.9840
9.085
8.109
9.097
---
---
---
0.0000
---
---
1.048
1.295
1.047
1.003
1.342
2.837
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
5.347e+004 --63.12 2.102e+004
11.09 3.337e-002
---
---
1.159
4.057
8.955e-002 1.915e+005
63.43 2.065e+004
0.9773
0.0000
1.000
(ft3/lbmole)
1.725
30.86
1.047
(Btu/lb)
898.8
---
---
0.0227
0.0227
0.9773
(dyne/cm)
35.78
(Btu/hr-ft-F)
---
1.798e-002
---
2.035e-002
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
35.78 9.423e-002 3.731
41.49
6.729
42.29
0.6974
0.1990
0.7039
43.33
6.492
15.61
0.7283
0.1919
0.2597
---
---
15.85
(Btu/lb-F)
---
---
0.2638
---
---
2.794
Reid VP at 37.8 C
(psia)
60.63
---
35.00
62
True VP at 37.8 C
(psia)
782.2
---
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
2.122e+005 17.04
1.915e+005 ---
206.0 2.065e+004 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 125 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 43 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
0.0227
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
CO
58.6847
0.0112
1643.8102
0.0053
140.8031
0.0066
16
H2O
14.4510
0.0028
260.3363
0.0008
17.8619
0.0008
17
Oxygen
4.1931
0.0008
134.1791
0.0004
8.0757
0.0004
18
Methane
3.6632
0.0007
58.7686
0.0002
13.4407
0.0006
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
8.4386
0.0016
17.0122
0.0001
16.6746
0.0008
21
Ethane
9.4564
0.0018
284.3530
0.0009
54.7410
0.0026
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
261.8536
0.0502
11524.0976
0.0371
956.0815
0.0452
24
Nitrogen
6.3500
0.0012
177.8814
0.0006
15.1047
0.0007
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
4850.9181
0.9296
28
Ammonia
0.0000
0.0000
29
Total
5218.0085
1.0000
30
296312.9955 0.0000 310413.4339
0.9546 0.0000 1.0000
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
19950.8243 0.0000 21173.6077 Phase Fraction
MASS FRACTION
0.9422 0.0000 1.0000 2.273e-002
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
34
CO
45.7020
0.3853
1280.1549
0.3190
109.6537
0.3065
35
H2O
0.0818
0.0007
1.4731
0.0004
0.1011
0.0003
36
Oxygen
2.5625
0.0216
81.9996
0.0204
4.9353
0.0138
37
Methane
1.8937
0.0160
30.3812
0.0076
6.9483
0.0194
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
7.0207
0.0592
14.1538
0.0035
13.8729
0.0388
40
Ethane
1.9461
0.0164
58.5198
0.0146
11.2657
0.0315
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
54.0742
0.4558
2379.7885
0.5931
197.4360
0.5518
43
Nitrogen
4.8547
0.0409
135.9935
0.0339
11.5478
0.0323
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.4905
0.0041
29.9613
0.0075
2.0173
0.0056
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
118.6262
1.0000
4012.4257
1.0000
357.7781
1.0000
49
Liquid Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9773 LIQUID VOLUME FRACTION
53
CO
12.9826
0.0025
363.6553
0.0012
31.1495
0.0015
54
H2O
14.3692
0.0028
258.8633
0.0008
17.7609
0.0009
55
Oxygen
1.6306
0.0003
52.1794
0.0002
3.1405
0.0002
56
Methane
1.7695
0.0003
28.3874
0.0001
6.4923
0.0003
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
1.4178
0.0003
2.8584
0.0000
2.8017
0.0001
59
Ethane
7.5103
0.0015
225.8333
0.0007
43.4753
0.0021
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
207.7794
0.0407
9144.3091
0.0298
758.6455
0.0364
62
Nitrogen
1.4953
0.0003
41.8879
0.0001
3.5569
0.0002
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
4850.4276
0.9512
66
Ammonia
0.0000
0.0000
67
Total
5099.3823
1.0000
296283.0342 0.0000 306401.0082
0.9670 0.0000 1.0000
19948.8070 0.0000 20815.8296
0.9583 0.0000 1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 126 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 43 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
151.3
151.3
---
13
H2O
0.2446
0.2446
---
14
Oxygen
67.55
67.55
---
15
Methane
46.01
46.01
---
---
---
---
16
H2S
17
Hydrogen
212.9
212.9
---
18
Ethane
11.14
11.14
---
19
Propane
---
---
---
20
CO2
11.19
11.19
---
21
Nitrogen
139.6
139.6
---
---
---
---
---
---
---
22
Air
23
Mercury
24
MEAmine
25
Ammonia
4.347e-003 ---
26
---
---
---
UNIT OPERATIONS
27 28 29
4.347e-003
FEED TO
PRODUCT FROM
Distillation:
T-102
Heater:
LOGICAL CONNECTION E-108
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
225.7 psia 5218 lbmole/hrMass:
40
3.104e+005 lb/hrStd Ideal Liq Volume: 2.117e+004 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 44
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
60 61 62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
1.0000
1.0000
0.0000
(F)
110.0*
110.0
110.0
(psia)
228.7*
228.7
1982
1982
(lbmole/hr) (lb/hr)
2.365e+004
2.364e+004
(barrel/day)
4358
4358
Molar Enthalpy
(Btu/lbmole)
-2980
-2976
Molar Entropy
(Btu/lbmole-F)
29.12
29.12
228.7 7.459e-002 4.534 0.3063 -1.122e+005 4.192
(Btu/hr)
-5.907e+006
-5.898e+006
-8373
(barrel/day)
* 3.209e+006
3.209e+006
0.3061
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 11.93
(lbmole/ft3)
3.732e-002
11.93 3.732e-002
Liquid Phase 60.78 1.008
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 127 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 44 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-249.8
-249.5
15
Mass Entropy
(Btu/lb-F)
2.441
2.441
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
8.432e+004
8.430e+004
5.826e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
9.715e+004
9.713e+004
6.440e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.4453 2.270e+005
0.4452 2.270e+005
61.24 0.3165 -1847 6.898e-002
7.106
7.105
43.03
0.5956
0.5956
0.7080
8143
8143
1.060e+004
---
---
1.548e-003
(lbmole/ft3)
---
---
1.547e-003
(lbmol/lb)
---
---
2.526e-005
(Btu/lb)
7068
7067
Phase Fraction [Vol. Basis]
0.9999
0.9999
7.027e-005
26
Phase Fraction [Mass Basis]
0.9998
0.9998
1.917e-004
27
Phase Fraction [Act. Vol. Basis]
1.000
1.000
1.394e-006
28
Mass Exergy
(Btu/lb)
245.9
---
29
Partial Pressure of CO2
(psia)
2.118
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
9586
---
(ACFM)
885.0
885.0
---
(lbmole/ft3)
1.944
1.944
1.041
Specific Heat
(Btu/lbmole-F)
7.106
7.105
Std. Gas Flow
(MMSCFD)
18.02
18.02
23.19
23.19
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
1.538e-004
(Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
63.28
---
1.538e-004 3.713e-002
---
1.002
11.65
11.66
9.113
---
---
---
0.0000
---
---
1.388
1.388
1.048
1.404
1.404
2.900
5000
---
---
---
1.730
10.75
3.150e-002
3.149e-002
63.31
3.209e+006
3.209e+006
0.3061
3.764e-005 (ft3/lbmole)
43.03 6.780e-004
26.79
0.0000
1.000
26.79
0.9925
419.1
---
---
1.0000
1.0000
0.0000
---
---
46.13
5.261e-002
5.261e-002
0.1082
1.234e-002
1.234e-002
10.55
5.120
5.119
41.05
0.4292
0.4291
0.6753
5.060
5.059
14.84
0.4242
0.4241
0.2441
---
---
18.84
---
---
0.3099
---
---
2.284
---
---
9.733
---
---
3.209e+006 -23.63
3.209e+006 ---
236.7 0.3061 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 128 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 44 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
CO
0.2915
0.0001
8.1648
0.0003
0.6994
0.0002
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
130.6356
0.0659
4180.3394
0.1768
251.5994
0.0577
18
Methane
72.2034
0.0364
1158.3525
0.0490
264.9207
0.0608
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1226.5292
0.6189
2472.6829
0.1046
2423.6154
0.5561
21
Ethane
23.3595
0.0118
702.4180
0.0297
135.2231
0.0310
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
18.3571
0.0093
807.8917
0.0342
67.0257
0.0154
24
Nitrogen
510.1373
0.2574
14290.4765
0.6044
1213.4684
0.2784
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1981.9296
1.0000
1.0000
4358.2627
1.0000
30
23645.7332
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.2915
0.0001
8.1648
0.0003
0.6994
0.0002
35
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Oxygen
130.6355
0.0659
4180.3371
0.1768
251.5993
0.0577
37
Methane
72.2034
0.0364
1158.3515
0.0490
264.9205
0.0608
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1226.5290
0.6189
2472.6826
0.1046
2423.6151
0.5561
40
Ethane
23.3594
0.0118
702.4143
0.0297
135.2224
0.0310
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
18.3570
0.0093
807.8867
0.0342
67.0253
0.0154
43
Nitrogen
510.1372
0.2574
14290.4734
0.6045
1213.4681
0.2784
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.3420
0.0002
20.8891
0.0009
1.4065
0.0003
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
1981.8550
1.0000
1.0000
4357.9564
1.0000
49
23641.1995
Liquid Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
3.764e-005 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Oxygen
0.0001
0.0010
0.0023
0.0005
0.0001
0.0004
56
Methane
0.0001
0.0008
0.0010
0.0002
0.0002
0.0007
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0001
0.0019
0.0003
0.0001
0.0003
0.0009
59
Ethane
0.0001
0.0016
0.0037
0.0008
0.0007
0.0023
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0001
0.0015
0.0050
0.0011
0.0004
0.0014
62
Nitrogen
0.0001
0.0014
0.0030
0.0007
0.0003
0.0008
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0740
0.9917
4.5184
0.9966
0.3042
0.9934
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0746
1.0000
4.5337
1.0000
0.3063
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 129 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 44 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
13
H2O
14
Oxygen
69.17
69.17
---
15
Methane
44.20
44.20
---
---
---
---
16
189.3
189.3
4.265e-002
H2S
---
4.265e-002
---
17
Hydrogen
322.1
322.1
---
18
Ethane
7.222
7.222
---
19
Propane
---
---
---
20
CO2
6.032
6.032
---
21
Nitrogen
177.6
177.6
---
---
---
---
---
---
---
22
Air
23
Mercury
24
MEAmine
25
Ammonia
1.740e-004 ---
26
---
---
---
UNIT OPERATIONS
27 28 29
1.740e-004
FEED TO
PRODUCT FROM
LNG:
LNG-100 Component Splitter:
30
LOGICAL CONNECTION X-100
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 228.7 psia
1982 lbmole/hrMass:
40
2.365e+004 lb/hrStd Ideal Liq Volume:
4358 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 45
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
4358
4358
60
Molar Enthalpy
(Btu/lbmole)
486.0
486.0
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
585.0*
585.0
(psia)
228.7
228.7
(lbmole/hr) (lb/hr)
1982 2.365e+004
33.53
1982 2.365e+004
33.53
(Btu/hr)
9.633e+005
9.633e+005
(barrel/day)
* 3.209e+006
3.209e+006
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 11.93
(lbmole/ft3)
2.031e-002
11.93 2.031e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 130 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 45 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
40.74
40.74
15
Mass Entropy
(Btu/lb-F)
2.811
2.811
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
8.432e+004
8.432e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
9.715e+004
9.715e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.2423 4.172e+005
0.2423 4.172e+005
7.511
7.511
0.6296
0.6296
8143
8143
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7068
7068
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
27
Phase Fraction [Act. Vol. Basis]
1.000
1.000
28
Mass Exergy
(Btu/lb)
337.9
---
29
Partial Pressure of CO2
(psia)
2.118
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
(ACFM)
1627
1627
(lbmole/ft3)
1.944
1.944
Specific Heat
(Btu/lbmole-F)
7.511
7.511
Std. Gas Flow
(MMSCFD)
18.02
18.02
(lb/ft3)
23.19
23.19
(USGPS)
---
---
Z Factor
1.005
1.005
38
Watson K
11.65
11.65
39
User Property
---
---
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.359
1.359
1.363
1.363
5000
---
5.288
5.288
3.150e-002
3.150e-002
3.209e+006
3.209e+006
0.0000
0.0000
(ft3/lbmole)
49.24
49.24
(Btu/lb)
419.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
8.346e-002
8.346e-002
2.052e-002
2.052e-002
5.525
5.525
0.4631
0.4631
5.513
5.513
0.4621
0.4621
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.209e+006 -7.696
3.209e+006 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 131 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 45 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
CO
0.2915
0.0001
8.1648
0.0003
0.6994
0.0002
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
130.6356
0.0659
4180.3394
0.1768
251.5994
0.0577
18
Methane
72.2034
0.0364
1158.3525
0.0490
264.9207
0.0608
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1226.5292
0.6189
2472.6829
0.1046
2423.6154
0.5561
21
Ethane
23.3595
0.0118
702.4180
0.0297
135.2231
0.0310
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
18.3571
0.0093
807.8917
0.0342
67.0257
0.0154
24
Nitrogen
510.1373
0.2574
14290.4765
0.6044
1213.4684
0.2784
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1981.9296
1.0000
1.0000
4358.2627
1.0000
30
23645.7332
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.2915
0.0001
8.1648
0.0003
0.6994
0.0002
35
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Oxygen
130.6356
0.0659
4180.3394
0.1768
251.5994
0.0577
37
Methane
72.2034
0.0364
1158.3525
0.0490
264.9207
0.0608
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1226.5292
0.6189
2472.6829
0.1046
2423.6154
0.5561
40
Ethane
23.3595
0.0118
702.4180
0.0297
135.2231
0.0310
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
18.3571
0.0093
807.8917
0.0342
67.0257
0.0154
43
Nitrogen
510.1373
0.2574
14290.4765
0.6044
1213.4684
0.2784
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
1981.9296
1.0000
1.0000
4358.2627
1.0000
49
K VALUE
50 51
23645.7332
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 132 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 45 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Conversion Reactor:
D-1 METANADOR LNG:
LOGICAL CONNECTION LNG-100
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
228.7 psia 1982 lbmole/hrMass:
23
2.365e+004 lb/hrStd Ideal Liq Volume:
4358 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 46
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
44
Molar Entropy
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
618.7
618.7
618.7
(psia)
225.7
225.7
225.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(Btu/lbmole)
489.3
489.2
489.3
(Btu/lbmole-F)
33.98
33.98
33.98
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
47
PROPERTIES
48 49
Overall
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Vapour Phase 12.01
(lbmole/ft3)
1.942e-002
Liquid Phase 12.01 1.942e-002
0.2332
0.2332
0.2332
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
40.74
40.74
40.74
55
Mass Entropy
(Btu/lb-F)
2.830
2.830
2.830
56
Heat Capacity
7.564
7.564
7.564
57
Mass Heat Capacity
0.6298
0.6298
0.6298
58
LHV Molar Basis (Std)
(Btu/lbmole)
8.465e+004
8.465e+004
8.465e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
9.756e+004
9.756e+004
9.756e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
Phase Fraction [Vol. Basis]
66
Phase Fraction [Mass Basis]
67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
1.942e-002
12.01
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
8124
8124
8124
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
7048
7048
7048
(Btu/lb)
---
---
1.000
0.0000
0.0000
1.000
---
---
---
345.1
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 133 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 46 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Vapour Phase
Liquid Phase
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
7.564
7.564
7.564
17
Std. Gas Flow
(MMSCFD)
0.0000
18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46 47
0.0000
0.0000
(lb/ft3)
23.38
23.38
23.38
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
---
1.004
1.004
11.64
11.64
11.64
---
---
---
0.0000
---
---
1.356
1.356
1.356
1.359
1.359
1.359
5168
---
---
0.5358
5.628
0.5358
3.171e-002
(barrel/day)
3.171e-002
3.171e-002
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
51.50
51.50
51.50
(Btu/lb)
430.3
---
---
0.0000
0.0000
1.0000
(dyne/cm)
5.591e-002
(Btu/hr-ft-F)
4.133e-002
8.439e-002
4.133e-002
2.001e-003
2.103e-002
2.001e-003
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
5.591e-002
5.578
5.578
5.578
0.4645
0.4645
0.4645
5.566
5.566
5.566
0.4634
0.4634
0.4634
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-7.043
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
55
H2O
0.0000
0.0066
0.0000
0.0099
0.0000
0.0037
56
Oxygen
0.0000
0.0663
0.0000
0.1768
0.0000
0.0582
57
Methane
0.0000
0.0400
0.0000
0.0534
0.0000
0.0668
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0000
0.6098
0.0000
0.1024
0.0000
0.5487
60
Ethane
0.0000
0.0119
0.0000
0.0297
0.0000
0.0313
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0000
0.0061
0.0000
0.0222
0.0000
0.0101
63
Nitrogen
0.0000
0.2591
0.0000
0.6044
0.0000
0.2807
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0002
0.0000
0.0011
0.0000
0.0004
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
0.0000
1.0000
0.0000
1.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 134 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 46 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
16
H2O
0.0000
0.0066
0.0000
0.0099
0.0000
0.0037
17
Oxygen
0.0000
0.0664
0.0000
0.1768
0.0000
0.0582
18
Methane
0.0000
0.0400
0.0000
0.0534
0.0000
0.0668
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.6098
0.0000
0.1024
0.0000
0.5487
21
Ethane
0.0000
0.0119
0.0000
0.0297
0.0000
0.0313
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0061
0.0000
0.0222
0.0000
0.0101
24
Nitrogen
0.0000
0.2591
0.0000
0.6044
0.0000
0.2807
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0002
0.0000
0.0011
0.0000
0.0004
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
35
H2O
0.0000
0.0066
0.0000
0.0099
0.0000
0.0037
36
Oxygen
0.0000
0.0663
0.0000
0.1768
0.0000
0.0582
37
Methane
0.0000
0.0400
0.0000
0.0534
0.0000
0.0668
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.6098
0.0000
0.1024
0.0000
0.5487
40
Ethane
0.0000
0.0119
0.0000
0.0297
0.0000
0.0313
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0061
0.0000
0.0222
0.0000
0.0101
43
Nitrogen
0.0000
0.2591
0.0000
0.6044
0.0000
0.2807
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0002
0.0000
0.0011
0.0000
0.0004
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
1.000
1.000
---
53
H2O
1.000
1.000
---
54
Oxygen
1.000
1.000
---
55
Methane
1.000
1.000
---
---
---
---
56
H2S
57
Hydrogen
1.000
1.000
---
58
Ethane
1.000
1.000
---
59
Propane
---
---
---
60
CO2
1.000
1.000
---
61
Nitrogen
1.000
1.000
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
1.000
1.000
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 135 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 46 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Conversion Reactor:
13
LOGICAL CONNECTION D-1 METANADOR
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
225.7 psia 0.0000 lbmole/hrMass:
23
0.0000 barrel/day
User Variables
24 25
NOTES
26 27
0.0000 lb/hr Std Ideal Liq Volume:
29285
28 29 30
(Last modified Tue Dec 11, 2018, 17:29)
31 32
Description
33 34 35
Material Stream: 47
36 37 38
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
39 40
Overall
Vapour Phase
Liquid Phase
41
Vapour / Phase Fraction
42
Temperature:
43
Pressure:
44
Molar Flow
45
Mass Flow
46
Std Ideal Liq Vol Flow
(barrel/day)
4323
4323
0.0000
47
Molar Enthalpy
(Btu/lbmole)
489.2
489.2
489.3
48
Molar Entropy
(Btu/lbmole-F)
33.98
33.98
49
Heat Flow
50
Liq Vol Flow @Std Cond
1.0000
1.0000
0.0000
(F)
618.7
618.7
618.7
(psia)
225.7
225.7
225.7
1969
1969
0.0000
(lbmole/hr) (lb/hr)
2.365e+004
2.365e+004
0.0000
33.98
(Btu/hr)
9.633e+005
9.633e+005
0.0000
(barrel/day)
* 3.188e+006
3.188e+006
0.0000
51
PROPERTIES
52 53
Overall
Vapour Phase
Liquid Phase
54
Molecular Weight
55
Molar Density
56
Mass Density
57
Act. Volume Flow
58
Mass Enthalpy
(Btu/lb)
40.74
40.74
40.74
59
Mass Entropy
(Btu/lb-F)
2.830
2.830
2.830
60
Heat Capacity
7.564
7.564
7.564
61
Mass Heat Capacity
0.6298
0.6298
0.6298
62
LHV Molar Basis (Std)
(Btu/lbmole)
8.465e+004
8.465e+004
8.465e+004
63
HHV Molar Basis (Std)
(Btu/lbmole)
9.756e+004
9.756e+004
9.756e+004
64
HHV Mass Basis (Std)
65
CO2 Loading
66
CO2 App ML Con
67
CO2 App WT Con
68
LHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
12.01 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.942e-002 0.2332 4.334e+005
12.01 1.942e-002 0.2332 4.334e+005
12.01 1.942e-002 0.2332 0.0000
8124
8124
8124
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
7048
7048
7048
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 136 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 47 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Phase Fraction [Vol. Basis]
1.000
1.000
---
13
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
14
Phase Fraction [Act. Vol. Basis]
15
Mass Exergy
16
Partial Pressure of CO2
17
Cost Based on Flow
18
Act. Gas Flow
19
Avg. Liq. Density
20 21 22
Std. Ideal Liq. Mass Density
23
Act. Liq. Flow
24
Z Factor
25
Watson K
26
User Property
27
Partial Pressure of H2S
28
Cp/(Cp - R)
29
Cp/Cv
30
Heat of Vap.
31
Kinematic Viscosity
32
Liq. Mass Density (Std. Cond)
33
Liq. Vol. Flow (Std. Cond)
34
Liquid Fraction
35
Molar Volume
36
Mass Heat of Vap.
37
Phase Fraction [Molar Basis]
38
Surface Tension
39
Thermal Conductivity
40
Viscosity
41
Cv (Semi-Ideal)
42
Mass Cv (Semi-Ideal)
43
Cv
44
Mass Cv
45
Cv (Ent. Method)
46
Mass Cv (Ent. Method)
47
Cp/Cv (Ent. Method)
48
Reid VP at 37.8 C
49
True VP at 37.8 C
50
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
51
Viscosity Index
1.000
1.000
0.0000
(Btu/lb)
345.1
---
---
(psia)
1.368
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1690
1690
---
(lbmole/ft3)
1.947
1.947
1.947
Specific Heat
(Btu/lbmole-F)
7.564
7.564
7.564
Std. Gas Flow
(MMSCFD)
17.90
17.90
0.0000
(lb/ft3)
23.38
23.38
23.38
(USGPS)
---
---
---
---
1.004
1.004
11.64
11.64
11.64
---
---
---
0.0000
---
---
1.356
1.356
1.356
1.359
1.359
1.359
5168
---
---
5.628
5.628
0.5358
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
3.171e-002
3.171e-002
3.188e+006
3.188e+006
3.171e-002 0.0000
0.0000
0.0000
1.000
(ft3/lbmole)
51.50
51.50
51.50
(Btu/lb)
430.3
---
---
1.0000
1.0000
0.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
5.591e-002
8.439e-002
8.439e-002
4.133e-002
2.103e-002
2.103e-002
2.001e-003
5.578
5.578
5.578
0.4645
0.4645
0.4645
5.566
5.566
5.566
0.4634
0.4634
0.4634
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
3.188e+006 -7.043
52
3.188e+006 ---
--0.0000 ---
COMPOSITION
53 54
Overall Phase
55 56
COMPONENTS
57
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
58
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
59
H2O
12.9520
0.0066
233.3318
0.0099
16.0091
0.0037
60
Oxygen
130.6356
0.0664
4180.3394
0.1768
251.5994
0.0582
61
Methane
78.7305
0.0400
1263.0648
0.0534
288.8689
0.0668
62
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Hydrogen
1200.5231
0.6098
2420.2547
0.1024
2372.2276
0.5487
64
Ethane
23.3595
0.0119
702.4180
0.0297
135.2231
0.0313
65
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
CO2
11.9321
0.0061
525.1296
0.0222
43.5667
0.0101
67
Nitrogen
510.1373
0.2591
14290.4765
0.6044
1213.4684
0.2807
68
Air
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 137 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 47 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
17
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Total
1968.8755
1.0000
1.0000
4323.1284
1.0000
19
23645.7292
Vapour Phase
20 21
COMPONENTS
22
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
23
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
24
H2O
12.9520
0.0066
233.3318
0.0099
16.0091
0.0037
25
Oxygen
130.6356
0.0664
4180.3394
0.1768
251.5994
0.0582
26
Methane
78.7305
0.0400
1263.0648
0.0534
288.8689
0.0668
27
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Hydrogen
1200.5231
0.6098
2420.2547
0.1024
2372.2276
0.5487
29
Ethane
23.3595
0.0119
702.4180
0.0297
135.2231
0.0313
30
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
CO2
11.9321
0.0061
525.1296
0.0222
43.5667
0.0101
32
Nitrogen
510.1373
0.2591
14290.4765
0.6044
1213.4684
0.2807
33
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
36
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Total
1968.8755
1.0000
1.0000
4323.1284
1.0000
38
23645.7292
Liquid Phase
39 40
COMPONENTS
41
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
42
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
43
H2O
0.0000
0.0066
0.0000
0.0099
0.0000
0.0037
44
Oxygen
0.0000
0.0663
0.0000
0.1768
0.0000
0.0582
45
Methane
0.0000
0.0400
0.0000
0.0534
0.0000
0.0668
46
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Hydrogen
0.0000
0.6098
0.0000
0.1024
0.0000
0.5487
48
Ethane
0.0000
0.0119
0.0000
0.0297
0.0000
0.0313
49
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
CO2
0.0000
0.0061
0.0000
0.0222
0.0000
0.0101
51
Nitrogen
0.0000
0.2591
0.0000
0.6044
0.0000
0.2807
52
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
MEAmine
0.0000
0.0002
0.0000
0.0011
0.0000
0.0004
55
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
57
K VALUE
58 59
COMPONENTS
MIXED
LIGHT
HEAVY
60
CO
1.000
1.000
---
61
H2O
1.000
1.000
---
62
Oxygen
1.000
1.000
---
63
Methane
1.000
1.000
---
---
---
---
64
H2S
65
Hydrogen
1.000
1.000
---
66
Ethane
1.000
1.000
---
67
Propane
---
---
---
68
CO2
1.000
1.000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 138 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 47 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
LIGHT
Nitrogen
13
Air
HEAVY
1.000
1.000
---
---
---
---
14
Mercury
---
---
---
15
MEAmine
1.000
1.000
---
16
Ammonia
---
---
---
17
UNIT OPERATIONS
18 19 20
FEED TO
PRODUCT FROM
LNG:
LNG-101 Conversion Reactor:
21
LOGICAL CONNECTION D-1 METANADOR
UTILITIES
22 23
( No utilities reference this stream )
24
PROCESS UTILITY
25 26 27
DYNAMICS
28 29
Pressure Specification
(Inactive):
30
Flow Specification
(Inactive) Molar:
225.7 psia 1969 lbmole/hrMass:
31
2.365e+004 lb/hrStd Ideal Liq Volume:
4323 barrel/day
User Variables
32 33
NOTES
34 35 36
Description
37 38 39
Material Stream: 48
40 41 42
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
43 44
Overall
Vapour Phase
45
Vapour / Phase Fraction
46
Temperature:
47
Pressure:
48
Molar Flow
49
Mass Flow
50
Std Ideal Liq Vol Flow
(barrel/day)
4323
4323
51
Molar Enthalpy
(Btu/lbmole)
-177.8
-177.8
52
Molar Entropy
(Btu/lbmole-F)
53
Heat Flow
54
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
530.0*
530.0
(psia)
225.7
225.7
(lbmole/hr) (lb/hr)
1969 2.365e+004
33.34
1969 2.365e+004
33.34
(Btu/hr)
-3.501e+005
-3.501e+005
(barrel/day)
* 3.188e+006
3.188e+006
55
PROPERTIES
56 57
Overall
Vapour Phase
58
Molecular Weight
59
Molar Density
60
Mass Density
61
Act. Volume Flow
62
Mass Enthalpy
(Btu/lb)
-14.81
-14.81
63
Mass Entropy
(Btu/lb-F)
2.776
2.776
64
Heat Capacity
65
Mass Heat Capacity
66
LHV Molar Basis (Std)
(Btu/lbmole)
8.465e+004
8.465e+004
67
HHV Molar Basis (Std)
(Btu/lbmole)
9.756e+004
9.756e+004
68
HHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
12.01 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.116e-002 0.2541 3.978e+005
12.01 2.116e-002 0.2541 3.978e+005
7.477
7.477
0.6226
0.6226
8124
8124
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 139 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 48 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
CO2 Loading
13
CO2 App ML Con
14
CO2 App WT Con
15
LHV Mass Basis (Std)
16 17
Vapour Phase ---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7048
7048
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
18
Phase Fraction [Act. Vol. Basis]
1.000
1.000
19
Mass Exergy
(Btu/lb)
318.4
---
20
Partial Pressure of CO2
(psia)
1.368
---
21
Cost Based on Flow
(Cost/s)
0.0000
0.0000
22
Act. Gas Flow
23
Avg. Liq. Density
24 25 26
Std. Ideal Liq. Mass Density
27
Act. Liq. Flow
28
(ACFM)
1551
1551
(lbmole/ft3)
1.947
1.947
Specific Heat
(Btu/lbmole-F)
7.477
7.477
Std. Gas Flow
(MMSCFD)
17.90
17.90
(lb/ft3)
23.38
23.38
(USGPS)
---
---
Z Factor
1.004
1.004
29
Watson K
11.64
11.64
30
User Property
---
---
31
Partial Pressure of H2S
32
Cp/(Cp - R)
33
Cp/Cv
34
Heat of Vap.
35
Kinematic Viscosity
36
Liq. Mass Density (Std. Cond)
37
Liq. Vol. Flow (Std. Cond)
38
Liquid Fraction
39
Molar Volume
40
Mass Heat of Vap.
41
Phase Fraction [Molar Basis]
42
Surface Tension
43
Thermal Conductivity
44
Viscosity
45
Cv (Semi-Ideal)
46
Mass Cv (Semi-Ideal)
47
Cv
48
Mass Cv
49
Cv (Ent. Method)
50
Mass Cv (Ent. Method)
51
Cp/Cv (Ent. Method)
52
Reid VP at 37.8 C
53
True VP at 37.8 C
54
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
55
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.362
1.362
1.366
1.366
5168
---
4.786
4.786
3.171e-002
3.171e-002
3.188e+006
3.188e+006
0.0000
0.0000
(ft3/lbmole)
47.26
47.26
(Btu/lb)
430.3
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
7.923e-002
7.923e-002
1.948e-002
1.948e-002
5.491
5.491
0.4572
0.4572
5.476
5.476
0.4559
0.4559
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.188e+006 -8.874
56
3.188e+006 ---
COMPOSITION
57 58
Overall Phase
59 60
COMPONENTS
61
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
62
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
63
H2O
12.9520
0.0066
233.3318
0.0099
16.0091
0.0037
64
Oxygen
130.6356
0.0664
4180.3394
0.1768
251.5994
0.0582
65
Methane
78.7305
0.0400
1263.0648
0.0534
288.8689
0.0668
66
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Hydrogen
1200.5231
0.6098
2420.2547
0.1024
2372.2276
0.5487
68
Ethane
23.3595
0.0119
702.4180
0.0297
135.2231
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0313
Page 140 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 48 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14 15
Propane
16
CO2
17
Nitrogen
18
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
11.9321
0.0061
525.1296
0.0222
43.5667
0.0101
510.1373
0.2591
14290.4765
0.6044
1213.4684
0.2807
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
21
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Total
1968.8755
1.0000
1.0000
4323.1284
1.0000
23
23645.7292
Vapour Phase
24 25
COMPONENTS
26
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
27
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
28
H2O
12.9520
0.0066
233.3318
0.0099
16.0091
0.0037
29
Oxygen
130.6356
0.0664
4180.3394
0.1768
251.5994
0.0582
30
Methane
78.7305
0.0400
1263.0648
0.0534
288.8689
0.0668
31
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Hydrogen
1200.5231
0.6098
2420.2547
0.1024
2372.2276
0.5487
33
Ethane
23.3595
0.0119
702.4180
0.0297
135.2231
0.0313
34
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
CO2
11.9321
0.0061
525.1296
0.0222
43.5667
0.0101
36
Nitrogen
510.1373
0.2591
14290.4765
0.6044
1213.4684
0.2807
37
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
40
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Total
1968.8755
1.0000
1.0000
4323.1284
1.0000
23645.7292
42
K VALUE
43 44
COMPONENTS
MIXED
LIGHT
HEAVY
45
CO
---
---
---
46
H2O
---
---
---
47
Oxygen
---
---
---
48
Methane
---
---
---
---
---
---
49
H2S
50
Hydrogen
---
---
---
51
Ethane
---
---
---
52
Propane
---
---
---
53
CO2
---
---
---
54
Nitrogen
---
---
---
---
---
---
55
Air
56
Mercury
---
---
---
57
MEAmine
---
---
---
58
Ammonia
---
---
---
59
UNIT OPERATIONS
60 61 62
FEED TO Cooler:
63
PRODUCT FROM E-101
LNG:
LOGICAL CONNECTION LNG-101
UTILITIES
64 65
( No utilities reference this stream )
66
PROCESS UTILITY
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 141 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 48 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
DYNAMICS
10 11
Pressure Specification
(Inactive):
12
Flow Specification
(Inactive) Molar:
225.7 psia 1969 lbmole/hrMass:
13
2.365e+004 lb/hrStd Ideal Liq Volume:
4323 barrel/day
User Variables
14 15
NOTES
16 17 18
Description
19 20 21
Material Stream: 49
22 23 24
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
25 26
Overall
Vapour Phase
27
Vapour / Phase Fraction
28
Temperature:
29
Pressure:
30
Molar Flow
31
Mass Flow
32
Std Ideal Liq Vol Flow
(barrel/day)
4323
4318
33
Molar Enthalpy
(Btu/lbmole)
-3346
-3110
34
Molar Entropy
(Btu/lbmole-F)
35
Heat Flow
36
Liq Vol Flow @Std Cond
Liquid Phase
Aqueous Phase
0.9980
0.9980
0.0001
0.0019
(F)
100.0*
100.0
100.0
100.0
(psia)
220.7
220.7
220.7
220.7
1969
1965
0.2592
3.646
14.07
65.69
(lbmole/hr) (lb/hr)
2.365e+004
29.18
2.357e+004
29.21
(Btu/hr)
-6.588e+006
-6.111e+006
(barrel/day)
* 3.188e+006
3.181e+006
37
0.9507 -1.136e+005 6.286 -2.944e+004 0.9716
4.508 -1.226e+005 13.60 -4.471e+005 4.433
PROPERTIES
38 39
Overall
Vapour Phase
Liquid Phase
Aqueous Phase
40
Molecular Weight
41
Molar Density
42
Mass Density
43
Act. Volume Flow
44
Mass Enthalpy
(Btu/lb)
-278.6
-259.3
-2093
-6805
45
Mass Entropy
(Btu/lb-F)
2.429
2.435
0.1158
0.7551
46
Heat Capacity
47
Mass Heat Capacity
48
LHV Molar Basis (Std)
(Btu/lbmole)
8.465e+004
8.475e+004
4.940e+005
49
HHV Molar Basis (Std)
(Btu/lbmole)
9.756e+004
9.765e+004
5.487e+005
50
HHV Mass Basis (Std)
51
CO2 Loading
52
CO2 App ML Con
(lbmole/ft3)
53
CO2 App WT Con
(lbmol/lb)
54
LHV Mass Basis (Std)
(Btu/lb)
55
Phase Fraction [Vol. Basis]
0.9987
0.9987
2.199e-004
1.043e-003
56
Phase Fraction [Mass Basis]
0.9966
0.9966
5.950e-004
2.778e-003
57
Phase Fraction [Act. Vol. Basis]
1.000
1.000
4.352e-006
1.969e-005
58
Mass Exergy
(Btu/lb)
240.6
---
---
59
Partial Pressure of CO2
(psia)
1.340
---
---
---
60
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
0.0000
61
Act. Gas Flow
62
Avg. Liq. Density
63 64 65
Std. Ideal Liq. Mass Density
66
Act. Liq. Flow
67
Z Factor
68
Watson K
69
Aspen Technology Inc.
12.01 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.676e-002 0.4415 2.289e+005
11.99 3.669e-002 0.4400 2.289e+005
54.29
18.02
1.112
3.458
60.36
62.31
0.9964
4.507
7.130
7.105
39.23
18.56
0.5937
0.5924
0.7226
1.030 15.28 1.765e+004
8124
8142
1.011e+004
---
---
1.236e-003
---
---
1.156e-003
1.115e-004
---
---
1.915e-005
1.789e-006
7048
7066
9101
979.4 1.373
0.8482
---
(ACFM)
892.6
892.6
---
---
(lbmole/ft3)
1.947
1.945
1.165
3.458
Specific Heat
(Btu/lbmole-F)
7.130
7.105
Std. Gas Flow
(MMSCFD)
17.90
17.86
23.38
23.33
Licensed to: LEGENDS
(lb/ft3) (USGPS)
2.675e-003
39.23 2.356e-003 63.26
18.56 3.314e-002 62.30
---
4.843e-004
2.191e-003
---
1.002
3.305e-002
1.063e-002
11.64
11.64
9.110
Aspen HYSYS Version 8.8 (34.0.0.8909)
8.332
Page 142 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 49 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
User Property
13
Partial Pressure of H2S
14
Cp/(Cp - R)
15
Cp/Cv
16
Heat of Vap.
17
Kinematic Viscosity
18
Liq. Mass Density (Std. Cond)
19
Liq. Vol. Flow (Std. Cond)
20
Liquid Fraction
21
Molar Volume
22
Mass Heat of Vap.
23
Phase Fraction [Molar Basis]
24
Surface Tension
25
Thermal Conductivity
26
Viscosity
27
Cv (Semi-Ideal)
28
Mass Cv (Semi-Ideal)
29
Cv
30
Mass Cv
31
Cv (Ent. Method)
32
Mass Cv (Ent. Method)
33
Cp/Cv (Ent. Method)
34
Reid VP at 37.8 C
(psia)
35
True VP at 37.8 C
(psia)
36
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
37
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
Vapour Phase
(Btu/lb)
Aqueous Phase
---
---
0.0000
---
---
---
1.386
1.388
1.053
1.120
1.402
1.406
1.751
1.154
5165
---
---
---
---
1.728
10.21
0.6813
---
3.171e-002
3.167e-002
61.90
63.35
3.188e+006
3.181e+006
0.9716
4.433
1.984e-003 (ft3/lbmole)
Liquid Phase
---
27.20
0.0000
1.000
1.000
27.26
0.8994
0.2892
430.0
---
---
---
0.9980
0.9980
0.0001
0.0019
(dyne/cm)
---
50.63
69.87
(Btu/hr-ft-F)
---
5.128e-002
0.1358
0.3633
---
1.218e-002
9.875
0.6799
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
5.144
5.119
37.24
16.57
0.4284
0.4268
0.6860
0.9199
5.084
5.055
22.40
16.08
0.4234
0.4215
0.4125
0.8925
---
---
23.79
15.91
---
---
0.4382
0.8829
---
---
1.649
1.167
---
---
9.275
3393
---
---
220.6
203.8
0.9716
4.433
---
---
3.181e+006 -23.99
38
3.181e+006 ---
COMPOSITION
39 40
Overall Phase
41 42
COMPONENTS
43
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9980
LIQUID VOLUME FRACTION
44
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
45
H2O
12.9520
0.0066
233.3318
0.0099
16.0091
0.0037
46
Oxygen
130.6356
0.0664
4180.3394
0.1768
251.5994
0.0582
47
Methane
78.7305
0.0400
1263.0648
0.0534
288.8689
0.0668
48
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Hydrogen
1200.5231
0.6098
2420.2547
0.1024
2372.2276
0.5487
50
Ethane
23.3595
0.0119
702.4180
0.0297
135.2231
0.0313
51
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
CO2
11.9321
0.0061
525.1296
0.0222
43.5667
0.0101
53
Nitrogen
510.1373
0.2591
14290.4765
0.6044
1213.4684
0.2807
54
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
57
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Total
1968.8755
1.0000
1.0000
4323.1284
1.0000
59
23645.7292
Vapour Phase
60 61
COMPONENTS
62
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9980 LIQUID VOLUME FRACTION
63
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
64
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
65
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
66
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
67
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.5494
Page 143 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 49 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
COMPONENTS
14 15
Ethane
16
Propane
17
CO2
18
Nitrogen
19
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
0.9980
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
22
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
23565.9660
24
Liquid Phase
25 26
COMPONENTS
27
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.316e-004 LIQUID VOLUME FRACTION
28
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
H2O
0.0395
0.1522
0.7107
0.0505
0.0488
0.0513
30
Oxygen
0.0002
0.0008
0.0069
0.0005
0.0004
0.0004
31
Methane
0.0002
0.0006
0.0027
0.0002
0.0006
0.0006
32
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
Hydrogen
0.0004
0.0016
0.0008
0.0001
0.0008
0.0008
34
Ethane
0.0003
0.0011
0.0083
0.0006
0.0016
0.0017
35
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
CO2
0.0003
0.0010
0.0119
0.0008
0.0010
0.0010
37
Nitrogen
0.0004
0.0014
0.0098
0.0007
0.0008
0.0009
38
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
MEAmine
0.2180
0.8413
13.3183
0.9466
0.8967
0.9432
41
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Total
0.2592
1.0000
14.0693
1.0000
0.9507
1.0000
43
Aqueous Phase
44 45
COMPONENTS
46
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.852e-003 LIQUID VOLUME FRACTION
47
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
H2O
3.6458
0.9999
65.6787
0.9998
4.5063
0.9997
49
Oxygen
0.0000
0.0000
0.0005
0.0000
0.0000
0.0000
50
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
Hydrogen
0.0001
0.0000
0.0001
0.0000
0.0001
0.0000
53
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
CO2
0.0001
0.0000
0.0052
0.0001
0.0004
0.0001
56
Nitrogen
0.0001
0.0000
0.0042
0.0001
0.0004
0.0001
57
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
MEAmine
0.0001
0.0000
0.0052
0.0001
0.0004
0.0001
60
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Total
3.6462
1.0000
65.6939
1.0000
4.5076
1.0000
62
K VALUE
63 64
COMPONENTS
MIXED
65
CO
66
H2O
67
Oxygen
68 69
Methane
Aspen Technology Inc. Licensed to: LEGENDS
LIGHT 2985 4.998e-003
HEAVY 215.9 3.098e-002
1133
80.26
941.1
62.46
Aspen HYSYS Version 8.8 (34.0.0.8909)
3.388e+004 4.717e-003 1.674e+004 5.940e+006
Page 144 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 49 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
H2S
LIGHT
HEAVY
---
---
Hydrogen
5212
391.3
4.186e+004
14
Ethane
169.1
11.22
2.250e+008
15
Propane
---
---
---
16
CO2
61.28
5.841
188.3
17
Nitrogen
2030
191.7
6375
---
---
---
---
---
13
18
Air
19
Mercury
20
MEAmine
21
Ammonia
1.803e-003
4.287
---
---
UNIT OPERATIONS
23 24 25
---
1.197e-004
---
22
---
FEED TO
PRODUCT FROM
Separator:
D-9
Cooler:
LOGICAL CONNECTION E-101
26
UTILITIES
27 28
( No utilities reference this stream )
29
PROCESS UTILITY
30 31 32
DYNAMICS
33 34
Pressure Specification
(Inactive):
35
Flow Specification
(Inactive) Molar:
220.7 psia 1969 lbmole/hrMass:
36
2.365e+004 lb/hrStd Ideal Liq Volume:
4323 barrel/day
User Variables
37 38
NOTES
39 40 41
Description
42 43 44
Material Stream: 50
45 46 47
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
48 49
Overall
50
Vapour / Phase Fraction
51
Temperature:
52
Pressure:
53
Molar Flow
54
Mass Flow
55
Std Ideal Liq Vol Flow
(barrel/day)
56
Molar Enthalpy
(Btu/lbmole)
57
Molar Entropy
(Btu/lbmole-F)
58
Heat Flow
59
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
Aqueous Phase
0.0000
0.0000
0.0664
0.9336
(F)
100.0
100.0
100.0
100.0
(psia)
220.7
220.7
220.7
220.7
3.905
0.0000
0.2592
3.646
79.76
0.0000
14.07
65.69
5.458
0.0000
0.9507
(lbmole/hr) (lb/hr)
(Btu/hr)
-1.220e+005 13.12 -4.765e+005 5.457*
(barrel/day)
60
-3110 29.21 0.0000 0.0000
-1.136e+005 6.286 -2.944e+004 0.9716
4.508 -1.226e+005 13.60 -4.471e+005 4.433
PROPERTIES
61 62
Overall
63
Molecular Weight
64
Molar Density
65
Mass Density
66
Act. Volume Flow
67 68 69
Fluid Package:
Vapour Phase 20.42
(lbmole/ft3)
3.669e-002
Liquid Phase
Aqueous Phase
54.29
18.02
1.112
3.458
61.95
0.4400
60.36
62.31
(barrel/day)
5.503
0.0000
0.9964
4.507
Mass Enthalpy
(Btu/lb)
-5974
-259.3
-2093
-6805
Mass Entropy
(Btu/lb-F)
0.6423
2.435
0.1158
0.7551
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
3.033
11.99
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 145 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 50 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
Aqueous Phase
12
Heat Capacity
13
Mass Heat Capacity
14
LHV Molar Basis (Std)
(Btu/lbmole)
3.280e+004
8.475e+004
4.940e+005
15
HHV Molar Basis (Std)
(Btu/lbmole)
5.289e+004
9.765e+004
5.487e+005
16
HHV Mass Basis (Std)
17
CO2 Loading
18
CO2 App ML Con
19
CO2 App WT Con
20
LHV Mass Basis (Std)
21
Phase Fraction [Vol. Basis]
22
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
19.93
7.105
39.23
18.56
0.9758
0.5924
0.7226
1.030
2590
15.28 1.765e+004
8142
1.011e+004
1.774e-003
---
1.236e-003
(lbmole/ft3)
3.006e-004
---
1.156e-003
1.115e-004
(lbmol/lb)
4.852e-006
---
1.915e-005
1.789e-006
(Btu/lb)
979.4 1.373
1606
7066
9101
0.8482
---
---
0.1742
0.8258
Phase Fraction [Mass Basis]
0.0000
0.0000
0.1764
0.8236
23
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
0.1810
0.8190
24
Mass Exergy
(Btu/lb)
1.271
---
---
---
25
Partial Pressure of CO2
(psia)
0.0000
---
---
---
26
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
0.0000
27
Act. Gas Flow
28
Avg. Liq. Density
29
Specific Heat
(Btu/lbmole-F)
30
Std. Gas Flow
(MMSCFD)
31
Std. Ideal Liq. Mass Density
32
Act. Liq. Flow
33
Z Factor
34
Watson K
35
User Property
36
Partial Pressure of H2S
37
Cp/(Cp - R)
38
Cp/Cv
39
Heat of Vap.
40
Kinematic Viscosity
41
Liq. Mass Density (Std. Cond)
42
Liq. Vol. Flow (Std. Cond)
43
Liquid Fraction
44
Molar Volume
45
Mass Heat of Vap.
46
Phase Fraction [Molar Basis]
47
Surface Tension
48
Thermal Conductivity
49
Viscosity
50
Cv (Semi-Ideal)
51
Mass Cv (Semi-Ideal)
52
Cv
53
Mass Cv
54
Cv (Ent. Method)
55
Mass Cv (Ent. Method)
56
Cp/Cv (Ent. Method)
57
(ACFM)
---
---
---
---
(lbmole/ft3)
3.058
1.945
1.165
3.458
(lb/ft3)
19.93 3.550e-002 62.47
(USGPS)
2.675e-003
(psia)
(Btu/lbmole)
62.30
---
4.843e-004
2.191e-003
3.305e-002
1.063e-002
1.002 11.64
9.110
8.332
---
---
---
---
0.0000
---
---
---
1.111
1.388
1.053
1.120
1.202
1.406
1.751
1.154
---
---
---
1.728
10.21
0.6813
1.620e+004
(lb/ft3)
62.48
(Btu/lb)
63.26
18.56 3.314e-002
---
0.9833
(ft3/lbmole)
23.33
39.23 2.356e-003
9.109
(cSt) (barrel/day)
7.105 0.0000
61.90
63.35
5.457
3.167e-002 0.0000
0.9716
4.433
1.000
0.0000
1.000
1.000
0.3297
27.26
0.8994
0.2892
793.1
---
---
---
0.0000
0.0000
0.0664
0.9336
(dyne/cm)
---
50.63
69.87
(Btu/hr-ft-F)
0.3067
5.128e-002
0.1358
0.3633
0.9758
1.218e-002
9.875
0.6799
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
17.94
5.119
37.24
16.57
0.8786
0.4268
0.6860
0.9199
16.59
5.055
22.40
16.08
0.8122
0.4215
0.4125
0.8925
---
---
23.79
15.91
(Btu/lb-F)
---
---
0.4382
0.8829
---
---
1.649
1.167
Reid VP at 37.8 C
(psia)
11.08
---
9.275
3393
58
True VP at 37.8 C
(psia)
219.8
---
220.6
203.8
59
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
5.404
0.0000
0.9716
4.433
60
Viscosity Index
3.703
---
---
---
61
COMPOSITION
62 63
Overall Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
3.6852
0.9436
66.3895
0.8323
4.5550
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
LIQUID VOLUME FRACTION 0.0000 0.8345
Page 146 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 50 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
Oxygen
0.0002
0.0001
0.0073
0.0001
0.0004
0.0001
16
Methane
0.0002
0.0000
0.0027
0.0000
0.0006
0.0001
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0005
0.0001
0.0009
0.0000
0.0009
0.0002
19
Ethane
0.0003
0.0001
0.0083
0.0001
0.0016
0.0003
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0004
0.0001
0.0170
0.0002
0.0014
0.0003
22
Nitrogen
0.0005
0.0001
0.0140
0.0002
0.0012
0.0002
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.2181
0.0559
13.3235
0.1670
0.8971
0.1644
26
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Total
3.9053
1.0000
79.7632
1.0000
5.4583
1.0000
28
Vapour Phase
29 30
COMPONENTS
31
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
32
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
33
H2O
0.0000
0.0047
0.0000
0.0071
0.0000
0.0027
34
Oxygen
0.0000
0.0665
0.0000
0.1774
0.0000
0.0583
35
Methane
0.0000
0.0401
0.0000
0.0536
0.0000
0.0669
36
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Hydrogen
0.0000
0.6110
0.0000
0.1027
0.0000
0.5494
38
Ethane
0.0000
0.0119
0.0000
0.0298
0.0000
0.0313
39
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
CO2
0.0000
0.0061
0.0000
0.0223
0.0000
0.0101
41
Nitrogen
0.0000
0.2596
0.0000
0.6064
0.0000
0.2810
42
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
MEAmine
0.0000
0.0001
0.0000
0.0005
0.0000
0.0002
45
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
47
Liquid Phase
48 49
COMPONENTS
50
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
6.636e-002 LIQUID VOLUME FRACTION
51
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
H2O
0.0395
0.1522
0.7107
0.0505
0.0488
0.0513
53
Oxygen
0.0002
0.0008
0.0069
0.0005
0.0004
0.0004
54
Methane
0.0002
0.0006
0.0027
0.0002
0.0006
0.0006
55
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Hydrogen
0.0004
0.0016
0.0008
0.0001
0.0008
0.0008
57
Ethane
0.0003
0.0011
0.0083
0.0006
0.0016
0.0017
58
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
CO2
0.0003
0.0010
0.0119
0.0008
0.0010
0.0010
60
Nitrogen
0.0004
0.0014
0.0098
0.0007
0.0008
0.0009
61
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
MEAmine
0.2180
0.8413
13.3183
0.9466
0.8967
0.9432
64
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Total
0.2592
1.0000
14.0693
1.0000
0.9507
1.0000
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 147 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 50 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Aqueous Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9336 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
3.6458
0.9999
65.6787
0.9998
4.5063
0.9997
17
Oxygen
0.0000
0.0000
0.0005
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0001
0.0000
0.0001
0.0000
0.0001
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0001
0.0000
0.0052
0.0001
0.0004
0.0001
24
Nitrogen
0.0001
0.0000
0.0042
0.0001
0.0004
0.0001
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0001
0.0000
0.0052
0.0001
0.0004
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
3.6462
1.0000
65.6939
1.0000
4.5076
1.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
34
H2O
35
Oxygen
1133
80.26
1.674e+004
36
Methane
941.1
62.46
5.940e+006
---
---
Hydrogen
5212
391.3
4.186e+004
39
Ethane
169.1
11.22
2.250e+008
40
Propane
---
---
---
41
CO2
61.28
5.841
188.3
42
Nitrogen
2030
191.7
6375
---
---
---
---
---
37
2985 4.998e-003
H2S
38
43
Air
44
Mercury
45
MEAmine
46
Ammonia
215.9
1.803e-003
4.717e-003
---
---
1.197e-004
---
47
3.388e+004
3.098e-002
4.287
---
---
UNIT OPERATIONS
48 49
FEED TO
PRODUCT FROM
50
Separator:
51
LOGICAL CONNECTION D-9
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Inactive) Molar:
61
220.7 psia 3.905 lbmole/hrMass:
79.76 lb/hr Std Ideal Liq Volume:
5.458 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 148 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 51
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Vapour Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
18
Molar Enthalpy
(Btu/lbmole)
-3110
-3110
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Liquid Phase
1.0000
1.0000
0.0000
(F)
99.94
99.94
99.94
(psia)
214.7
214.7
214.7
1965
1965
0.0000
(lbmole/hr) (lb/hr)
2.357e+004
29.26
2.357e+004
29.26
0.0000 0.0000 -1.136e+005 6.272
(Btu/hr)
-6.111e+006
-6.111e+006
0.0000
(barrel/day)
* 3.181e+006
3.181e+006
0.0000
22
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-259.3
-259.3
-2092
30
Mass Entropy
(Btu/lb-F)
2.440
2.440
0.1155
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
4.944e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
5.491e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41 42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
11.99 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.570e-002 0.4281 2.353e+005
11.99 3.570e-002 0.4281 2.353e+005
54.31 0.7208 39.15 0.0000
7.103
7.103
39.24
0.5922
0.5922
0.7225
8142
8142
---
---
1.011e+004 ---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
7066
7066
9103
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
238.6
---
---
(psia)
1.304
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
917.4
917.4
---
(lbmole/ft3)
1.945
1.945
1.165
Specific Heat
(Btu/lbmole-F)
7.103
7.103
39.24
Std. Gas Flow
(MMSCFD)
17.86
17.86
0.0000
(lb/ft3)
23.33
23.33
63.26
(USGPS)
---
---
---
1.002
11.64
11.64
9.110
---
---
---
0.0000
---
---
1.388
1.388
1.053
1.405
1.405
1.753
4951
---
---
1.776
1.776
11.81
Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
--4.960e-002
3.167e-002
3.167e-002
61.90
3.181e+006
3.181e+006
0.0000
0.0000
0.0000
1.000
(ft3/lbmole)
28.01
28.01
1.387
(Btu/lb)
412.8
---
---
1.0000
1.0000
0.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
50.63
5.126e-002
5.126e-002
0.1358
1.218e-002
1.218e-002
7.409
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 149 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 51 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
5.117
5.117
37.25
0.4267
0.4267
0.6859
5.055
5.055
22.38
0.4215
0.4215
0.4121
---
---
---
---
---
---
---
---
---
---
---
9.211
---
---
3.181e+006 -23.72
23
3.181e+006 ---
219.0 0.0000 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
30
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
31
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
32
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
35
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
38
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
44
23565.9660
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
49
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
50
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
51
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
54
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
57
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
63
23565.9660
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
0.0000
0.1517
0.0000
0.0503
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000 LIQUID VOLUME FRACTION 0.0000 0.0511
Page 150 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 51 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
Oxygen
0.0000
0.0008
0.0000
0.0005
0.0000
0.0004
16
Methane
0.0000
0.0006
0.0000
0.0002
0.0000
0.0006
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0000
0.0016
0.0000
0.0001
0.0000
0.0008
19
Ethane
0.0000
0.0011
0.0000
0.0006
0.0000
0.0017
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0000
0.0010
0.0000
0.0008
0.0000
0.0010
22
Nitrogen
0.0000
0.0013
0.0000
0.0007
0.0000
0.0009
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0000
0.8419
0.0000
0.9468
0.0000
0.9434
26
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
80.76
80.76
---
34
Methane
62.79
62.79
---
---
---
---
35
217.3
217.3
3.109e-002
H2S
---
3.109e-002
---
36
Hydrogen
394.1
394.1
---
37
Ethane
11.26
11.26
---
38
Propane
---
---
---
39
CO2
5.873
5.873
---
40
Nitrogen
193.0
193.0
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
1.196e-004 ---
45
---
---
---
UNIT OPERATIONS
46 47 48
1.196e-004
FEED TO
PRODUCT FROM
Compressor:
K-100
49
Separator:
LOGICAL CONNECTION D-9
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
214.7 psia 1965 lbmole/hrMass:
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 151 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 52
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Vapour Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
18
Molar Enthalpy
(Btu/lbmole)
-693.7
-693.7
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
434.3
434.3
(psia)
814.7*
814.7
(lbmole/hr) (lb/hr)
1965 2.357e+004
29.97
1965 2.357e+004
29.97
(Btu/hr)
-1.363e+006
-1.363e+006
(barrel/day)
* 3.181e+006
3.181e+006
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-57.84
-57.84
30
Mass Entropy
(Btu/lb-F)
2.499
2.499
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
34
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41
11.99 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
8.353e-002 1.002 1.006e+005
11.99 8.353e-002 1.002 1.006e+005
7.444
7.444
0.6207
0.6207
8142
8142
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7066
7066
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
(Btu/lb)
408.4
---
44
Partial Pressure of CO2
(psia)
4.947
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48
(ACFM)
392.1
392.1
(lbmole/ft3)
1.945
1.945
Specific Heat
(Btu/lbmole-F)
7.444
7.444
49
Std. Gas Flow
(MMSCFD)
17.86
17.86
50
Std. Ideal Liq. Mass Density
(lb/ft3)
23.33
23.33
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
1.017
1.017
53
Watson K
11.64
11.64
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.364
1.364
1.381
1.381
5169
---
1.120
1.120
3.167e-002
3.167e-002
3.181e+006
3.181e+006
0.0000
0.0000
(ft3/lbmole)
11.97
11.97
(Btu/lb)
431.0
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
7.427e-002
7.427e-002
1.797e-002
1.797e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 152 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 52 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 5.458
5.458
0.4551
0.4551
5.390
5.390
0.4494
0.4494
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.181e+006
3.181e+006
-23.19
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
30
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
31
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
32
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
35
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
38
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
44
23565.9660
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
49
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
50
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
51
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
54
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
57
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
63
K VALUE
64 65
23565.9660
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 153 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 52 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Cooler:
E-103
Compressor:
27
LOGICAL CONNECTION K-100
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Inactive) Molar:
* 814.7 psia
1965 lbmole/hrMass:
37
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 53
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
Vapour Phase
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
57
Molar Enthalpy
(Btu/lbmole)
-1687
-1687
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
300.0*
300.0
(psia)
814.7
814.7
(lbmole/hr) (lb/hr)
1965 2.357e+004
28.77
1965 2.357e+004
28.77
(Btu/hr)
-3.315e+006
-3.315e+006
(barrel/day)
* 3.181e+006
3.181e+006
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 11.99
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
9.837e-002 1.180 8.538e+004 -140.7
11.99 9.837e-002 1.180 8.538e+004 -140.7
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 154 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 53 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
16
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22 23
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.399
2.399
7.350
7.350
0.6128
0.6128
8142
8142
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7066
7066
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
24
Phase Fraction [Act. Vol. Basis]
1.000
1.000
25
Mass Exergy
(Btu/lb)
379.5
---
26
Partial Pressure of CO2
(psia)
4.947
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30
(ACFM)
332.9
332.9
(lbmole/ft3)
1.945
1.945
Specific Heat
(Btu/lbmole-F)
7.350
7.350
31
Std. Gas Flow
(MMSCFD)
17.86
17.86
32
Std. Ideal Liq. Mass Density
(lb/ft3)
23.33
23.33
33
Act. Liq. Flow
(USGPS)
---
---
34
Z Factor
1.016
1.016
35
Watson K
11.64
11.64
36
User Property
---
---
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.370
1.370
1.397
1.397
5169
---
0.8293
0.8293
3.167e-002
3.167e-002
3.181e+006
3.181e+006
0.0000
0.0000
(ft3/lbmole)
10.17
10.17
(Btu/lb)
431.0
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
6.586e-002
6.586e-002
1.567e-002
1.567e-002
5.364
5.364
0.4473
0.4473
5.261
5.261
0.4386
0.4386
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.181e+006 -31.06
62
3.181e+006 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.1895
MOLE FRACTION 0.0001
MASS FLOW (lb/hr) 5.3071
Vapour Fraction MASS FRACTION 0.0002
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.4546
1.0000
LIQUID VOLUME FRACTION 0.0001
Page 155 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 53 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
16
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
17
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
20
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
23
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
29
23565.9660
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
33
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
34
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
35
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
36
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
39
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
42
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
23565.9660
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
---
---
---
52
H2O
---
---
---
53
Oxygen
---
---
---
54
Methane
---
---
---
---
---
---
55
H2S
56
Hydrogen
---
---
---
57
Ethane
---
---
---
58
Propane
---
---
---
59
CO2
---
---
---
60
Nitrogen
---
---
---
---
---
---
61
Air
62
Mercury
---
---
---
63
MEAmine
---
---
---
64
Ammonia
---
---
---
65
UNIT OPERATIONS
66 67 68 69
FEED TO Compressor:
Aspen Technology Inc. Licensed to: LEGENDS
PRODUCT FROM K-101
Cooler:
LOGICAL CONNECTION E-103
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 156 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 53 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Inactive):
18
Flow Specification
(Inactive) Molar:
814.7 psia 1965 lbmole/hrMass:
19
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: 54
28 29 30
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
Vapour Phase
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
39
Molar Enthalpy
(Btu/lbmole)
-295.3
-295.3
40
Molar Entropy
(Btu/lbmole-F)
41
Heat Flow
42
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
487.1
487.1
(psia)
1515*
1515
(lbmole/hr) (lb/hr)
1965 2.357e+004
29.14
1965 2.357e+004
29.14
(Btu/hr)
-5.803e+005
-5.803e+005
(barrel/day)
* 3.181e+006
3.181e+006
43
PROPERTIES
44 45
Overall
Vapour Phase
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Mass Enthalpy
(Btu/lb)
-24.62
-24.62
51
Mass Entropy
(Btu/lb-F)
2.430
2.430
52
Heat Capacity
53
Mass Heat Capacity
54
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
55
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
56
HHV Mass Basis (Std)
57
CO2 Loading
58
CO2 App ML Con
59
CO2 App WT Con
60
LHV Mass Basis (Std)
61 62
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
11.99
0.1445
0.1445
1.733 5.812e+004
1.733 5.812e+004
7.547
7.547
0.6292
0.6292
8142
8142
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7066
7066
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
63
Phase Fraction [Act. Vol. Basis]
1.000
1.000
64
Mass Exergy
(Btu/lb)
478.7
---
65
Partial Pressure of CO2
(psia)
9.198
---
66
Cost Based on Flow
(Cost/s)
0.0000
0.0000
67
Act. Gas Flow
(ACFM)
226.6
226.6
68
Avg. Liq. Density
(lbmole/ft3)
1.945
1.945
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
11.99
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 157 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 54 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Specific Heat
(Btu/lbmole-F)
7.547
7.547
13
Std. Gas Flow
(MMSCFD)
17.86
17.86
14
Std. Ideal Liq. Mass Density
(lb/ft3)
23.33
23.33
15
Act. Liq. Flow
(USGPS)
---
---
16
Z Factor
1.031
1.031
17
Watson K
11.64
11.64
18
User Property
---
---
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
41
True VP at 37.8 C
42
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
43
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.357
1.357
1.382
1.382
5226
---
0.6870
0.6870
3.167e-002
3.167e-002
3.181e+006
3.181e+006
0.0000
0.0000
(ft3/lbmole)
6.919
6.919
(Btu/lb)
435.8
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
7.818e-002
7.818e-002
1.908e-002
1.908e-002
5.561
5.561
0.4637
0.4637
5.459
5.459
0.4552
0.4552
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.181e+006 -31.26
44
3.181e+006 ---
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
50
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
51
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
52
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
53
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
54
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
56
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
57
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
59
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
60
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
63
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
23565.9660
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 158 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 54 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
16
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
17
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
18
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
21
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
24
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
23565.9660
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Cooler:
E-104
51
Compressor:
LOGICAL CONNECTION K-101
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Active):
60
Flow Specification
(Inactive) Molar:
61
1965 lbmole/hrMass:
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
62 63
NOTES
64 65
* 1515 psia
29285
66 67 68 69
(Last modified Mon Dec 17, 2018, 15:08)
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 159 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 54 (continued)
7 8
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
9 10
Description
11 12 13
Material Stream: 55
14 15 16
CONDITIONS
17 18
Overall
Vapour Phase
19
Vapour / Phase Fraction
20
Temperature:
21
Pressure:
22
Molar Flow
23
Mass Flow
24
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
25
Molar Enthalpy
(Btu/lbmole)
-2441
-2441
26
Molar Entropy
(Btu/lbmole-F)
27
Heat Flow
28
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
200.0*
200.0
(psia)
1515
1515
(lbmole/hr) (lb/hr)
1965 2.357e+004
26.45
1965 2.357e+004
26.45
(Btu/hr)
-4.796e+006
-4.796e+006
(barrel/day)
* 3.181e+006
3.181e+006
29
PROPERTIES
30 31
Overall
Vapour Phase
32
Molecular Weight
33
Molar Density
34
Mass Density
35
Act. Volume Flow
36
Mass Enthalpy
(Btu/lb)
-203.5
-203.5
37
Mass Entropy
(Btu/lb-F)
2.205
2.205
38
Heat Capacity
39
Mass Heat Capacity
40
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
41
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
42
HHV Mass Basis (Std)
43
CO2 Loading
44
CO2 App ML Con
45
CO2 App WT Con
46
LHV Mass Basis (Std)
47 48
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
11.99
11.99
0.2080
0.2080
2.494 4.038e+004
2.494 4.038e+004
7.433
7.433
0.6198
0.6198
8142
8142
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7066
7066
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
49
Phase Fraction [Act. Vol. Basis]
1.000
1.000
50
Mass Exergy
(Btu/lb)
420.5
---
51
Partial Pressure of CO2
(psia)
9.198
---
52
Cost Based on Flow
(Cost/s)
0.0000
0.0000
53
Act. Gas Flow
54
Avg. Liq. Density
55
(ACFM)
157.5
157.5
(lbmole/ft3)
1.945
1.945
Specific Heat
(Btu/lbmole-F)
7.433
7.433
56
Std. Gas Flow
(MMSCFD)
17.86
17.86
57
Std. Ideal Liq. Mass Density
(lb/ft3)
23.33
23.33
58
Act. Liq. Flow
(USGPS)
---
---
59
Z Factor
1.029
1.029
60
Watson K
11.64
11.64
61
User Property
---
---
62
Partial Pressure of H2S
63
Cp/(Cp - R)
64
Cp/Cv
65
Heat of Vap.
66
Kinematic Viscosity
67
Liq. Mass Density (Std. Cond)
68
Liq. Vol. Flow (Std. Cond)
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.365
1.365
1.430
1.430
5226
---
0.3585
0.3585
3.167e-002
3.167e-002
3.181e+006
3.181e+006
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 160 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 55 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Liquid Fraction
13
Molar Volume
14
Mass Heat of Vap.
15
Phase Fraction [Molar Basis]
16
Surface Tension
17
Thermal Conductivity
18
Viscosity
19
Cv (Semi-Ideal)
20
Mass Cv (Semi-Ideal)
21
Cv
22
Mass Cv
23
Cv (Ent. Method)
24
Mass Cv (Ent. Method)
25
Cp/Cv (Ent. Method)
26
Reid VP at 37.8 C
27
True VP at 37.8 C
28
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
29
Viscosity Index
Vapour Phase 0.0000
0.0000
(ft3/lbmole)
4.808
4.808
(Btu/lb)
435.8
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
6.036e-002
6.036e-002
1.433e-002
1.433e-002
5.447
5.447
0.4542
0.4542
5.199
5.199
0.4335
0.4335
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.181e+006 ---
3.181e+006 ---
30
COMPOSITION
31 32
Overall Phase
33 34
COMPONENTS
35
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
36
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
37
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
38
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
39
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
40
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
42
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
43
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
45
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
46
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
49
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
51
23565.9660
Vapour Phase
52 53
COMPONENTS
54
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
55
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
56
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
57
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
58
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
59
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
61
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
62
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
64
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
65
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
68
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 161 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 55 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
Fluid Package:
Total
1964.9702
1.0000
Phase Fraction
23565.9660
14
1.0000
1.000
4317.6702
1.0000
K VALUE
15 16
COMPONENTS
MIXED
LIGHT
HEAVY
17
CO
---
---
---
18
H2O
---
---
---
19
Oxygen
---
---
---
20
Methane
---
---
---
---
---
---
21
H2S
22
Hydrogen
---
---
---
23
Ethane
---
---
---
24
Propane
---
---
---
25
CO2
---
---
---
26
Nitrogen
---
---
---
---
---
---
27
Air
28
Mercury
---
---
---
29
MEAmine
---
---
---
30
Ammonia
---
---
---
31
UNIT OPERATIONS
32 33 34
FEED TO
PRODUCT FROM
Compressor:
K-102
Cooler:
LOGICAL CONNECTION E-104
35
UTILITIES
36 37
( No utilities reference this stream )
38
PROCESS UTILITY
39 40 41
DYNAMICS
42 43
Pressure Specification
(Inactive):
44
Flow Specification
(Inactive) Molar:
1515 psia 1965 lbmole/hrMass:
45
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
46 47
NOTES
48 49 50
Description
51 52 53
Material Stream: 56
54 55 56
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
57 58
Overall
Vapour Phase
59
Vapour / Phase Fraction
60
Temperature:
61
Pressure:
62
Molar Flow
63
Mass Flow
64
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
65
Molar Enthalpy
(Btu/lbmole)
169.3
169.3
66
Molar Entropy
(Btu/lbmole-F)
67
Heat Flow
68
Liq Vol Flow @Std Cond
69
Aspen Technology Inc. Licensed to: LEGENDS
1.0000
1.0000
(F)
539.9
539.9
(psia)
4940*
4940
(lbmole/hr) (lb/hr)
1965 2.357e+004
27.13
1965 2.357e+004
27.13
(Btu/hr)
3.327e+005
3.327e+005
(barrel/day)
* 3.181e+006
3.181e+006
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 162 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 56 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Molecular Weight
13
Molar Density
14
Mass Density
15
Act. Volume Flow
16
Mass Enthalpy
(Btu/lb)
14.12
14.12
17
Mass Entropy
(Btu/lb-F)
2.262
2.262
18
Heat Capacity
19
Mass Heat Capacity
20
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
21
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
22
HHV Mass Basis (Std)
23
CO2 Loading
24
CO2 App ML Con
25
CO2 App WT Con
26
LHV Mass Basis (Std)
27 28
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
11.99
11.99
0.4152
0.4152
4.980 2.023e+004
4.980 2.023e+004
7.770
7.770
0.6479
0.6479
8142
8142
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7066
7066
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
29
Phase Fraction [Act. Vol. Basis]
1.000
1.000
30
Mass Exergy
(Btu/lb)
607.6
---
31
Partial Pressure of CO2
(psia)
29.99
---
32
Cost Based on Flow
(Cost/s)
0.0000
0.0000
33
Act. Gas Flow
34
Avg. Liq. Density
35
(ACFM)
78.87
78.87
(lbmole/ft3)
1.945
1.945
Specific Heat
(Btu/lbmole-F)
7.770
7.770
36
Std. Gas Flow
(MMSCFD)
17.86
17.86
37
Std. Ideal Liq. Mass Density
(lb/ft3)
23.33
23.33
38
Act. Liq. Flow
(USGPS)
---
---
39
Z Factor
1.109
1.109
40
Watson K
11.64
11.64
41
User Property
---
---
42
Partial Pressure of H2S
43
Cp/(Cp - R)
44
Cp/Cv
45
Heat of Vap.
46
Kinematic Viscosity
47
Liq. Mass Density (Std. Cond)
48
Liq. Vol. Flow (Std. Cond)
49
Liquid Fraction
50
Molar Volume
51
Mass Heat of Vap.
52
Phase Fraction [Molar Basis]
53
Surface Tension
54
Thermal Conductivity
55
Viscosity
56
Cv (Semi-Ideal)
57
Mass Cv (Semi-Ideal)
58
Cv
59
Mass Cv
60
Cv (Ent. Method)
61
Mass Cv (Ent. Method)
62
Cp/Cv (Ent. Method)
63
Reid VP at 37.8 C
(psia)
64
True VP at 37.8 C
(psia)
---
65
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
66
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.343
1.343
1.394
1.394
5157
---
0.2638
0.2638
3.167e-002
3.167e-002
3.181e+006
3.181e+006
0.0000
0.0000
(ft3/lbmole)
2.408
2.408
(Btu/lb)
430.0
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
---
8.469e-002
8.469e-002
2.105e-002
2.105e-002
5.784
5.784
0.4823
0.4823
5.576
5.576
0.4649
0.4649
5.632
5.632
0.4696
0.4696
1.380
1.380
---
-----
3.181e+006 ---
3.181e+006 ---
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 163 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 56 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
16
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
17
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
18
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
21
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
24
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
30
23565.9660
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
35
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
36
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
37
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
40
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
43
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
49
K VALUE
50 51
23565.9660
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 164 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 56 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Cooler:
E-105
Compressor:
13
LOGICAL CONNECTION K-102
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 4940 psia
1965 lbmole/hrMass:
23
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 57
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
4318
4308
43
Molar Enthalpy
(Btu/lbmole)
-3348
-2899
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Liquid Phase
Aqueous Phase
0.9962
0.9962
0.0000
0.0037
(F)
95.00*
95.00
95.00
95.00
(psia)
4940
4940
4940
1965
1958
(lbmole/hr) (lb/hr)
2.357e+004
22.45
2.343e+004
22.48
6.076e-002 3.135 0.2197 -1.047e+005 7.744
(Btu/hr)
-6.579e+006
-5.674e+006
-6361
(barrel/day)
* 3.181e+006
3.169e+006
0.2259
47
4940 7.345 132.4 9.093 -1.224e+005 13.36 -8.988e+005 8.942
PROPERTIES
48 49
Overall
Vapour Phase
Liquid Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-279.2
-242.2
-2029
-6787
55
Mass Entropy
(Btu/lb-F)
1.872
1.878
0.1501
0.7410
56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.505e+004
4.659e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.794e+004
5.173e+005
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
(lbmole/ft3)
63
CO2 App WT Con
(lbmol/lb)
64
LHV Mass Basis (Std)
(Btu/lb)
65
Phase Fraction [Vol. Basis]
0.9978
0.9978
5.088e-005
2.106e-003
66
Phase Fraction [Mass Basis]
0.9942
0.9942
1.330e-004
5.619e-003
67
Phase Fraction [Act. Vol. Basis]
0.9992
0.9992
1.995e-005
7.839e-004
68
Mass Exergy
523.9
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
11.99
11.97
51.60
18.03
0.7328
0.7306
1.136
3.495
8.789
8.745
58.61
63.00
0.2286
8.985
1.146e+004
1.145e+004
7.990
7.951
36.26
18.39
0.6663
0.6642
0.7028
1.020 39.33 1.765e+004
8142
8183
1.003e+004
---
---
1.465e-002
---
---
1.286e-002
1.261e-003
---
---
2.195e-004
2.002e-005
7066
7106
9030
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
979.1 20.21
2.182
---
Page 165 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 57 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Liquid Phase
Aqueous Phase
(psia)
30.10
---
---
---
(Cost/s)
0.0000
0.0000
0.0000
0.0000
(ACFM)
44.65
44.65
---
---
(lbmole/ft3)
1.945
1.942
1.182
3.453
Specific Heat
(Btu/lbmole-F)
7.990
7.951
Std. Gas Flow
(MMSCFD)
17.86
17.79
23.33
23.25
(lb/ft3) (USGPS)
4.479e-003
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
(Btu/lb)
61.00 1.111e-004
18.39 6.677e-002 62.25 4.367e-003
---
1.136
0.7305
0.2375
11.64
11.64
9.183
7.895
---
---
---
---
0.0000
---
---
---
1.331
1.333
1.058
1.121
1.503
1.510
1.717
1.147
5157
---
---
---
---
0.1099
8.555
0.7502
3.167e-002
3.160e-002
59.32
63.31
3.181e+006
3.169e+006
0.2259
8.942
3.769e-003 (ft3/lbmole)
---
36.26 5.523e-004
1.365
0.0000
1.000
1.000
1.369
0.8803
0.2861
430.0
---
---
---
0.9962
0.9962
0.0000
0.0037
(dyne/cm)
70.27
46.22
70.27
(Btu/hr-ft-F)
---
6.120e-002
0.1213
0.3603
---
1.539e-002
8.032
0.7571
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
6.005
5.965
34.27
16.41
0.5007
0.4983
0.6643
0.9101
5.316
5.267
21.12
16.04
0.4432
0.4400
0.4094
0.8898
---
5.250
24.58
15.89
---
0.4387
0.4764
0.8814
---
1.514
1.475
---
---
159.7
---
---
3.169e+006 ---
3.169e+006 ---
48
1.158 2.883e+004
4820
4516
0.2259
8.942
---
---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9962
LIQUID VOLUME FRACTION
54
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
55
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
56
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
57
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
60
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
63
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
1964.9702
1.0000
1.0000
4317.6702
69
Aspen Technology Inc. Licensed to: LEGENDS
23565.9660
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 166 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 57 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9962 LIQUID VOLUME FRACTION
15
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
16
H2O
1.9239
0.0010
34.6590
0.0015
2.3780
0.0006
17
Oxygen
130.6342
0.0667
4180.2936
0.1784
251.5967
0.0584
18
Methane
78.7297
0.0402
1263.0531
0.0539
288.8662
0.0670
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1200.5187
0.6133
2420.2458
0.1033
2372.2189
0.5506
21
Ethane
23.3586
0.0119
702.3901
0.0300
135.2177
0.0314
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
11.9284
0.0061
524.9657
0.0224
43.5531
0.0101
24
Nitrogen
510.1305
0.2606
14290.2853
0.6099
1213.4521
0.2817
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1507
0.0001
9.2079
0.0004
0.6200
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1957.5642
1.0000
1.0000
4308.3572
1.0000
23430.4075
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
3.092e-005 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0078
0.1291
0.1413
0.0451
0.0097
0.0441
36
Oxygen
0.0008
0.0129
0.0250
0.0080
0.0015
0.0069
37
Methane
0.0006
0.0092
0.0090
0.0029
0.0021
0.0094
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0019
0.0318
0.0039
0.0012
0.0038
0.0174
40
Ethane
0.0007
0.0107
0.0196
0.0063
0.0038
0.0172
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0007
0.0113
0.0303
0.0097
0.0025
0.0114
43
Nitrogen
0.0013
0.0222
0.0378
0.0120
0.0032
0.0146
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0470
0.7727
2.8680
0.9148
0.1931
0.8790
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0608
1.0000
3.1349
1.0000
0.2197
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
3.738e-003 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
7.3351
0.9986
132.1420
0.9979
9.0664
0.9970
55
Oxygen
0.0004
0.0001
0.0134
0.0001
0.0008
0.0001
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0020
0.0003
0.0041
0.0000
0.0040
0.0004
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0027
0.0004
0.1167
0.0009
0.0097
0.0011
62
Nitrogen
0.0050
0.0007
0.1394
0.0011
0.0118
0.0013
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0001
0.0000
0.0080
0.0001
0.0005
0.0001
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
7.3453
1.0000
132.4236
1.0000
9.0933
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 167 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 57 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
CO
13
H2O
LIGHT
HEAVY
928.8
13.01
9.912e-004
14
Oxygen
410.8
5.180
15
Methane
530.4
4.356
16
H2S
2224
7.612e-003
9.842e-004 1167 5.141e+005
---
---
---
Hydrogen
1145
19.30
2213
18
Ethane
135.5
1.112
19
Propane
---
---
---
20
CO2
13.52
0.5381
16.89
21
Nitrogen
305.2
11.74
384.8
---
---
---
---
---
17
22
Air
23
Mercury
24
MEAmine
25
Ammonia
1.211e-002
4.312
---
---
UNIT OPERATIONS
27 28 29
---
9.965e-005
---
26
3.122e+007
FEED TO
PRODUCT FROM
Mixer:
MIX-102 Cooler:
LOGICAL CONNECTION E-105
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
4940 psia 1965 lbmole/hrMass:
40
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 58
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
7276
7246
60
Molar Enthalpy
(Btu/lbmole)
-5210
-4829
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Liquid Phase
0.9943
0.9943
0.0057
(F)
94.55
94.55
94.55
(psia)
4820
4820
4820
3256
3238
18.71
(lbmole/hr) (lb/hr)
4.521e+004
23.85
4.488e+004
23.89
(Btu/hr)
-1.697e+007
-1.563e+007
(barrel/day)
* 5.270e+006
5.240e+006
64
328.2 30.09 -7.123e+004 16.91 -1.332e+006 29.42
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Vapour Phase
Liquid Phase
13.88
13.86
17.55
0.7417
0.7386
2.706
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 168 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 58 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-375.2
-348.3
-4059
15
Mass Entropy
(Btu/lb-F)
1.718
1.723
0.9639
16
Heat Capacity
8.581
8.522
18.78
17
Mass Heat Capacity
0.6180
0.6147
18
LHV Molar Basis (Std)
(Btu/lbmole)
8.968e+004
8.976e+004
7.589e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
1.030e+005
1.030e+005
9.836e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
10.30 1.877e+004
10.24 1.874e+004
47.48 29.55
1.070
7418
7431
5606
---
---
1.455
(lbmole/ft3)
---
---
3.955e-003
(lbmol/lb)
---
---
8.331e-005
(Btu/lb)
6459
6475
Phase Fraction [Vol. Basis]
0.9959
0.9959
4.135e-003
26
Phase Fraction [Mass Basis]
0.9927
0.9927
7.260e-003
27
Phase Fraction [Act. Vol. Basis]
0.9984
0.9984
1.575e-003
28
Mass Exergy
(Btu/lb)
445.7
---
29
Partial Pressure of CO2
(psia)
34.78
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
4325
---
(ACFM)
73.05
73.05
---
(lbmole/ft3)
1.913
1.910
2.658
Specific Heat
(Btu/lbmole-F)
8.581
8.522
18.78
Std. Gas Flow
(MMSCFD)
29.60
29.43
0.1700
26.56
26.48
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
1.437e-002
(Btu/lb)
46.64 1.437e-002
---
1.097
0.2995
11.10
11.09
12.17
---
---
---
0.0000
---
---
1.301
1.304
1.118
1.543
1.553
1.275
4826
---
---
---
0.1039
0.3464
3.667e-002
3.661e-002
47.69
5.270e+006
5.240e+006
29.42
5.745e-003 (ft3/lbmole)
---
1.348
0.0000
1.000
1.354
0.3696
347.6
---
---
0.9943
0.9943
0.0057
(dyne/cm)
44.24
(Btu/hr-ft-F)
---
5.552e-002
0.3014
---
1.704e-002
0.2634
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
44.24
6.595
6.536
16.79
0.4750
0.4715
0.9570
5.562
5.489
14.73
0.4006
0.3959
0.8393
6.093
5.459
15.20
0.4389
0.3938
0.8662
1.408
1.561
1.235
---
---
239.1
---
---
5.240e+006 ---
5.240e+006 ---
4505 29.42 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 169 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 58 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9943
LIQUID VOLUME FRACTION
15
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
16
H2O
9.2845
0.0029
167.2607
0.0037
11.4759
0.0016
17
Oxygen
311.9685
0.0958
9982.9913
0.2208
600.8400
0.0826
18
Methane
186.2348
0.0572
2987.7458
0.0661
683.3116
0.0939
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1675.5884
0.5146
3377.9863
0.0747
3310.9542
0.4550
21
Ethane
49.3871
0.0152
1485.0654
0.0328
285.8912
0.0393
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
23.3883
0.0072
1029.3111
0.0228
85.3954
0.0117
24
Nitrogen
831.2466
0.2553
23285.7121
0.5150
1977.2941
0.2718
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1983
0.0001
12.1117
0.0003
0.8155
0.0001
28
Ammonia
168.5154
0.0518
2869.8180
0.0635
318.9647
0.0438
29
Total
3256.2735
1.0000
45210.9342
1.0000
7276.0502
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9943 LIQUID VOLUME FRACTION
34
CO
0.4617
0.0001
12.9315
0.0003
1.1077
0.0002
35
H2O
1.0154
0.0003
18.2934
0.0004
1.2551
0.0002
36
Oxygen
311.9482
0.0964
9982.3432
0.2224
600.8010
0.0829
37
Methane
186.2335
0.0575
2987.7259
0.0666
683.3071
0.0943
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1675.5476
0.5175
3377.9041
0.0753
3310.8736
0.4569
40
Ethane
49.3870
0.0153
1485.0617
0.0331
285.8904
0.0395
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
23.3609
0.0072
1028.1076
0.0229
85.2956
0.0118
43
Nitrogen
831.2237
0.2567
23285.0686
0.5188
1977.2395
0.2729
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.1795
0.0001
10.9640
0.0002
0.7382
0.0001
47
Ammonia
158.2086
0.0489
2694.2933
0.0600
299.4560
0.0413
48
Total
3237.5662
1.0000
44882.6933
1.0000
7245.9642
1.0000
49
Liquid Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
5.745e-003 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0003
0.0000
0.0000
0.0000
54
H2O
8.2690
0.4420
148.9673
0.4538
10.2208
0.3397
55
Oxygen
0.0203
0.0011
0.6481
0.0020
0.0390
0.0013
56
Methane
0.0012
0.0001
0.0198
0.0001
0.0045
0.0002
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0408
0.0022
0.0822
0.0003
0.0806
0.0027
59
Ethane
0.0001
0.0000
0.0038
0.0000
0.0007
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0273
0.0015
1.2035
0.0037
0.0998
0.0033
62
Nitrogen
0.0230
0.0012
0.6435
0.0020
0.0546
0.0018
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0188
0.0010
1.1476
0.0035
0.0773
0.0026
66
Ammonia
10.3068
0.5509
175.5248
0.5347
19.5086
0.6484
67
Total
18.7073
1.0000
328.2408
1.0000
30.0861
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 170 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 58 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
13
H2O
14
Oxygen
89.00
89.00
---
15
Methane
871.8
871.8
---
---
---
---
16
257.1
257.1
7.096e-004
H2S
---
7.096e-004
---
17
Hydrogen
237.4
237.4
---
18
Ethane
2286
2286
---
19
Propane
---
---
---
20
CO2
4.936
4.936
---
21
Nitrogen
209.1
209.1
---
---
---
---
---
---
---
22
Air
23
Mercury
24
MEAmine
5.520e-002
5.520e-002
---
25
Ammonia
8.870e-002
8.870e-002
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Component Splitter:
D-12
LOGICAL CONNECTION
Mixer:
MIX-102
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
4820 psia 3256 lbmole/hrMass:
40
4.521e+004 lb/hrStd Ideal Liq Volume:
7276 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 59
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
6957
6950
60
Molar Enthalpy
(Btu/lbmole)
-4239
-4012
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Aqueous Phase
0.9981
0.9981
0.0019
(F)
97.00*
97.00
97.00
(psia)
4940*
4940
4940
3088
3082
5.921
(lbmole/hr) (lb/hr)
4.234e+004
23.32
4.223e+004
23.34
(Btu/hr)
-1.309e+007
-1.236e+007
(barrel/day)
* 4.999e+006
4.989e+006
64
106.8 7.331 -1.223e+005 13.43 -7.242e+005 7.208
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Vapour Phase
Aqueous Phase
13.71
13.70
18.03
0.7351
0.7340
3.492
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 171 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 59 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-309.1
-292.7
-6784
15
Mass Entropy
(Btu/lb-F)
1.701
1.703
0.7447
16
Heat Capacity
8.210
8.190
18.39
17
Mass Heat Capacity
0.5987
0.5976
1.020
18
LHV Molar Basis (Std)
(Btu/lbmole)
8.714e+004
8.731e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
9.974e+004
9.989e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
24
LHV Mass Basis (Std)
(Btu/lb)
25
Phase Fraction [Vol. Basis]
0.9989
0.9989
1.054e-003
26
Phase Fraction [Mass Basis]
0.9975
0.9975
2.521e-003
27
Phase Fraction [Act. Vol. Basis]
0.9996
0.9996
4.037e-004
28
Mass Exergy
(Btu/lb)
457.1
---
29
Partial Pressure of CO2
(psia)
37.48
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
10.08 1.796e+004
10.06 1.795e+004
62.96 7.248
33.42 1.764e+004
7273
7289
---
---
978.6
---
---
1.467e-003
---
---
2.331e-005
6355
6371
37.00
1.853
---
(ACFM)
69.98
69.98
---
(lbmole/ft3)
1.897
1.896
3.453
Specific Heat
(Btu/lbmole-F)
8.210
8.190
Std. Gas Flow
(MMSCFD)
28.07
28.01
26.02
25.98
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
3.523e-003
(Btu/lb)
62.25 3.523e-003
---
1.127
0.2368
10.85
10.85
7.791
---
---
---
0.0000
---
---
1.319
1.320
1.121
1.521
1.524
1.147
5131
---
---
---
0.1045
0.7357
3.621e-002
3.619e-002
63.31
4.999e+006
4.989e+006
7.208
1.917e-003 (ft3/lbmole)
---
18.39 5.382e-002
1.360
0.0000
1.000
1.362
0.2864
374.2
---
---
0.9981
0.9981
0.0019
(dyne/cm)
70.07
(Btu/hr-ft-F)
---
5.611e-002
0.3611
---
1.684e-002
0.7420
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
70.07
6.224
6.204
16.41
0.4539
0.4527
0.9099
5.399
5.375
16.04
0.3937
0.3922
0.8894
5.732
5.359
15.88
0.4180
0.3911
0.8806
1.432
1.528
1.158
---
---
---
---
---
4560
4.989e+006 ---
4.989e+006 ---
7.208 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 172 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 59 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9981
LIQUID VOLUME FRACTION
15
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
16
H2O
9.2845
0.0030
167.2607
0.0040
11.4759
0.0016
17
Oxygen
311.9685
0.1010
9982.9913
0.2358
600.8400
0.0864
18
Methane
186.2348
0.0603
2987.7458
0.0706
683.3116
0.0982
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1675.5884
0.5427
3377.9863
0.0798
3310.9542
0.4759
21
Ethane
49.3871
0.0160
1485.0654
0.0351
285.8912
0.0411
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
23.3883
0.0076
1029.3111
0.0243
85.3954
0.0123
24
Nitrogen
831.2466
0.2692
23285.7121
0.5500
1977.2941
0.2842
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1983
0.0001
12.1117
0.0003
0.8155
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
3087.7581
1.0000
1.0000
6957.0856
1.0000
42341.1161
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9981 LIQUID VOLUME FRACTION
34
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
35
H2O
3.3724
0.0011
60.7549
0.0014
4.1685
0.0006
36
Oxygen
311.9680
0.1012
9982.9747
0.2364
600.8390
0.0865
37
Methane
186.2348
0.0604
2987.7457
0.0707
683.3116
0.0983
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1675.5869
0.5437
3377.9832
0.0800
3310.9512
0.4764
40
Ethane
49.3871
0.0160
1485.0654
0.0352
285.8912
0.0411
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
23.3858
0.0076
1029.2016
0.0244
85.3863
0.0123
43
Nitrogen
831.2426
0.2697
23285.5981
0.5513
1977.2844
0.2845
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.1982
0.0001
12.1075
0.0003
0.8152
0.0001
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
3081.8374
1.0000
1.0000
6949.7550
1.0000
49
42234.3631
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.917e-003 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
5.9120
0.9985
106.5058
0.9977
7.3075
0.9969
55
Oxygen
0.0005
0.0001
0.0166
0.0002
0.0010
0.0001
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0015
0.0003
0.0031
0.0000
0.0030
0.0004
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0025
0.0004
0.1095
0.0010
0.0091
0.0012
62
Nitrogen
0.0041
0.0007
0.1140
0.0011
0.0097
0.0013
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0001
0.0000
0.0041
0.0000
0.0003
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
5.9207
1.0000
106.7531
1.0000
7.3305
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 173 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 59 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
CO
13
H2O Oxygen
15
Methane
1154
Hydrogen
2188
---
1.096e-003
---
4.979e+005
H2S
17
HEAVY ---
1.096e-003
14
16
LIGHT 2188
1154
---
4.979e+005
---
---
---
2117
---
2117
18
Ethane
19
Propane
---
---
---
20
CO2
18.06
---
18.06
21
Nitrogen
392.4
---
392.4
---
---
---
22
3.073e+007
Air
---
3.073e+007
23
Mercury
---
---
---
24
MEAmine
5.662
---
5.662
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Valve:
VLV-101 Component Splitter:
30
LOGICAL CONNECTION D-12
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 4940 psia
3088 lbmole/hrMass:
40
4.234e+004 lb/hrStd Ideal Liq Volume:
6957 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 60
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
333.5
333.5
(psia)
4940*
4940
168.5
168.5
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
2870
2870
319.0
319.0
-2.301e+004 27.30 -3.877e+006 320.9*
(barrel/day)
64
-2.301e+004 27.30 -3.877e+006 320.9
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Liquid Phase 17.03
17.03
1.216
1.216
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 174 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 60 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Density
13
Act. Volume Flow
14
(lb/ft3)
Liquid Phase 20.70
20.70
(barrel/day)
592.6
592.6
Mass Enthalpy
(Btu/lb)
-1351
-1351
15
Mass Entropy
(Btu/lb-F)
1.603
1.603
16
Heat Capacity
26.30
26.30
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
1.362e+005
1.362e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
1.627e+005
1.627e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.544
9551
1.544
9551
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
7998
7998
Phase Fraction [Vol. Basis]
0.0000
1.000
26
Phase Fraction [Mass Basis]
0.0000
1.000
27
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
28
Mass Exergy
(Btu/lb)
227.3
---
29
Partial Pressure of CO2
(psia)
0.0000
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
2.258
2.258
Specific Heat
(Btu/lbmole-F)
26.30
26.30
Std. Gas Flow
(MMSCFD)
1.532
1.532
(lb/ft3)
38.46
38.46
(USGPS)
0.2881
0.2881
0.4774
0.4774
12.24
12.24
---
---
(psia)
(Btu/lbmole)
0.0000
---
1.082
1.082
2.648
2.648
---
---
(cSt)
0.1228
0.1228
(lb/ft3)
38.22
38.22
320.9
320.9
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.8227
0.8227
-827.2
---
0.0000
1.0000
(dyne/cm)
---
---
(Btu/hr-ft-F)
0.1332
0.1332
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
4.071e-002
4.071e-002
24.31
24.31
1.427
1.427
9.929
9.929
0.5830
0.5830
17.77
17.77
1.043
1.043
1.480
1.480
(psia)
210.5
210.5
(psia)
210.5
210.5
320.9
320.9
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 175 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 60 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
29
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
48
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
0.0000
0.0000
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 176 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 60 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Cooler:
E-106
LOGICAL CONNECTION
Component Splitter:
13
D-12
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 4940 psia
168.5 lbmole/hrMass:
23
2870 lb/hr Std Ideal Liq Volume:
319.0 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 61
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
6957
6950
43
Molar Enthalpy
(Btu/lbmole)
-4239
-4011
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Aqueous Phase
0.9981
0.9981
0.0019
(F)
96.93
96.93
96.93
(psia)
4820*
4820
4820
3088
3082
5.951
(lbmole/hr) (lb/hr)
4.234e+004
23.38
4.223e+004
23.40
(Btu/hr)
-1.309e+007
-1.236e+007
(barrel/day)
* 4.999e+006
4.989e+006
47
107.3 7.367 -1.223e+005 13.43 -7.279e+005 7.244
PROPERTIES
48 49
Overall
Vapour Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-309.1
-292.7
-6785
55
Mass Entropy
(Btu/lb-F)
1.705
1.707
0.7447
56
Heat Capacity
8.199
8.180
18.40
57
Mass Heat Capacity
0.5980
0.5969
1.020
58
LHV Molar Basis (Std)
(Btu/lbmole)
8.714e+004
8.731e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
9.974e+004
9.989e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
(lbmole/ft3)
63
CO2 App WT Con
(lbmol/lb)
64
LHV Mass Basis (Std)
(Btu/lb)
65
Phase Fraction [Vol. Basis]
0.9989
0.9989
1.059e-003
66
Phase Fraction [Mass Basis]
0.9975
0.9975
2.534e-003
67
Phase Fraction [Act. Vol. Basis]
0.9996
0.9996
3.977e-004
68
Mass Exergy
455.0
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
13.71
13.70
18.03
0.7204
0.7193
3.491
9.879
9.858
62.94
1.832e+004
1.831e+004
7.286
33.04 1.764e+004
7273
7289
---
---
978.6
---
---
1.454e-003
---
---
2.309e-005
6355
6371
35.37
1.832
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 177 of 336 * Specified by user.
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LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 61 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Aqueous Phase
(psia)
36.57
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
71.41
71.41
---
(lbmole/ft3)
1.897
1.896
3.453
Specific Heat
(Btu/lbmole-F)
8.199
8.180
Std. Gas Flow
(MMSCFD)
28.07
28.01
26.02
25.98
(lb/ft3) (USGPS)
3.542e-003
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
(Btu/lb)
62.25 3.542e-003
---
1.122
0.2311
10.85
10.85
7.792
---
---
---
0.0000
---
---
1.320
1.321
1.121
1.520
1.523
1.147
5139
---
---
---
0.1058
0.7363
3.621e-002
3.619e-002
63.31
4.999e+006
4.989e+006
7.244
1.927e-003 (ft3/lbmole)
---
18.40 5.409e-002
1.388
0.0000
1.000
1.390
0.2864
374.7
---
---
0.9981
0.9981
0.0019
(dyne/cm)
70.08
(Btu/hr-ft-F)
---
5.579e-002
0.3611
---
1.671e-002
0.7424
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
70.08
6.214
6.194
16.41
0.4531
0.4520
0.9101
5.395
5.370
16.04
0.3934
0.3919
0.8895
5.714
5.342
15.84
0.4167
0.3898
0.8786
1.435
1.531
1.161
---
---
---
---
---
4446
4.989e+006 ---
4.989e+006 ---
48
7.244 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9981
LIQUID VOLUME FRACTION
54
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
55
H2O
9.2845
0.0030
167.2607
0.0040
11.4759
0.0016
56
Oxygen
311.9685
0.1010
9982.9913
0.2358
600.8400
0.0864
57
Methane
186.2348
0.0603
2987.7458
0.0706
683.3116
0.0982
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1675.5884
0.5427
3377.9863
0.0798
3310.9542
0.4759
60
Ethane
49.3871
0.0160
1485.0654
0.0351
285.8912
0.0411
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
23.3883
0.0076
1029.3111
0.0243
85.3954
0.0123
63
Nitrogen
831.2466
0.2692
23285.7121
0.5500
1977.2941
0.2842
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.1983
0.0001
12.1117
0.0003
0.8155
0.0001
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
3087.7581
1.0000
1.0000
6957.0856
69
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42341.1161
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 178 of 336 * Specified by user.
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LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 61 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9981 LIQUID VOLUME FRACTION
15
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
16
H2O
3.3425
0.0011
60.2148
0.0014
4.1314
0.0006
17
Oxygen
311.9680
0.1012
9982.9749
0.2364
600.8390
0.0865
18
Methane
186.2348
0.0604
2987.7457
0.0707
683.3116
0.0983
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1675.5869
0.5437
3377.9833
0.0800
3310.9512
0.4764
21
Ethane
49.3871
0.0160
1485.0654
0.0352
285.8912
0.0411
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
23.3858
0.0076
1029.2020
0.0244
85.3864
0.0123
24
Nitrogen
831.2426
0.2697
23285.5995
0.5513
1977.2845
0.2845
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
3081.8075
1.0000
1.0000
6949.7182
1.0000
30
42233.8250
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.927e-003 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
5.9420
0.9986
107.0458
0.9977
7.3445
0.9969
36
Oxygen
0.0005
0.0001
0.0164
0.0002
0.0010
0.0001
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0015
0.0003
0.0030
0.0000
0.0029
0.0004
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0025
0.0004
0.1090
0.0010
0.0090
0.0012
43
Nitrogen
0.0040
0.0007
0.1126
0.0010
0.0096
0.0013
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0001
0.0000
0.0043
0.0000
0.0003
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
5.9506
1.0000
107.2912
1.0000
7.3674
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
52
CO
53
H2O
54
Oxygen
55
Methane
56
H2S
57
Hydrogen
LIGHT 2230 1.086e-003 1174 5.063e+005
HEAVY ---------
2230 1.086e-003 1174 5.063e+005
---
---
---
2168
---
2168
58
Ethane
59
Propane
---
---
---
60
CO2
18.22
---
18.22
61
Nitrogen
399.4
---
399.4
---
---
---
62
Air
3.104e+007
---
3.104e+007
63
Mercury
---
---
---
64
MEAmine
5.463
---
5.463
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 179 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 61 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO Separator:
PRODUCT FROM
LOGICAL CONNECTION
S-2 SEPARADOR SECUNDARIOValve: CARGA
VLV-101
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 4820 psia
3088 lbmole/hrMass:
23
4.234e+004 lb/hrStd Ideal Liq Volume:
6957 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 62
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.0000
0.0000
1.0000
(F)
96.93
96.93
96.93
(psia)
4820
4820
4820
5.951
0.0000
5.951
107.3
0.0000
107.3
7.367
0.0000
(lbmole/hr) (lb/hr)
(Btu/hr)
-1.223e+005 13.43 -7.279e+005 7.244*
(barrel/day)
47
-4011 23.40 0.0000 0.0000
7.367 -1.223e+005 13.43 -7.279e+005 7.244
PROPERTIES
48 49
Overall
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Vapour Phase
Aqueous Phase
18.03
13.70
18.03
3.491
0.7193
3.491
62.94
9.858
62.94
(barrel/day)
7.286
0.0000
7.286
Mass Enthalpy
(Btu/lb)
-6785
-292.7
-6785
55
Mass Entropy
(Btu/lb-F)
0.7447
1.707
0.7447
56
Heat Capacity
57
Mass Heat Capacity
58
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F)
18.40
8.180
18.40
(Btu/lb-F)
1.020
0.5969
1.020
LHV Molar Basis (Std)
(Btu/lbmole)
33.04
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
(lbmole/ft3)
1.454e-003
63
CO2 App WT Con
(lbmol/lb)
2.309e-005
64
LHV Mass Basis (Std)
65
Phase Fraction [Vol. Basis]
66
(Btu/lb)
9.989e+004
978.6
7289
35.37
---
33.04 1.764e+004 978.6 35.37
---
1.454e-003
---
2.309e-005
1.832
6371
1.832
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
67
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
68
Mass Exergy
17.40
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
1.764e+004
8.731e+004
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
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1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 62 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Specific Heat
(Btu/lbmole-F)
17
Std. Gas Flow
(MMSCFD)
18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46 47
Vapour Phase
Aqueous Phase
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
3.453
1.896
3.453
(lb/ft3)
18.40 5.409e-002 62.25
(USGPS)
3.542e-003
8.180 0.0000 25.98 ---
18.40 5.409e-002 62.25 3.542e-003
---
1.122
0.2311
7.792
10.85
7.792
---
---
---
0.0000
---
---
1.121
1.321
1.121
1.147
1.523
1.147
---
---
---
(cSt)
0.7363
0.1058
0.7363
(lb/ft3)
63.31
(psia)
(Btu/lbmole)
(barrel/day) (ft3/lbmole) (Btu/lb)
3.619e-002
63.31
7.244
0.0000
1.000
0.0000
7.244 1.000
0.2864
1.390
0.2864
-781.3
---
---
0.0000
0.0000
1.0000
(dyne/cm)
70.08
(Btu/hr-ft-F)
0.3611
5.579e-002
0.3611
0.7424
1.671e-002
0.7424
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
70.08
16.41
6.194
16.41
0.9101
0.4520
0.9101
16.04
5.370
16.04
0.8895
0.3919
0.8895
15.84
5.342
15.84
0.8786
0.3898
0.8786
1.161
1.531
1.161
---
---
---
4446
---
4446
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
7.244
0.0000
7.244
Viscosity Index
-1.313
---
---
(Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
H2O
5.9420
0.9986
107.0458
0.9977
7.3445
0.9969
56
Oxygen
0.0005
0.0001
0.0164
0.0002
0.0010
0.0001
57
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0015
0.0003
0.0030
0.0000
0.0029
0.0004
60
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0025
0.0004
0.1090
0.0010
0.0090
0.0012
63
Nitrogen
0.0040
0.0007
0.1126
0.0010
0.0096
0.0013
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0001
0.0000
0.0043
0.0000
0.0003
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
5.9506
1.0000
107.2912
1.0000
7.3674
69
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Aspen HYSYS Version 8.8 (34.0.0.8909)
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LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 62 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0001
0.0000
0.0003
0.0000
0.0002
16
H2O
0.0000
0.0011
0.0000
0.0014
0.0000
0.0006
17
Oxygen
0.0000
0.1012
0.0000
0.2364
0.0000
0.0865
18
Methane
0.0000
0.0604
0.0000
0.0707
0.0000
0.0983
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.5437
0.0000
0.0800
0.0000
0.4764
21
Ethane
0.0000
0.0160
0.0000
0.0352
0.0000
0.0411
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0076
0.0000
0.0244
0.0000
0.0123
24
Nitrogen
0.0000
0.2697
0.0000
0.5513
0.0000
0.2845
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0001
0.0000
0.0003
0.0000
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
5.9420
0.9986
107.0458
0.9977
7.3445
0.9969
36
Oxygen
0.0005
0.0001
0.0164
0.0002
0.0010
0.0001
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0015
0.0003
0.0030
0.0000
0.0029
0.0004
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0025
0.0004
0.1090
0.0010
0.0090
0.0012
43
Nitrogen
0.0040
0.0007
0.1126
0.0010
0.0096
0.0013
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0001
0.0000
0.0043
0.0000
0.0003
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
5.9506
1.0000
107.2912
1.0000
7.3674
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
52
CO
53
H2O
54
Oxygen
55
Methane
56
H2S
57
Hydrogen
LIGHT 2230 1.086e-003 1174 5.063e+005
HEAVY ---------
2230 1.086e-003 1174 5.063e+005
---
---
---
2168
---
2168
58
Ethane
59
Propane
---
---
---
60
CO2
18.22
---
18.22
61
Nitrogen
399.4
---
399.4
---
---
---
62
Air
3.104e+007
---
3.104e+007
63
Mercury
---
---
---
64
MEAmine
5.463
---
5.463
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 182 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 62 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Separator:
LOGICAL CONNECTION
S-2 SEPARADOR SECUNDARIO CARGA
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
4820 psia 5.951 lbmole/hrMass:
23
107.3 lb/hr Std Ideal Liq Volume:
7.367 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 63
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
6950
6950
43
Molar Enthalpy
(Btu/lbmole)
-4011
-4011
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Aqueous Phase
1.0000
1.0000
0.0000
(F)
96.93
96.93
96.93
(psia)
4820
4820
4820
3082
3082
0.0000
(lbmole/hr) (lb/hr)
4.223e+004
23.40
4.223e+004
23.40
0.0000 0.0000 -1.223e+005 13.43
(Btu/hr)
-1.236e+007
-1.236e+007
0.0000
(barrel/day)
* 4.989e+006
4.989e+006
0.0000
47
PROPERTIES
48 49
Overall
Vapour Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-292.7
-292.7
-6785
55
Mass Entropy
(Btu/lb-F)
1.707
1.707
0.7447
56
Heat Capacity
8.180
8.180
18.40
57
Mass Heat Capacity
0.5969
0.5969
1.020
58
LHV Molar Basis (Std)
(Btu/lbmole)
8.731e+004
8.731e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
9.989e+004
9.989e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66 67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
13.70
18.03
0.7193
0.7193
3.491
9.858
9.858
1.831e+004
1.831e+004
62.94 0.0000
33.04 1.764e+004
7289
7289
978.6
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
6371
6371
1.832
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
455.7
---
---
Licensed to: LEGENDS
(Btu/lb)
13.70
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 183 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 63 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Aqueous Phase
(psia)
36.57
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
71.41
71.41
---
(lbmole/ft3)
1.896
1.896
3.453
Specific Heat
(Btu/lbmole-F)
8.180
8.180
18.40
Std. Gas Flow
(MMSCFD)
28.01
28.01
0.0000
(lb/ft3)
25.98
25.98
62.25
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.122
0.2311
10.85
10.85
7.792
---
---
---
0.0000
---
---
1.321
1.321
1.121
1.523
1.523
1.147
4625
---
---
0.1058
0.1058
0.7363
3.619e-002
3.619e-002
63.31
4.989e+006
4.989e+006
0.0000
0.0000
0.0000
1.000
1.390
1.390
0.2864
337.5
---
---
1.0000
1.0000
0.0000
---
---
70.08
5.579e-002
5.579e-002
0.3611
1.671e-002
1.671e-002
0.7424
6.194
6.194
16.41
0.4520
0.4520
0.9101
5.370
5.370
16.04
0.3919
0.3919
0.8895
5.342
5.342
15.84
0.3898
0.3898
0.8786
1.531
1.531
1.161
---
---
---
---
---
4446
4.989e+006 ---
4.989e+006 ---
48
0.0000 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
54
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
55
H2O
3.3425
0.0011
60.2148
0.0014
4.1314
0.0006
56
Oxygen
311.9680
0.1012
9982.9749
0.2364
600.8390
0.0865
57
Methane
186.2348
0.0604
2987.7457
0.0707
683.3116
0.0983
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1675.5869
0.5437
3377.9833
0.0800
3310.9512
0.4764
60
Ethane
49.3871
0.0160
1485.0654
0.0352
285.8912
0.0411
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
23.3858
0.0076
1029.2020
0.0244
85.3864
0.0123
63
Nitrogen
831.2426
0.2697
23285.5995
0.5513
1977.2845
0.2845
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
3081.8075
1.0000
1.0000
6949.7182
69
Aspen Technology Inc. Licensed to: LEGENDS
42233.8250
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 184 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 63 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
16
H2O
3.3425
0.0011
60.2148
0.0014
4.1314
0.0006
17
Oxygen
311.9680
0.1012
9982.9749
0.2364
600.8390
0.0865
18
Methane
186.2348
0.0604
2987.7457
0.0707
683.3116
0.0983
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1675.5869
0.5437
3377.9833
0.0800
3310.9512
0.4764
21
Ethane
49.3871
0.0160
1485.0654
0.0352
285.8912
0.0411
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
23.3858
0.0076
1029.2020
0.0244
85.3864
0.0123
24
Nitrogen
831.2426
0.2697
23285.5995
0.5513
1977.2845
0.2845
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
3081.8075
1.0000
1.0000
6949.7182
1.0000
30
42233.8250
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.9986
0.0000
0.9977
0.0000
0.9969
36
Oxygen
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0003
0.0000
0.0000
0.0000
0.0004
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0004
0.0000
0.0010
0.0000
0.0012
43
Nitrogen
0.0000
0.0007
0.0000
0.0010
0.0000
0.0013
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
52
CO
53
H2O
54
Oxygen
55
Methane
56
H2S
57
Hydrogen
LIGHT 2230 1.086e-003 1174 5.063e+005
HEAVY ---------
2230 1.086e-003 1174 5.063e+005
---
---
---
2168
---
2168
58
Ethane
59
Propane
---
---
---
60
CO2
18.22
---
18.22
61
Nitrogen
399.4
---
399.4
---
---
---
62
Air
3.104e+007
---
3.104e+007
63
Mercury
---
---
---
64
MEAmine
5.463
---
5.463
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 185 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 63 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Conversion Reactor:
T-3 CONVERTIDOR Separator:
13
LOGICAL CONNECTION
S-2 SEPARADOR SECUNDARIO CARGA
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
4820 psia 3082 lbmole/hrMass:
23
4.223e+004 lb/hrStd Ideal Liq Volume:
6950 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 64
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
44
Molar Entropy
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
652.0
652.0
652.0
(psia)
4820
4820
4820
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(Btu/lbmole)
-4658
-4944
-4658
(Btu/lbmole-F)
32.68
32.81
32.68
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
47
PROPERTIES
48 49
Overall
Vapour Phase
Liquid Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54 55 56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
1.017e+005
1.030e+005
1.017e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
1.170e+005
1.185e+005
1.170e+005
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
Phase Fraction [Vol. Basis]
66
Phase Fraction [Mass Basis]
67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
(lbmole/ft3)
16.89
16.84
0.3748
0.3753
0.3748
6.313
6.341
6.313
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-276.6
-292.7
-276.6
Mass Entropy
(Btu/lb-F)
1.940
1.942
1.940
9.485
9.560
9.485
0.5631
0.5659
0.5631
Licensed to: LEGENDS
(lb/ft3)
16.84
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
6948
7016
6948
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
6039
6098
6039
(Btu/lb)
---
---
1.000
0.0000
0.0000
1.000
---
---
---
455.6
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 186 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 64 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Vapour Phase
Liquid Phase
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
9.485
9.560
9.485
17
Std. Gas Flow
(MMSCFD)
0.0000
18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
0.0000
0.0000
(lb/ft3)
31.97
32.04
31.97
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
---
1.076
1.078
10.75
10.79
10.75
---
---
---
0.0000
---
---
1.265
1.262
1.265
1.358
1.358
1.358
7709
---
---
0.1787
0.2397
0.1787
4.454e-002
(barrel/day)
4.467e-002
4.454e-002
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
2.668
2.664
2.668
(Btu/lb)
457.7
---
---
0.0000
0.0000
1.0000
(dyne/cm)
5.316e-003
(Btu/hr-ft-F)
5.156e-002
6.495e-002
5.156e-002
1.807e-002
2.435e-002
1.807e-002
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
5.316e-003
7.499
7.574
7.499
0.4452
0.4483
0.4452
6.985
7.041
6.985
0.4147
0.4168
0.4147
---
7.039
---
---
0.4167
---
---
1.358
---
(psia)
---
---
---
(psia)
---
---
---
0.0000
0.0000
0.0000
---
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0002
0.0000
0.0003
0.0000
0.0002
55
H2O
0.0000
0.0011
0.0000
0.0012
0.0000
0.0006
56
Oxygen
0.0000
0.1253
0.0000
0.2381
0.0000
0.1072
57
Methane
0.0000
0.0739
0.0000
0.0704
0.0000
0.1204
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0000
0.3273
0.0000
0.0392
0.0000
0.2871
60
Ethane
0.0000
0.0190
0.0000
0.0340
0.0000
0.0490
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0000
0.0091
0.0000
0.0239
0.0000
0.0148
63
Nitrogen
0.0000
0.2207
0.0000
0.3670
0.0000
0.2330
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
67
Ammonia
0.0000
0.2232
0.0000
0.2257
0.0000
0.1875
68
Total
0.0000
1.0000
0.0000
1.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 187 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 64 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0002
0.0000
0.0003
0.0000
0.0002
16
H2O
0.0000
0.0013
0.0000
0.0014
0.0000
0.0007
17
Oxygen
0.0000
0.1248
0.0000
0.2364
0.0000
0.1066
18
Methane
0.0000
0.0745
0.0000
0.0707
0.0000
0.1213
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.3211
0.0000
0.0383
0.0000
0.2815
21
Ethane
0.0000
0.0198
0.0000
0.0352
0.0000
0.0507
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0094
0.0000
0.0244
0.0000
0.0152
24
Nitrogen
0.0000
0.2161
0.0000
0.3584
0.0000
0.2281
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0001
0.0000
0.0003
0.0000
0.0001
28
Ammonia
0.0000
0.2328
0.0000
0.2346
0.0000
0.1955
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0002
0.0000
0.0003
0.0000
0.0002
35
H2O
0.0000
0.0011
0.0000
0.0012
0.0000
0.0006
36
Oxygen
0.0000
0.1253
0.0000
0.2381
0.0000
0.1072
37
Methane
0.0000
0.0739
0.0000
0.0704
0.0000
0.1204
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.3273
0.0000
0.0392
0.0000
0.2871
40
Ethane
0.0000
0.0190
0.0000
0.0340
0.0000
0.0490
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0091
0.0000
0.0239
0.0000
0.0148
43
Nitrogen
0.0000
0.2207
0.0000
0.3670
0.0000
0.2330
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
47
Ammonia
0.0000
0.2232
0.0000
0.2257
0.0000
0.1875
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
0.9867
0.9867
---
53
H2O
1.179
1.179
---
54
Oxygen
0.9957
0.9957
---
55
Methane
1.008
1.008
---
---
---
---
56
H2S
57
Hydrogen
0.9811
0.9811
---
58
Ethane
1.037
1.037
---
59
Propane
---
---
---
60
CO2
1.024
1.024
---
61
Nitrogen
0.9794
0.9794
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
1.160
1.160
---
65
Ammonia
1.043
1.043
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 188 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 64 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Conversion Reactor:
13
LOGICAL CONNECTION
T-3 CONVERTIDOR
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
4820 psia 0.0000 lbmole/hrMass:
23
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 65
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
Liquid Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
5634
5634
0.0000
43
Molar Enthalpy
(Btu/lbmole)
-4944
-4944
-4658
44
Molar Entropy
(Btu/lbmole-F)
32.81
32.81
45
Heat Flow
46
Liq Vol Flow @Std Cond
1.0000
1.0000
0.0000
(F)
652.0
652.0
652.0
(psia)
4820
4820
4820
2500
2500
0.0000
(lbmole/hr) (lb/hr)
4.223e+004
4.223e+004
0.0000
32.68
(Btu/hr)
-1.236e+007
-1.236e+007
0.0000
(barrel/day)
* 4.041e+006
4.041e+006
0.0000
47
PROPERTIES
48 49
Overall
Vapour Phase
Liquid Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-292.7
-292.7
-276.6
55
Mass Entropy
(Btu/lb-F)
1.942
1.942
1.940
56
Heat Capacity
9.560
9.560
9.485
57
Mass Heat Capacity
0.5659
0.5659
0.5631
58
LHV Molar Basis (Std)
(Btu/lbmole)
1.030e+005
1.030e+005
1.017e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
1.185e+005
1.185e+005
1.170e+005
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66 67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
16.89
16.84
0.3753
0.3753
0.3748
6.341 2.847e+004
6.341 2.847e+004
6.313 0.0000
7016
7016
6948
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
6098
6098
6039
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
454.1
---
---
Licensed to: LEGENDS
(Btu/lb)
16.89
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 189 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 65 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Liquid Phase
(psia)
45.09
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
111.0
111.0
---
(lbmole/ft3)
1.897
1.897
1.898
Specific Heat
(Btu/lbmole-F)
9.560
9.560
9.485
Std. Gas Flow
(MMSCFD)
22.72
22.72
0.0000
(lb/ft3)
32.04
32.04
31.97
(USGPS)
---
---
---
---
1.076
1.078
10.79
10.79
10.75
---
---
---
0.0000
---
---
1.262
1.262
1.265
1.358
1.358
1.358
7865
---
---
0.2397
0.2397
0.1787
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
4.467e-002
4.467e-002
4.041e+006
4.041e+006
4.454e-002 0.0000
0.0000
0.0000
1.000
(ft3/lbmole)
2.664
2.664
2.668
(Btu/lb)
465.5
---
---
1.0000
1.0000
0.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
5.316e-003
6.495e-002
6.495e-002
5.156e-002
2.435e-002
2.435e-002
1.807e-002
7.574
7.574
7.499
0.4483
0.4483
0.4452
7.041
7.041
6.985
0.4168
0.4168
0.4147
7.039
7.039
---
0.4167
0.4167
---
1.358
1.358
---
(psia)
---
---
---
(psia)
---
---
(Btu/lb-F)
4.041e+006 ---
4.041e+006 ---
48
--0.0000 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
54
CO
0.4617
0.0002
12.9318
0.0003
1.1077
0.0002
55
H2O
3.3425
0.0013
60.2148
0.0014
4.1314
0.0007
56
Oxygen
311.9680
0.1248
9982.9749
0.2364
600.8390
0.1066
57
Methane
186.2348
0.0745
2987.7457
0.0707
683.3116
0.1213
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
802.7822
0.3211
1618.4089
0.0383
1586.2935
0.2815
60
Ethane
49.3871
0.0198
1485.0654
0.0352
285.8912
0.0507
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
23.3858
0.0094
1029.2020
0.0244
85.3864
0.0152
63
Nitrogen
540.3077
0.2161
15135.6397
0.3584
1285.2349
0.2281
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
67
Ammonia
581.8698
0.2328
9909.2435
0.2346
1101.3585
0.1955
68
Total
2499.9377
1.0000
42233.5343
1.0000
5634.3694
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 190 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 65 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.4617
0.0002
12.9318
0.0003
1.1077
0.0002
16
H2O
3.3425
0.0013
60.2148
0.0014
4.1314
0.0007
17
Oxygen
311.9680
0.1248
9982.9749
0.2364
600.8390
0.1066
18
Methane
186.2348
0.0745
2987.7457
0.0707
683.3116
0.1213
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
802.7822
0.3211
1618.4089
0.0383
1586.2935
0.2815
21
Ethane
49.3871
0.0198
1485.0654
0.0352
285.8912
0.0507
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
23.3858
0.0094
1029.2020
0.0244
85.3864
0.0152
24
Nitrogen
540.3077
0.2161
15135.6397
0.3584
1285.2349
0.2281
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
28
Ammonia
581.8698
0.2328
9909.2435
0.2346
1101.3585
0.1955
29
Total
2499.9377
1.0000
42233.5343
1.0000
5634.3694
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0002
0.0000
0.0003
0.0000
0.0002
35
H2O
0.0000
0.0011
0.0000
0.0012
0.0000
0.0006
36
Oxygen
0.0000
0.1253
0.0000
0.2381
0.0000
0.1072
37
Methane
0.0000
0.0739
0.0000
0.0704
0.0000
0.1204
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.3273
0.0000
0.0392
0.0000
0.2871
40
Ethane
0.0000
0.0190
0.0000
0.0340
0.0000
0.0490
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0091
0.0000
0.0239
0.0000
0.0148
43
Nitrogen
0.0000
0.2207
0.0000
0.3670
0.0000
0.2330
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
47
Ammonia
0.0000
0.2232
0.0000
0.2257
0.0000
0.1875
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
0.9867
0.9867
---
53
H2O
1.179
1.179
---
54
Oxygen
0.9957
0.9957
---
55
Methane
1.008
1.008
---
---
---
---
56
H2S
57
Hydrogen
0.9811
0.9811
---
58
Ethane
1.037
1.037
---
59
Propane
---
---
---
60
CO2
1.024
1.024
---
61
Nitrogen
0.9794
0.9794
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
1.160
1.160
---
65
Ammonia
1.043
1.043
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 191 of 336 * Specified by user.
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LEGENDS Bedford, MA USA
3 4 5
Case Name:
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Unit Set:
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Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 65 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO Cooler:
PRODUCT FROM E-21 CONDENSADOR Conversion Reactor:
13
LOGICAL CONNECTION
T-3 CONVERTIDOR
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
4820 psia 2500 lbmole/hrMass:
23
4.223e+004 lb/hrStd Ideal Liq Volume:
5634 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 66
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.8626
0.8626
0.1374
(F)
87.00*
87.00
87.00
(psia)
4565*
4565
4565
2500
2156
343.5
(lbmole/hr) (lb/hr)
4.223e+004
(barrel/day)
5634 -1.104e+004 24.93
3.613e+004 4942 -8118 25.54
(Btu/hr)
-2.761e+007
-1.751e+007
(barrel/day)
* 4.041e+006
3.488e+006
47
6104 692.5 -2.941e+004 21.07 -1.010e+007 721.7
PROPERTIES
48 49
Overall
Vapour Phase
Liquid Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-653.7
-484.6
-1655
55
Mass Entropy
(Btu/lb-F)
1.476
1.525
1.186
56
Heat Capacity
11.04
9.827
18.65
57
Mass Heat Capacity
0.6535
0.5866
58
LHV Molar Basis (Std)
(Btu/lbmole)
1.030e+005
9.722e+004
1.394e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
1.185e+005
1.112e+005
1.649e+005
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
16.75
17.77
0.8445
0.7725
2.039
14.27
12.94
36.24
1.265e+004
1.193e+004
719.9
1.049
7016
6635
9277
---
---
20.97
(lbmole/ft3)
---
---
2.459e-002
(lbmol/lb)
---
---
6.786e-004
(Btu/lb)
6098
5803
7845
Phase Fraction [Vol. Basis]
0.8771
0.8771
0.1229
66
Phase Fraction [Mass Basis]
0.8555
0.8555
67
Phase Fraction [Act. Vol. Basis]
0.9431
0.9431
68
Mass Exergy
343.4
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
16.89
(Btu/lb)
0.1445 5.690e-002 ---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 192 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 66 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Liquid Phase
(psia)
40.73
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
46.53
46.53
---
(lbmole/ft3)
1.897
1.865
2.120
Specific Heat
(Btu/lbmole-F)
11.04
9.827
18.65
Std. Gas Flow
(MMSCFD)
22.72
19.60
3.122
(lb/ft3)
32.04
31.25
37.68
(USGPS)
0.3500
---
0.3500
(psia)
(Btu/lbmole) (cSt)
---
1.007
0.3816
10.79
10.42
12.17
---
---
---
0.0000
---
---
1.219
1.253
1.119
1.491
1.673
1.907
7911
---
---
(lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb)
0.1651
4.467e-002
4.428e-002
36.15
4.041e+006
3.488e+006
721.7
0.1374
0.0000
1.000
1.184
1.295
0.4904
468.3
---
---
0.8626
0.8626
0.1374
(dyne/cm)
22.44
(Btu/hr-ft-F)
---
4.891e-002
---
2.006e-002
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
9.675e-002
---
22.44 0.2277 9.584e-002
9.054
7.841
16.66
0.5359
0.4680
0.9377
7.405
5.874
9.781
0.4383
0.3506
0.5504
15.84
5.850
9.126
0.9377
0.3492
0.5135
0.6968
1.680
2.044
---
---
511.5
---
---
3.489e+006 ---
3.488e+006 ---
48
4059 721.7 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.8626
LIQUID VOLUME FRACTION
54
CO
0.4617
0.0002
12.9318
0.0003
1.1077
0.0002
55
H2O
3.3425
0.0013
60.2148
0.0014
4.1314
0.0007
56
Oxygen
311.9680
0.1248
9982.9749
0.2364
600.8390
0.1066
57
Methane
186.2348
0.0745
2987.7457
0.0707
683.3116
0.1213
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
802.7822
0.3211
1618.4089
0.0383
1586.2935
0.2815
60
Ethane
49.3871
0.0198
1485.0654
0.0352
285.8912
0.0507
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
23.3858
0.0094
1029.2020
0.0244
85.3864
0.0152
63
Nitrogen
540.3077
0.2161
15135.6397
0.3584
1285.2349
0.2281
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
67
Ammonia
581.8698
0.2328
9909.2435
0.2346
1101.3585
0.1955
68
Total
2499.9377
1.0000
42233.5343
1.0000
5634.3694
69
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Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 193 of 336 * Specified by user.
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LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 66 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.8626 LIQUID VOLUME FRACTION
15
CO
0.4558
0.0002
12.7670
0.0004
1.0936
0.0002
16
H2O
0.0276
0.0000
0.4979
0.0000
0.0342
0.0000
17
Oxygen
302.4065
0.1402
9677.0083
0.2678
582.4240
0.1179
18
Methane
179.2695
0.0831
2876.0034
0.0796
657.7556
0.1331
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
794.8027
0.3686
1602.3222
0.0443
1570.5260
0.3178
21
Ethane
43.8254
0.0203
1317.8243
0.0365
253.6954
0.0513
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
19.2440
0.0089
846.9214
0.0234
70.2637
0.0142
24
Nitrogen
536.4766
0.2488
15028.3201
0.4160
1276.1220
0.2582
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0007
0.0000
0.0400
0.0000
0.0027
0.0000
28
Ammonia
279.9713
0.1298
4767.9118
0.1320
529.9275
0.1072
29
Total
2156.4801
1.0000
36129.6164
1.0000
4941.8446
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.1374 LIQUID VOLUME FRACTION
34
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
35
H2O
3.3148
0.0097
59.7169
0.0098
4.0972
0.0059
36
Oxygen
9.5615
0.0278
305.9667
0.0501
18.4150
0.0266
37
Methane
6.9652
0.0203
111.7423
0.0183
25.5560
0.0369
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
7.9795
0.0232
16.0867
0.0026
15.7675
0.0228
40
Ethane
5.5617
0.0162
167.2411
0.0274
32.1957
0.0465
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
4.1418
0.0121
182.2807
0.0299
15.1227
0.0218
43
Nitrogen
3.8311
0.0112
107.3196
0.0176
9.1130
0.0132
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.1976
0.0006
12.0674
0.0020
0.8125
0.0012
47
Ammonia
301.8985
0.8790
5141.3317
0.8423
571.4310
0.8251
48
Total
343.4576
1.0000
6103.9179
1.0000
692.5248
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
53
H2O
54
Oxygen
5.037
5.037
---
55
Methane
4.099
4.099
---
---
---
---
56
H2S
12.33 1.328e-003
12.33 1.328e-003
-----
57
Hydrogen
15.86
15.86
---
58
Ethane
1.255
1.255
---
59
Propane
---
---
---
60
CO2
0.7400
0.7400
---
61
Nitrogen
22.30
22.30
---
---
---
---
---
---
---
62
Air
63
Mercury
64
MEAmine
65
Ammonia
5.275e-004 0.1477
5.275e-004 0.1477
-----
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 194 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 66 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO Separator:
PRODUCT FROM
S-1 SEPARADOR PRIMARIO Cooler:
LOGICAL CONNECTION
E-21 CONDENSADOR
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 4565 psia
2500 lbmole/hrMass:
23
5634 barrel/day
User Variables
24 25
NOTES
26 27
4.223e+004 lb/hrStd Ideal Liq Volume:
29285
28 29 30
(Last modified Mon Dec 17, 2018, 15:22)
31 32
Description
33 34 35
Material Stream: 67
36 37 38
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
39 40
Overall
Vapour Phase
41
Vapour / Phase Fraction
42
Temperature:
43
Pressure:
44
Molar Flow
45
Mass Flow
46
Std Ideal Liq Vol Flow
(barrel/day)
4942
4942
47
Molar Enthalpy
(Btu/lbmole)
-8118
-8118
48
Molar Entropy
(Btu/lbmole-F)
49
Heat Flow
50
Liq Vol Flow @Std Cond
Liquid Phase
1.0000
1.0000
0.0000
(F)
87.00
87.00
87.00
(psia)
4565
4565
4565
2156
2156
0.0000
(lbmole/hr) (lb/hr)
3.613e+004
25.54
3.613e+004
25.54
0.0000 0.0000 -2.941e+004 21.07
(Btu/hr)
-1.751e+007
-1.751e+007
0.0000
(barrel/day)
* 3.488e+006
3.488e+006
0.0000
51
PROPERTIES
52 53
Overall
Vapour Phase
Liquid Phase
54
Molecular Weight
55
Molar Density
56
Mass Density
57
Act. Volume Flow
58
Mass Enthalpy
(Btu/lb)
-484.6
-484.6
-1655
59
Mass Entropy
(Btu/lb-F)
1.525
1.525
1.186
60
Heat Capacity
9.827
9.827
18.65
61
Mass Heat Capacity
0.5866
0.5866
62
LHV Molar Basis (Std)
(Btu/lbmole)
9.722e+004
9.722e+004
1.394e+005
63
HHV Molar Basis (Std)
(Btu/lbmole)
1.112e+005
1.112e+005
1.649e+005
64
HHV Mass Basis (Std)
65
CO2 Loading
66
CO2 App ML Con
67
CO2 App WT Con
68
LHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
16.75
16.75
17.77
0.7725
0.7725
2.039
12.94
12.94
1.193e+004
1.193e+004
36.24 0.0000
1.049
6635
6635
9277
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
5803
5803
7845
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 195 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 67 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Phase Fraction [Vol. Basis]
1.000
1.000
---
13
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
14
Phase Fraction [Act. Vol. Basis]
15
Mass Exergy
16
Partial Pressure of CO2
17
Cost Based on Flow
18
Act. Gas Flow
19
Avg. Liq. Density
20 21 22
Std. Ideal Liq. Mass Density
23
Act. Liq. Flow
24
Z Factor
25
Watson K
26
User Property
27
Partial Pressure of H2S
28
Cp/(Cp - R)
29
Cp/Cv
30
Heat of Vap.
31
Kinematic Viscosity
32
Liq. Mass Density (Std. Cond)
33
Liq. Vol. Flow (Std. Cond)
34
Liquid Fraction
35
Molar Volume
36
Mass Heat of Vap.
37
Phase Fraction [Molar Basis]
38
Surface Tension
39
Thermal Conductivity
40
Viscosity
41
Cv (Semi-Ideal)
42
Mass Cv (Semi-Ideal)
43
Cv
44
Mass Cv
45
Cv (Ent. Method)
46
Mass Cv (Ent. Method)
47
Cp/Cv (Ent. Method)
48
Reid VP at 37.8 C
(psia)
49
True VP at 37.8 C
(psia)
50
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
51
Viscosity Index
1.000
1.000
0.0000
(Btu/lb)
358.1
---
---
(psia)
40.73
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
46.53
46.53
---
(lbmole/ft3)
1.865
1.865
2.120
Specific Heat
(Btu/lbmole-F)
9.827
9.827
18.65
Std. Gas Flow
(MMSCFD)
19.60
19.60
0.0000
(lb/ft3)
31.25
31.25
37.68
(USGPS)
---
---
---
---
1.007
0.3816
10.42
10.42
12.17
---
---
---
0.0000
---
---
1.253
1.253
1.119
1.673
1.673
1.907
6063
---
(psia)
(Btu/lbmole) (cSt)
9.675e-002
(lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
9.675e-002
--0.1651
4.428e-002
4.428e-002
36.15
3.488e+006
3.488e+006
0.0000
0.0000
0.0000
1.000
1.295
1.295
0.4904
361.9
---
---
1.0000
1.0000
0.0000
---
---
4.891e-002
4.891e-002
2.006e-002
2.006e-002
22.44 0.2277 9.584e-002
7.841
7.841
16.66
0.4680
0.4680
0.9377
5.874
5.874
9.781
0.3506
0.3506
0.5504
5.850
5.850
9.126
0.3492
0.3492
0.5135
1.680
1.680
2.044
---
---
511.5
---
---
3.488e+006 ---
3.488e+006 ---
52
4059 0.0000 ---
COMPOSITION
53 54
Overall Phase
55 56
COMPONENTS
57
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
58
CO
0.4558
0.0002
12.7670
0.0004
1.0936
0.0002
59
H2O
0.0276
0.0000
0.4979
0.0000
0.0342
0.0000
60
Oxygen
302.4065
0.1402
9677.0083
0.2678
582.4240
0.1179
61
Methane
179.2695
0.0831
2876.0034
0.0796
657.7556
0.1331
62
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Hydrogen
794.8027
0.3686
1602.3222
0.0443
1570.5260
0.3178
64
Ethane
43.8254
0.0203
1317.8243
0.0365
253.6954
0.0513
65
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
CO2
19.2440
0.0089
846.9214
0.0234
70.2637
0.0142
67
Nitrogen
536.4766
0.2488
15028.3201
0.4160
1276.1220
0.2582
68
Air
0.0000
0.0000
0.0000
0.0000
69
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0.0000
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0.0000
Page 196 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 67 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
MEAmine
0.0007
0.0000
0.0400
0.0000
0.0027
0.0000
17
Ammonia
279.9713
0.1298
4767.9118
0.1320
529.9275
0.1072
18
Total
2156.4801
1.0000
36129.6164
1.0000
4941.8446
1.0000
19
Vapour Phase
20 21
COMPONENTS
22
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
23
CO
0.4558
0.0002
12.7670
0.0004
1.0936
0.0002
24
H2O
0.0276
0.0000
0.4979
0.0000
0.0342
0.0000
25
Oxygen
302.4065
0.1402
9677.0083
0.2678
582.4240
0.1179
26
Methane
179.2695
0.0831
2876.0034
0.0796
657.7556
0.1331
27
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Hydrogen
794.8027
0.3686
1602.3222
0.0443
1570.5260
0.3178
29
Ethane
43.8254
0.0203
1317.8243
0.0365
253.6954
0.0513
30
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
CO2
19.2440
0.0089
846.9214
0.0234
70.2637
0.0142
32
Nitrogen
536.4766
0.2488
15028.3201
0.4160
1276.1220
0.2582
33
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
MEAmine
0.0007
0.0000
0.0400
0.0000
0.0027
0.0000
36
Ammonia
279.9713
0.1298
4767.9118
0.1320
529.9275
0.1072
37
Total
2156.4801
1.0000
36129.6164
1.0000
4941.8446
1.0000
38
Liquid Phase
39 40
COMPONENTS
41
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
42
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
H2O
0.0000
0.0097
0.0000
0.0098
0.0000
0.0059
44
Oxygen
0.0000
0.0278
0.0000
0.0501
0.0000
0.0266
45
Methane
0.0000
0.0203
0.0000
0.0183
0.0000
0.0369
46
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Hydrogen
0.0000
0.0232
0.0000
0.0026
0.0000
0.0228
48
Ethane
0.0000
0.0162
0.0000
0.0274
0.0000
0.0465
49
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
CO2
0.0000
0.0121
0.0000
0.0299
0.0000
0.0218
51
Nitrogen
0.0000
0.0112
0.0000
0.0176
0.0000
0.0132
52
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
MEAmine
0.0000
0.0006
0.0000
0.0020
0.0000
0.0012
55
Ammonia
0.0000
0.8790
0.0000
0.8423
0.0000
0.8251
56
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
57
K VALUE
58 59
COMPONENTS
MIXED
LIGHT
HEAVY
60
CO
61
H2O
62
Oxygen
5.037
5.037
---
63
Methane
4.099
4.099
---
---
---
---
64
H2S
12.33 1.328e-003
12.33 1.328e-003
-----
65
Hydrogen
15.86
15.86
---
66
Ethane
1.255
1.255
---
67
Propane
---
---
---
68
CO2
0.7400
0.7400
69
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---
Page 197 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 67 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Nitrogen
13
Air
14
Mercury
15
MEAmine
16
Ammonia
LIGHT
HEAVY
22.30
22.30
---
---
---
---
---
---
---
5.275e-004
5.275e-004
0.1477
17
---
0.1477
---
UNIT OPERATIONS
18 19 20
Fluid Package:
FEED TO
PRODUCT FROM
Tee:
TEE-104 Separator:
21
LOGICAL CONNECTION
S-1 SEPARADOR PRIMARIO
UTILITIES
22 23
( No utilities reference this stream )
24
PROCESS UTILITY
25 26 27
DYNAMICS
28 29
Pressure Specification
(Inactive):
30
Flow Specification
(Inactive) Molar:
4565 psia 2156 lbmole/hrMass:
31
3.613e+004 lb/hrStd Ideal Liq Volume:
4942 barrel/day
User Variables
32 33
NOTES
34 35 36
Description
37 38 39
Material Stream: 68
40 41 42
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
43 44
Overall
45
Vapour / Phase Fraction
46
Temperature:
47
Pressure:
48
Molar Flow
49
Mass Flow
50
Std Ideal Liq Vol Flow
51
Molar Enthalpy
(Btu/lbmole)
52
Molar Entropy
(Btu/lbmole-F)
53
Heat Flow
54
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
87.00
87.00
87.00
(psia)
4565
4565
4565
343.5
0.0000
343.5
6104
0.0000
6104
692.5
0.0000
692.5
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-2.941e+004 21.07 -1.010e+007 721.7*
(barrel/day)
55
-8118 25.54 0.0000 0.0000
-2.941e+004 21.07 -1.010e+007 721.7
PROPERTIES
56 57
Overall
58
Molecular Weight
59
Molar Density
60
Mass Density
61
Act. Volume Flow
62
Vapour Phase
Liquid Phase
17.77
16.75
17.77
2.039
0.7725
2.039
36.24
12.94
36.24
(barrel/day)
719.9
0.0000
719.9
Mass Enthalpy
(Btu/lb)
-1655
-484.6
-1655
63
Mass Entropy
(Btu/lb-F)
1.186
1.525
1.186
64
Heat Capacity
18.65
9.827
18.65
65
Mass Heat Capacity
1.049
0.5866
66
LHV Molar Basis (Std)
(Btu/lbmole)
1.394e+005
9.722e+004
1.394e+005
67
HHV Molar Basis (Std)
(Btu/lbmole)
1.649e+005
1.112e+005
1.649e+005
68
HHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
9277
6635
1.049
9277
Aspen HYSYS Version 8.8 (34.0.0.8909)
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1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 68 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
CO2 Loading
13
CO2 App ML Con
(lbmole/ft3)
2.459e-002
14
CO2 App WT Con
(lbmol/lb)
6.786e-004
15
LHV Mass Basis (Std)
16
Phase Fraction [Vol. Basis]
17 18 19
Mass Exergy
20
Partial Pressure of CO2
21
Cost Based on Flow
22
Act. Gas Flow
23
Avg. Liq. Density
24 25 26
Std. Ideal Liq. Mass Density
27
Act. Liq. Flow
28
Z Factor
29
Watson K
30
User Property
31
Partial Pressure of H2S
32
Cp/(Cp - R)
33
Cp/Cv
34
Heat of Vap.
35
Kinematic Viscosity
36
Liq. Mass Density (Std. Cond)
37
Liq. Vol. Flow (Std. Cond)
38
Liquid Fraction
39
Molar Volume
40
Mass Heat of Vap.
41
Phase Fraction [Molar Basis]
42
Surface Tension
43
Thermal Conductivity
44
Viscosity
45
Cv (Semi-Ideal)
46
Mass Cv (Semi-Ideal)
47
Cv
48
Mass Cv
49
Cv (Ent. Method)
50
Mass Cv (Ent. Method)
51
Cp/Cv (Ent. Method)
52
Reid VP at 37.8 C
(psia)
53
True VP at 37.8 C
(psia)
54
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
55
Viscosity Index
20.97
(Btu/lb)
Liquid Phase
---
20.97
---
2.459e-002
---
6.786e-004
7845
5803
7845
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
(Btu/lb)
182.1
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.120
1.865
2.120
Specific Heat
(Btu/lbmole-F)
18.65
9.827
18.65
Std. Gas Flow
(MMSCFD)
3.122
0.0000
3.122
(lb/ft3)
37.68
31.25
37.68
(USGPS)
0.3500
---
0.3500
(psia)
(Btu/lbmole)
---
1.007
0.3816
12.17
10.42
12.17
---
---
---
0.0000
---
---
1.119
1.253
1.119
1.907
1.673
1.907
---
---
---
(cSt)
0.1651
9.675e-002
0.1651
(lb/ft3)
36.15
4.428e-002
36.15
(barrel/day) (ft3/lbmole) (Btu/lb)
721.7
0.0000
1.000
0.0000
1.000
0.4904
1.295
0.4904
-792.7
---
---
0.0000
0.0000
1.0000
(dyne/cm)
22.44
(Btu/hr-ft-F)
0.2277
(cP)
9.584e-002
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
721.7
--4.891e-002 2.006e-002
22.44 0.2277 9.584e-002
16.66
7.841
16.66
0.9377
0.4680
0.9377
9.781
5.874
9.781
0.5504
0.3506
0.5504
9.126
5.850
9.126
0.5135
0.3492
0.5135
2.044
1.680
2.044
511.5
---
511.5
4059
---
4059
721.7
0.0000
721.7
---
---
---
56
COMPOSITION
57 58
Overall Phase
59 60
COMPONENTS
61
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
62
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
63
H2O
3.3148
0.0097
59.7169
0.0098
4.0972
0.0059
64
Oxygen
9.5615
0.0278
305.9667
0.0501
18.4150
0.0266
65
Methane
6.9652
0.0203
111.7423
0.0183
25.5560
0.0369
66
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Hydrogen
7.9795
0.0232
16.0867
0.0026
15.7675
0.0228
68
Ethane
5.5617
0.0162
167.2411
0.0274
32.1957
69
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1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 68 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
CO2
4.1418
0.0121
182.2807
0.0299
15.1227
0.0218
17
Nitrogen
3.8311
0.0112
107.3196
0.0176
9.1130
0.0132
18
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
MEAmine
0.1976
0.0006
12.0674
0.0020
0.8125
0.0012
21
Ammonia
301.8985
0.8790
5141.3317
0.8423
571.4310
0.8251
22
Total
343.4576
1.0000
6103.9179
1.0000
692.5248
1.0000
23
Vapour Phase
24 25
COMPONENTS
26
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
27
CO
0.0000
0.0002
0.0000
0.0004
0.0000
0.0002
28
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Oxygen
0.0000
0.1402
0.0000
0.2678
0.0000
0.1179
30
Methane
0.0000
0.0831
0.0000
0.0796
0.0000
0.1331
31
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Hydrogen
0.0000
0.3686
0.0000
0.0443
0.0000
0.3178
33
Ethane
0.0000
0.0203
0.0000
0.0365
0.0000
0.0513
34
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
CO2
0.0000
0.0089
0.0000
0.0234
0.0000
0.0142
36
Nitrogen
0.0000
0.2488
0.0000
0.4160
0.0000
0.2582
37
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ammonia
0.0000
0.1298
0.0000
0.1320
0.0000
0.1072
41
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
42
Liquid Phase
43 44
COMPONENTS
45
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
46
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
47
H2O
3.3148
0.0097
59.7169
0.0098
4.0972
0.0059
48
Oxygen
9.5615
0.0278
305.9667
0.0501
18.4150
0.0266
49
Methane
6.9652
0.0203
111.7423
0.0183
25.5560
0.0369
50
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Hydrogen
7.9795
0.0232
16.0867
0.0026
15.7675
0.0228
52
Ethane
5.5617
0.0162
167.2411
0.0274
32.1957
0.0465
53
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
CO2
4.1418
0.0121
182.2807
0.0299
15.1227
0.0218
55
Nitrogen
3.8311
0.0112
107.3196
0.0176
9.1130
0.0132
56
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
MEAmine
0.1976
0.0006
12.0674
0.0020
0.8125
0.0012
59
Ammonia
301.8985
0.8790
5141.3317
0.8423
571.4310
0.8251
60
Total
343.4576
1.0000
6103.9179
1.0000
692.5248
1.0000
61
K VALUE
62 63
COMPONENTS
MIXED
LIGHT
HEAVY
64
CO
65
H2O
66
Oxygen
5.037
5.037
---
67
Methane
4.099
4.099
---
---
---
68 69
H2S
Aspen Technology Inc. Licensed to: LEGENDS
12.33 1.328e-003
Aspen HYSYS Version 8.8 (34.0.0.8909)
12.33 1.328e-003
-----
---
Page 200 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 68 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
Hydrogen
15.86
15.86
---
13
Ethane
1.255
1.255
---
14
Propane
---
---
---
15
CO2
0.7400
0.7400
---
16
Nitrogen
22.30
22.30
---
---
---
---
---
---
---
17
Air
18
Mercury
19
MEAmine
20
Ammonia
5.275e-004 0.1477
21
---
0.1477
---
UNIT OPERATIONS
22 23 24
5.275e-004
FEED TO
PRODUCT FROM
Mixer:
MIX-103 Separator:
LOGICAL CONNECTION
S-1 SEPARADOR PRIMARIO
25
UTILITIES
26 27
( No utilities reference this stream )
28
PROCESS UTILITY
29 30 31
DYNAMICS
32 33
Pressure Specification
(Inactive):
34
Flow Specification
(Inactive) Molar:
4565 psia 343.5 lbmole/hrMass:
35
6104 lb/hr Std Ideal Liq Volume:
692.5 barrel/day
User Variables
36 37
NOTES
38 39 40
Description
41 42 43
Material Stream: 69
44 45 46
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
47 48
Overall
Vapour Phase
49
Vapour / Phase Fraction
50
Temperature:
51
Pressure:
52
Molar Flow
53
Mass Flow
54
Std Ideal Liq Vol Flow
(barrel/day)
2959
2959
55
Molar Enthalpy
(Btu/lbmole)
-8118
-8118
56
Molar Entropy
(Btu/lbmole-F)
57
Heat Flow
58
Liq Vol Flow @Std Cond
Liquid Phase
1.0000
1.0000
0.0000
(F)
87.00
87.00
87.00
(psia)
4565
4565
4565
1291*
1291
0.0000
(lbmole/hr) (lb/hr)
2.163e+004
25.54
2.163e+004
25.54
0.0000 0.0000 -2.941e+004 21.07
(Btu/hr)
-1.048e+007
-1.048e+007
0.0000
(barrel/day)
* 2.089e+006
2.089e+006
0.0000
59
PROPERTIES
60 61
Overall
62
Molecular Weight
63
Molar Density
64
Mass Density
65
Act. Volume Flow
66 67 68
Heat Capacity
69
Aspen Technology Inc.
Vapour Phase
Liquid Phase
16.75
16.75
17.77
0.7725
0.7725
2.039
12.94
12.94
36.24
(barrel/day)
7146
7146
0.0000
Mass Enthalpy
(Btu/lb)
-484.6
-484.6
-1655
Mass Entropy
(Btu/lb-F)
1.525
1.525
1.186
9.827
9.827
18.65
Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 201 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 69 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Heat Capacity
13
LHV Molar Basis (Std)
(Btu/lbmole)
9.722e+004
9.722e+004
1.394e+005
14
HHV Molar Basis (Std)
(Btu/lbmole)
1.112e+005
1.112e+005
1.649e+005
15
HHV Mass Basis (Std)
16
CO2 Loading
17
CO2 App ML Con
18
CO2 App WT Con
19
LHV Mass Basis (Std)
20 21 22
Phase Fraction [Act. Vol. Basis]
23
Mass Exergy
24
Partial Pressure of CO2
25
Cost Based on Flow
26
Act. Gas Flow
27
Avg. Liq. Density
28 29 30
Std. Ideal Liq. Mass Density
31
Act. Liq. Flow
32
Z Factor
33
Watson K
34
User Property
35
Partial Pressure of H2S
36
Cp/(Cp - R)
37
Cp/Cv
38
Heat of Vap.
39
Kinematic Viscosity
40
Liq. Mass Density (Std. Cond)
41
Liq. Vol. Flow (Std. Cond)
42
Liquid Fraction
43
Molar Volume
44
Mass Heat of Vap.
45
Phase Fraction [Molar Basis]
46
Surface Tension
47
Thermal Conductivity
48
Viscosity
49
Cv (Semi-Ideal)
50
Mass Cv (Semi-Ideal)
51
Cv
52
Mass Cv
53
Cv (Ent. Method)
54
Mass Cv (Ent. Method)
55
Cp/Cv (Ent. Method)
56
Reid VP at 37.8 C
(psia)
57
True VP at 37.8 C
(psia)
58
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
59
Viscosity Index
(Btu/lb-F)
(Btu/lb)
0.5866
0.5866
1.049
6635
6635
9277
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
5803
5803
7845
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
358.1
---
---
(psia)
40.73
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
27.86
27.86
---
(lbmole/ft3)
1.865
1.865
2.120
Specific Heat
(Btu/lbmole-F)
9.827
9.827
18.65
Std. Gas Flow
(MMSCFD)
11.74
11.74
0.0000
(lb/ft3)
31.25
31.25
37.68
(USGPS)
---
---
---
---
1.007
0.3816
10.42
10.42
12.17
---
---
---
0.0000
---
---
1.253
1.253
1.119
1.673
1.673
1.907
6063
---
(psia)
(Btu/lbmole) (cSt)
9.675e-002
(lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
9.675e-002
--0.1651
4.428e-002
4.428e-002
36.15
2.089e+006
2.089e+006
0.0000
0.0000
0.0000
1.000
1.295
1.295
0.4904
361.9
---
---
1.0000
1.0000
0.0000
---
---
4.891e-002
4.891e-002
2.006e-002
2.006e-002
22.44 0.2277 9.584e-002
7.841
7.841
16.66
0.4680
0.4680
0.9377
5.874
5.874
9.781
0.3506
0.3506
0.5504
5.850
5.850
9.126
0.3492
0.3492
0.5135
1.680
1.680
2.044
---
---
511.5
---
---
2.089e+006 ---
2.089e+006 ---
60
4059 0.0000 ---
COMPOSITION
61 62
Overall Phase
63 64
COMPONENTS
65
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
66
CO
0.2729
0.0002
7.6449
0.0004
0.6548
0.0002
67
H2O
0.0165
0.0000
0.2981
0.0000
0.0205
0.0000
68
Oxygen
181.0814
0.1402
5794.6062
0.2678
348.7563
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.1179
Page 202 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 69 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14 15
Methane
16
H2S
17
Hydrogen
18
Ethane
19
Propane
20
CO2
21
Nitrogen
22
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
107.3469
0.0831
1722.1549
0.0796
393.8650
0.1331
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
475.9290
0.3686
959.4728
0.0443
940.4332
0.3178
26.2427
0.0203
789.1151
0.0365
151.9132
0.0513
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
11.5233
0.0089
507.1377
0.0234
42.0740
0.0142
321.2430
0.2488
8998.9793
0.4160
764.1436
0.2582
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
MEAmine
0.0004
0.0000
0.0239
0.0000
0.0016
0.0000
25
Ammonia
167.6472
0.1298
2855.0323
0.1320
317.3213
0.1072
26
Total
1291.3033
1.0000
21634.4653
1.0000
2959.1835
1.0000
27
Vapour Phase
28 29
COMPONENTS
30
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
31
CO
0.2729
0.0002
7.6449
0.0004
0.6548
0.0002
32
H2O
0.0165
0.0000
0.2981
0.0000
0.0205
0.0000
33
Oxygen
181.0814
0.1402
5794.6062
0.2678
348.7563
0.1179
34
Methane
107.3469
0.0831
1722.1549
0.0796
393.8650
0.1331
35
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Hydrogen
475.9290
0.3686
959.4728
0.0443
940.4332
0.3178
37
Ethane
26.2427
0.0203
789.1151
0.0365
151.9132
0.0513
38
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
CO2
11.5233
0.0089
507.1377
0.0234
42.0740
0.0142
40
Nitrogen
321.2430
0.2488
8998.9793
0.4160
764.1436
0.2582
41
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
MEAmine
0.0004
0.0000
0.0239
0.0000
0.0016
0.0000
44
Ammonia
167.6472
0.1298
2855.0323
0.1320
317.3213
0.1072
45
Total
1291.3033
1.0000
21634.4653
1.0000
2959.1835
1.0000
46
Liquid Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
50
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
H2O
0.0000
0.0097
0.0000
0.0098
0.0000
0.0059
52
Oxygen
0.0000
0.0278
0.0000
0.0501
0.0000
0.0266
53
Methane
0.0000
0.0203
0.0000
0.0183
0.0000
0.0369
54
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Hydrogen
0.0000
0.0232
0.0000
0.0026
0.0000
0.0228
56
Ethane
0.0000
0.0162
0.0000
0.0274
0.0000
0.0465
57
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
CO2
0.0000
0.0121
0.0000
0.0299
0.0000
0.0218
59
Nitrogen
0.0000
0.0112
0.0000
0.0176
0.0000
0.0132
60
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
MEAmine
0.0000
0.0006
0.0000
0.0020
0.0000
0.0012
63
Ammonia
0.0000
0.8790
0.0000
0.8423
0.0000
0.8251
64
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
65
K VALUE
66 67
COMPONENTS
68 69
MIXED CO
Aspen Technology Inc. Licensed to: LEGENDS
LIGHT 12.33
Aspen HYSYS Version 8.8 (34.0.0.8909)
HEAVY 12.33
---
Page 203 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 69 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
H2O
13
Oxygen
5.037
5.037
---
14
Methane
4.099
4.099
---
---
---
---
15
1.328e-003
H2S
1.328e-003
---
16
Hydrogen
15.86
15.86
---
17
Ethane
1.255
1.255
---
18
Propane
---
---
---
19
CO2
0.7400
0.7400
---
20
Nitrogen
22.30
22.30
---
---
---
---
---
---
---
21
Air
22
Mercury
23
MEAmine
24
Ammonia
5.275e-004 0.1477
25
---
0.1477
---
UNIT OPERATIONS
26 27 28
5.275e-004
FEED TO
PRODUCT FROM
Compressor:
K-103
Tee:
LOGICAL CONNECTION TEE-104
29
UTILITIES
30 31
( No utilities reference this stream )
32
PROCESS UTILITY
33 34 35
DYNAMICS
36 37
Pressure Specification
(Inactive):
38
Flow Specification
(Active)
4565 psia * Mass: 1291 lbmole/hr
Molar:
39
2.163e+004 lb/hrStd Ideal Liq Volume:
2959 barrel/day
User Variables
40 41
NOTES
42 43 44
Description
45 46 47
Material Stream: 70
48 49 50
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
51 52
Overall
Vapour Phase
53
Vapour / Phase Fraction
54
Temperature:
55
Pressure:
56
Molar Flow
57
Mass Flow
58
Std Ideal Liq Vol Flow
(barrel/day)
2959
2959
59
Molar Enthalpy
(Btu/lbmole)
-8038
-8038
60
Molar Entropy
(Btu/lbmole-F)
61
Heat Flow
62
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
96.88
96.88
(psia)
4820*
4820
(lbmole/hr) (lb/hr)
1291 2.163e+004
25.58
1291 2.163e+004
25.58
(Btu/hr)
-1.038e+007
-1.038e+007
(barrel/day)
* 2.089e+006
2.089e+006
63
PROPERTIES
64 65
Overall
66
Molecular Weight
67
Molar Density
68
Mass Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
Vapour Phase 16.75
16.75
0.7898
0.7898
13.23
13.23
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 204 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 70 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Act. Volume Flow
13
Mass Enthalpy
14
Mass Entropy
15
Heat Capacity
16
Mass Heat Capacity
17
LHV Molar Basis (Std)
(Btu/lbmole)
9.722e+004
9.722e+004
18
HHV Molar Basis (Std)
(Btu/lbmole)
1.112e+005
1.112e+005
19
HHV Mass Basis (Std)
20
CO2 Loading
21
CO2 App ML Con
22
CO2 App WT Con
23
LHV Mass Basis (Std)
24 25
(barrel/day)
6989
6989
(Btu/lb)
-479.8
-479.8
(Btu/lb-F)
1.527
1.527
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
9.786
9.786
0.5841
0.5841
6635
6635
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
5803
5803
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
26
Phase Fraction [Act. Vol. Basis]
1.000
1.000
27
Mass Exergy
(Btu/lb)
361.7
---
28
Partial Pressure of CO2
(psia)
43.01
29
Cost Based on Flow
30
Act. Gas Flow
31
Avg. Liq. Density
32
(Cost/s)
1.050e+004
--1.050e+004
(ACFM)
27.25
27.25
(lbmole/ft3)
1.865
1.865
Specific Heat
(Btu/lbmole-F)
9.786
9.786
33
Std. Gas Flow
(MMSCFD)
11.74
11.74
34
Std. Ideal Liq. Mass Density
(lb/ft3)
31.25
31.25
35
Act. Liq. Flow
(USGPS)
---
---
36
Z Factor
1.022
1.022
37
Watson K
10.42
10.42
38
User Property
---
---
39
Partial Pressure of H2S
40
Cp/(Cp - R)
41
Cp/Cv
42
Heat of Vap.
43
Kinematic Viscosity
44
Liq. Mass Density (Std. Cond)
45
Liq. Vol. Flow (Std. Cond)
46
Liquid Fraction
47
Molar Volume
48
Mass Heat of Vap.
49
Phase Fraction [Molar Basis]
50
Surface Tension
51
Thermal Conductivity
52
Viscosity
53
Cv (Semi-Ideal)
54
Mass Cv (Semi-Ideal)
55
Cv
56
Mass Cv
57
Cv (Ent. Method)
58
Mass Cv (Ent. Method)
59
Cp/Cv (Ent. Method)
60
Reid VP at 37.8 C
(psia)
61
True VP at 37.8 C
(psia)
---
62
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
63
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.255
1.255
1.660
1.660
6030 9.662e-002
--9.662e-002
4.428e-002
4.428e-002
2.089e+006
2.089e+006
0.0000
0.0000
(ft3/lbmole)
1.266
1.266
(Btu/lb)
359.9
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
---
4.995e-002
4.995e-002
2.048e-002
2.048e-002
7.800
7.800
0.4656
0.4656
5.894
5.894
0.3518
0.3518
5.846
5.846
0.3489
0.3489
1.674
1.674
---
-----
2.089e+006 ---
2.089e+006 ---
64 65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 205 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 70 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
CO
0.2729
0.0002
7.6449
0.0004
0.6548
0.0002
16
H2O
0.0165
0.0000
0.2981
0.0000
0.0205
0.0000
17
Oxygen
181.0814
0.1402
5794.6062
0.2678
348.7563
0.1179
18
Methane
107.3469
0.0831
1722.1549
0.0796
393.8650
0.1331
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
475.9290
0.3686
959.4728
0.0443
940.4332
0.3178
21
Ethane
26.2427
0.0203
789.1151
0.0365
151.9132
0.0513
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
11.5233
0.0089
507.1377
0.0234
42.0740
0.0142
24
Nitrogen
321.2430
0.2488
8998.9793
0.4160
764.1436
0.2582
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0004
0.0000
0.0239
0.0000
0.0016
0.0000
28
Ammonia
167.6472
0.1298
2855.0323
0.1320
317.3213
0.1072
29
Total
1291.3033
1.0000
21634.4653
1.0000
2959.1835
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.2729
0.0002
7.6449
0.0004
0.6548
0.0002
35
H2O
0.0165
0.0000
0.2981
0.0000
0.0205
0.0000
36
Oxygen
181.0814
0.1402
5794.6062
0.2678
348.7563
0.1179
37
Methane
107.3469
0.0831
1722.1549
0.0796
393.8650
0.1331
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
475.9290
0.3686
959.4728
0.0443
940.4332
0.3178
40
Ethane
26.2427
0.0203
789.1151
0.0365
151.9132
0.0513
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
11.5233
0.0089
507.1377
0.0234
42.0740
0.0142
43
Nitrogen
321.2430
0.2488
8998.9793
0.4160
764.1436
0.2582
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0004
0.0000
0.0239
0.0000
0.0016
0.0000
47
Ammonia
167.6472
0.1298
2855.0323
0.1320
317.3213
0.1072
48
Total
1291.3033
1.0000
21634.4653
1.0000
2959.1835
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 206 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 70 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Recycle:
RCY-2
Compressor:
13
LOGICAL CONNECTION K-103
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 4820 psia
1291 lbmole/hrMass:
23
2959 barrel/day
User Variables
24 25
NOTES
26 27
2.163e+004 lb/hrStd Ideal Liq Volume:
29285
28 29 30
(Last modified Mon Dec 17, 2018, 15:08)
31 32
Description
33 34 35
Material Stream: 71
36 37 38
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
39 40
Overall
Vapour Phase
41
Vapour / Phase Fraction
42
Temperature:
43
Pressure:
44
Molar Flow
45
Mass Flow
46
Std Ideal Liq Vol Flow
(barrel/day)
2958
2958
47
Molar Enthalpy
(Btu/lbmole)
-8043
-8043
48
Molar Entropy
(Btu/lbmole-F)
49
Heat Flow
50
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
96.86*
96.86
(psia)
4820*
4820
1291*
(lbmole/hr) (lb/hr)
2.164e+004
25.58
1291 2.164e+004
25.58
(Btu/hr)
-1.039e+007
-1.039e+007
(barrel/day)
* 2.089e+006
2.089e+006
51
PROPERTIES
52 53
Overall
Vapour Phase
54
Molecular Weight
55
Molar Density
56
Mass Density
57
Act. Volume Flow
58
Mass Enthalpy
59
Mass Entropy
60
Heat Capacity
61
Mass Heat Capacity
62
LHV Molar Basis (Std)
(Btu/lbmole)
9.718e+004
9.718e+004
63
HHV Molar Basis (Std)
(Btu/lbmole)
1.111e+005
1.111e+005
64
HHV Mass Basis (Std)
65
CO2 Loading
66
CO2 App ML Con
67
CO2 App WT Con
68
LHV Mass Basis (Std)
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
16.76
16.76
0.7902
0.7902
13.25
13.25
(barrel/day)
6985
6985
(Btu/lb)
-479.8
-479.8
(Btu/lb-F)
1.526
1.526
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
9.794
9.794
0.5843
0.5843
6629
6629
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
5797
5797
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 207 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 71 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Phase Fraction [Vol. Basis]
1.000
1.000
13
Phase Fraction [Mass Basis]
1.000
1.000
14
Phase Fraction [Act. Vol. Basis]
1.000
1.000
15
Mass Exergy
(Btu/lb)
361.5
---
16
Partial Pressure of CO2
(psia)
42.76
---
17
Cost Based on Flow
(Cost/s)
0.0000
0.0000
18
Act. Gas Flow
19
Avg. Liq. Density
20
(ACFM)
27.24
27.24
(lbmole/ft3)
1.866
1.866
Specific Heat
(Btu/lbmole-F)
9.794
9.794
21
Std. Gas Flow
(MMSCFD)
11.74
11.74
22
Std. Ideal Liq. Mass Density
(lb/ft3)
31.28
31.28
23
Act. Liq. Flow
(USGPS)
---
---
24
Z Factor
1.021
1.021
25
Watson K
10.41
10.41
26
User Property
---
---
27
Partial Pressure of H2S
28
Cp/(Cp - R)
29
Cp/Cv
30
Heat of Vap.
31
Kinematic Viscosity
32
Liq. Mass Density (Std. Cond)
33
Liq. Vol. Flow (Std. Cond)
34
Liquid Fraction
35
Molar Volume
36
Mass Heat of Vap.
37
Phase Fraction [Molar Basis]
38
Surface Tension
39
Thermal Conductivity
40
Viscosity
41
Cv (Semi-Ideal)
42
Mass Cv (Semi-Ideal)
43
Cv
44
Mass Cv
45
Cv (Ent. Method)
46
Mass Cv (Ent. Method)
47
Cp/Cv (Ent. Method)
48
Reid VP at 37.8 C
(psia)
49
True VP at 37.8 C
(psia)
---
50
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
51
Viscosity Index
(psia)
(Btu/lbmole) (cSt)
0.0000
---
1.254
1.254
1.661
1.661
6041 9.659e-002
(lb/ft3) (barrel/day)
--9.659e-002
4.430e-002
4.430e-002
2.089e+006
2.089e+006
0.0000
0.0000
(ft3/lbmole)
1.266
1.266
(Btu/lb)
360.4
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
---
4.994e-002
4.994e-002
2.049e-002
2.049e-002
7.808
7.808
0.4658
0.4658
5.898
5.898
0.3519
0.3519
5.872
5.872
0.3503
0.3503
1.668
1.668
---
-----
2.089e+006 ---
2.089e+006 ---
52
COMPOSITION
53 54
Overall Phase
55 56
COMPONENTS
57
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
58
CO
* 0.2722
* 0.0002
* 7.6247
* 0.0004
* 0.6531
* 0.0002
59
H2O
* 0.0177
* 0.0000
* 0.3184
* 0.0000
* 0.0218
* 0.0000
60
Oxygen
* 181.3331
* 0.1404
* 5802.6593
* 0.2681
* 349.2410
* 0.1181
61
Methane
* 107.5045
* 0.0833
* 1724.6836
* 0.0797
* 394.4433
* 0.1333
62
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
63
Hydrogen
* 475.0657
* 0.3679
* 957.7325
* 0.0442
* 938.7275
* 0.3173
64
Ethane
* 26.0279
* 0.0202
* 782.6557
* 0.0362
* 150.6697
* 0.0509
65
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
66
CO2
* 11.4565
* 0.0089
* 504.1985
* 0.0233
* 41.8302
* 0.0141
67
Nitrogen
* 321.1098
* 0.2487
* 8995.2496
* 0.4156
* 763.8269
* 0.2582
68
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
* 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
* 0.0000
Page 208 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 71 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
16
MEAmine
* 0.0005
* 0.0000
* 0.0277
* 0.0000
* 0.0019
* 0.0000
17
Ammonia
* 168.5154
* 0.1305
* 2869.8180
* 0.1326
* 318.9647
* 0.1078
18
Total
1291.3033
1.0000
21644.9682
1.0000
2958.3801
1.0000
19
Vapour Phase
20 21
COMPONENTS
MOLAR FLOW (lbmole/hr)
22
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
23
CO
0.2722
0.0002
7.6247
0.0004
0.6531
0.0002
24
H2O
0.0177
0.0000
0.3184
0.0000
0.0218
0.0000
25
Oxygen
181.3331
0.1404
5802.6593
0.2681
349.2410
0.1181
26
Methane
107.5045
0.0833
1724.6836
0.0797
394.4433
0.1333
27
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Hydrogen
475.0657
0.3679
957.7325
0.0442
938.7275
0.3173
29
Ethane
26.0279
0.0202
782.6557
0.0362
150.6697
0.0509
30
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
CO2
11.4565
0.0089
504.1985
0.0233
41.8302
0.0141
32
Nitrogen
321.1098
0.2487
8995.2496
0.4156
763.8269
0.2582
33
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
MEAmine
0.0005
0.0000
0.0277
0.0000
0.0019
0.0000
36
Ammonia
168.5154
0.1305
2869.8180
0.1326
318.9647
0.1078
37
Total
1291.3033
1.0000
21644.9682
1.0000
2958.3801
1.0000
38
K VALUE
39 40
COMPONENTS
MIXED
LIGHT
HEAVY
41
CO
---
---
---
42
H2O
---
---
---
43
Oxygen
---
---
---
44
Methane
---
---
---
---
---
---
45
H2S
46
Hydrogen
---
---
---
47
Ethane
---
---
---
48
Propane
---
---
---
49
CO2
---
---
---
50
Nitrogen
---
---
---
---
---
---
51
Air
52
Mercury
---
---
---
53
MEAmine
---
---
---
54
Ammonia
---
---
---
55
UNIT OPERATIONS
56 57 58
FEED TO
PRODUCT FROM
Mixer:
MIX-102 Recycle:
59
LOGICAL CONNECTION RCY-2
UTILITIES
60 61
( No utilities reference this stream )
62
PROCESS UTILITY
63 64 65
DYNAMICS
66 67
Pressure Specification
(Inactive):
68
Flow Specification
(Inactive) Molar:
69
Aspen Technology Inc. Licensed to: LEGENDS
* 4820 psia * Mass: 1291 lbmole/hr
2.164e+004 lb/hrStd Ideal Liq Volume:
Aspen HYSYS Version 8.8 (34.0.0.8909)
2958 barrel/day
Page 209 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 71 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
User Variables
10 11
NOTES
12 13 14
Description
15 16 17
Material Stream: 72
18 19 20
CONDITIONS
21 22
Overall
23
Vapour / Phase Fraction
24
Temperature:
25
Pressure:
26
Molar Flow
27
Mass Flow
28
Std Ideal Liq Vol Flow
29
Molar Enthalpy
(Btu/lbmole)
30
Molar Entropy
(Btu/lbmole-F)
31
Heat Flow
32
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
99.00*
99.00
(psia)
4820*
4820
168.5
168.5
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
2870
2870
319.0
319.0
-2.821e+004 19.63 -4.753e+006 320.9*
(barrel/day)
33
-2.821e+004 19.63 -4.753e+006 320.9
PROPERTIES
34 35
Overall
36
Molecular Weight
37
Molar Density
38
Mass Density
39
Act. Volume Flow
40
Liquid Phase 17.03
17.03
2.201
2.201
37.48
37.48
(barrel/day)
327.3
327.3
Mass Enthalpy
(Btu/lb)
-1656
-1656
41
Mass Entropy
(Btu/lb-F)
1.152
1.152
42
Heat Capacity
18.93
18.93
43
Mass Heat Capacity
44
LHV Molar Basis (Std)
(Btu/lbmole)
1.362e+005
1.362e+005
45
HHV Molar Basis (Std)
(Btu/lbmole)
1.627e+005
1.627e+005
46
HHV Mass Basis (Std)
47
CO2 Loading
48
CO2 App ML Con
49
CO2 App WT Con
50
LHV Mass Basis (Std)
51
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.112
9551
1.112
9551
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
7998
7998
Phase Fraction [Vol. Basis]
0.0000
1.000
52
Phase Fraction [Mass Basis]
0.0000
1.000
53
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
54
Mass Exergy
(Btu/lb)
163.9
---
55
Partial Pressure of CO2
(psia)
0.0000
---
56
Cost Based on Flow
(Cost/s)
0.0000
0.0000
57
Act. Gas Flow
58
Avg. Liq. Density
59 60 61
Std. Ideal Liq. Mass Density
62
Act. Liq. Flow
63
Z Factor
64
Watson K
65
User Property
66
Partial Pressure of H2S
67
(ACFM)
---
---
(lbmole/ft3)
2.258
2.258
Specific Heat
(Btu/lbmole-F)
18.93
18.93
Std. Gas Flow
(MMSCFD)
1.532
1.532
(lb/ft3)
38.46
38.46
(USGPS)
0.1591
0.1591
0.3653
0.3653
12.24
12.24
---
---
0.0000
---
Cp/(Cp - R)
1.117
1.117
68
Cp/Cv
2.169
2.169
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 210 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 72 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Heat of Vap.
13
Kinematic Viscosity
14
Liq. Mass Density (Std. Cond)
15
Liq. Vol. Flow (Std. Cond)
16
Liquid Fraction
17
Molar Volume
18
Mass Heat of Vap.
19
Phase Fraction [Molar Basis]
20
Surface Tension
21
Thermal Conductivity
22
Viscosity
23
Cv (Semi-Ideal)
24
Mass Cv (Semi-Ideal)
25
Cv
26
Mass Cv
27
Cv (Ent. Method)
28
Mass Cv (Ent. Method)
29
Cp/Cv (Ent. Method)
30
Reid VP at 37.8 C
31
True VP at 37.8 C
32
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
33
Viscosity Index
(Btu/lbmole)
Liquid Phase ---
---
(cSt)
0.1866
0.1866
(lb/ft3)
38.22
38.22
320.9
320.9
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4544
0.4544
-827.2
---
0.0000
1.0000
(dyne/cm)
23.13
23.13
(Btu/hr-ft-F)
0.2605
0.2605
0.1120
0.1120
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.94
16.94
0.9950
0.9950
8.726
8.726
0.5124
0.5124
---
---
---
---
---
---
(psia)
210.5
210.5
(psia)
210.5
210.5
320.9
320.9
---
---
34
COMPOSITION
35 36
Overall Phase
37 38
COMPONENTS
39
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
40
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
54
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
55
Liquid Phase
56 57
COMPONENTS
58
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
59
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 211 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 72 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
19
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
20
K VALUE
21 22
COMPONENTS
MIXED
LIGHT
HEAVY
23
CO
---
---
---
24
H2O
---
---
---
25
Oxygen
---
---
---
26
Methane
---
---
---
---
---
---
27
H2S
28
Hydrogen
---
---
---
29
Ethane
---
---
---
30
Propane
---
---
---
31
CO2
---
---
---
32
Nitrogen
---
---
---
---
---
---
33
Air
34
Mercury
---
---
---
35
MEAmine
---
---
---
36
Ammonia
0.0000
0.0000
---
37
UNIT OPERATIONS
38 39 40
FEED TO
PRODUCT FROM
Component Splitter:
X-101
Cooler:
LOGICAL CONNECTION E-106
41
UTILITIES
42 43
( No utilities reference this stream )
44
PROCESS UTILITY
45 46 47
DYNAMICS
48 49
Pressure Specification
(Active):
50
Flow Specification
(Inactive) Molar:
* 4820 psia
168.5 lbmole/hrMass:
51
2870 lb/hr Std Ideal Liq Volume:
319.0 barrel/day
User Variables
52 53
NOTES
54 55 56
Description
57 58 59
Material Stream: 73
60 61 62
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
63 64
Overall
65
Vapour / Phase Fraction
66
Temperature:
67
Pressure:
68
Molar Flow
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Liquid Phase 0.0000
1.0000
(F)
99.00
99.00
(psia)
4820*
4820
168.5
168.5
(lbmole/hr)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 212 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 73 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Mass Flow
13
Std Ideal Liq Vol Flow
14
Molar Enthalpy
(Btu/lbmole)
15
Molar Entropy
(Btu/lbmole-F)
16
Heat Flow
17
Liq Vol Flow @Std Cond
(lb/hr) (barrel/day)
(Btu/hr)
Liquid Phase 2870
2870
319.0
319.0
-2.821e+004 19.63 -4.753e+006 320.9*
(barrel/day)
18
-2.821e+004 19.63 -4.753e+006 320.9
PROPERTIES
19 20
Overall
21
Molecular Weight
22
Molar Density
23
Mass Density
24
Act. Volume Flow
25
Liquid Phase 17.03
17.03
2.201
2.201
37.48
37.48
(barrel/day)
327.3
327.3
Mass Enthalpy
(Btu/lb)
-1656
-1656
26
Mass Entropy
(Btu/lb-F)
1.152
1.152
27
Heat Capacity
18.93
18.93
28
Mass Heat Capacity
29
LHV Molar Basis (Std)
(Btu/lbmole)
1.362e+005
1.362e+005
30
HHV Molar Basis (Std)
(Btu/lbmole)
1.627e+005
1.627e+005
31
HHV Mass Basis (Std)
32
CO2 Loading
33
CO2 App ML Con
34
CO2 App WT Con
35
LHV Mass Basis (Std)
36
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.112
9551
1.112
9551
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
7998
7998
Phase Fraction [Vol. Basis]
0.0000
1.000
37
Phase Fraction [Mass Basis]
0.0000
1.000
38
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
39
Mass Exergy
(Btu/lb)
163.9
---
40
Partial Pressure of CO2
(psia)
0.0000
---
41
Cost Based on Flow
(Cost/s)
0.0000
0.0000
42
Act. Gas Flow
43
Avg. Liq. Density
44 45 46
Std. Ideal Liq. Mass Density
47
Act. Liq. Flow
48
Z Factor
49
Watson K
50
User Property
51
Partial Pressure of H2S
52
Cp/(Cp - R)
53
Cp/Cv
54
Heat of Vap.
55
Kinematic Viscosity
56
Liq. Mass Density (Std. Cond)
57
Liq. Vol. Flow (Std. Cond)
58
Liquid Fraction
59
Molar Volume
60
Mass Heat of Vap.
61
Phase Fraction [Molar Basis]
62
Surface Tension
63
Thermal Conductivity
64
Viscosity
65
Cv (Semi-Ideal)
66
Mass Cv (Semi-Ideal)
67
Cv
68
Mass Cv
69
Fluid Package:
(ACFM)
---
---
(lbmole/ft3)
2.258
2.258
Specific Heat
(Btu/lbmole-F)
18.93
18.93
Std. Gas Flow
(MMSCFD)
1.532
1.532
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
38.46
38.46
(USGPS)
0.1591
0.1591
0.3653
0.3653
12.24
12.24
---
---
(psia)
(Btu/lbmole)
0.0000
---
1.117
1.117
2.169
2.169
---
---
(cSt)
0.1866
0.1866
(lb/ft3)
38.22
38.22
320.9
320.9
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4544
0.4544
-827.2
---
0.0000
1.0000
(dyne/cm)
23.13
23.13
(Btu/hr-ft-F)
0.2605
0.2605
0.1120
0.1120
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.94
16.94
0.9950
0.9950
8.726
8.726
0.5124
0.5124
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 213 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 73 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Ent. Method)
13
Mass Cv (Ent. Method)
14
Cp/Cv (Ent. Method)
15
Reid VP at 37.8 C
16
True VP at 37.8 C
17
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
18
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F)
Liquid Phase ---
---
---
---
---
---
(psia)
210.5
210.5
(psia)
210.5
210.5
320.9
320.9
---
---
19
COMPOSITION
20 21
Overall Phase
22 23
COMPONENTS
24
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
25
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
39
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
40
Liquid Phase
41 42
COMPONENTS
43
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
44
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
58
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
59
K VALUE
60 61
COMPONENTS
MIXED
LIGHT
HEAVY
62
CO
---
---
---
63
H2O
---
---
---
64
Oxygen
---
---
---
65
Methane
---
---
---
---
---
-----
66
H2S
67
Hydrogen
---
---
68
Ethane
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 214 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 73 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
Propane
---
---
---
13
CO2
---
---
---
14
Nitrogen
---
---
---
---
---
---
15
Air
16
Mercury
---
---
---
17
MEAmine
---
---
---
18
Ammonia
0.0000
0.0000
---
19
UNIT OPERATIONS
20 21 22
FEED TO
PRODUCT FROM
Mixer:
MIX-103 Component Splitter:
23
LOGICAL CONNECTION X-101
UTILITIES
24 25
( No utilities reference this stream )
26
PROCESS UTILITY
27 28 29
DYNAMICS
30 31
Pressure Specification
(Active):
32
Flow Specification
(Inactive) Molar:
* 4820 psia
168.5 lbmole/hrMass:
33
2870 lb/hr Std Ideal Liq Volume:
319.0 barrel/day
User Variables
34 35
NOTES
36 37 38
Description
39 40 41
Material Stream: 74
42 43 44
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
45 46
Overall
47
Vapour / Phase Fraction
48
Temperature:
49
Pressure:
50
Molar Flow
51
Mass Flow
52
Std Ideal Liq Vol Flow
(barrel/day)
53
Molar Enthalpy
(Btu/lbmole)
54
Molar Entropy
(Btu/lbmole-F)
55
Heat Flow
56
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
99.00*
99.00
(psia)
4820*
4820
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
0.0000 -2.821e+004
0.0000 -2.821e+004
19.63
19.63
(Btu/hr)
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
57
PROPERTIES
58 59
Overall
60
Molecular Weight
61
Molar Density
62
Mass Density
63
Act. Volume Flow
64 65 66
Heat Capacity
67
Mass Heat Capacity
68
LHV Molar Basis (Std)
69
Fluid Package:
(lbmole/ft3)
17.03
2.201
2.201
37.48
37.48
(barrel/day)
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-1656
-1656
Mass Entropy
(Btu/lb-F)
1.152
1.152
18.93
18.93
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
Liquid Phase 17.03
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole)
1.112 1.362e+005
1.112 1.362e+005
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 215 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 74 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
HHV Molar Basis (Std)
13
HHV Mass Basis (Std)
14
CO2 Loading
15
CO2 App ML Con
16
CO2 App WT Con
17
LHV Mass Basis (Std)
18 19
(Btu/lbmole) (Btu/lb)
Liquid Phase
1.627e+005
1.627e+005
9551
9551
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7998
7998
Phase Fraction [Vol. Basis]
0.0000
1.000
Phase Fraction [Mass Basis]
0.0000
1.000
20
Phase Fraction [Act. Vol. Basis]
0.0000
---
21
Mass Exergy
(Btu/lb)
163.9
---
22
Partial Pressure of CO2
(psia)
0.0000
---
23
Cost Based on Flow
(Cost/s)
0.0000
0.0000
24
Act. Gas Flow
---
25
Avg. Liq. Density
26
(ACFM)
---
(lbmole/ft3)
---
---
Specific Heat
(Btu/lbmole-F)
18.93
18.93
27
Std. Gas Flow
(MMSCFD)
0.0000
0.0000
28
Std. Ideal Liq. Mass Density
29
Act. Liq. Flow
30
Z Factor
31
Watson K
32
User Property
33
Partial Pressure of H2S
34
Cp/(Cp - R)
35
Cp/Cv
36
Heat of Vap.
37
Kinematic Viscosity
38
Liq. Mass Density (Std. Cond)
39
Liq. Vol. Flow (Std. Cond)
40
Liquid Fraction
41
Molar Volume
42
Mass Heat of Vap.
43
Phase Fraction [Molar Basis]
44
Surface Tension
45
Thermal Conductivity
46
Viscosity
47
Cv (Semi-Ideal)
48
Mass Cv (Semi-Ideal)
49
Cv
50
Mass Cv
51
Cv (Ent. Method)
52
Mass Cv (Ent. Method)
53
Cp/Cv (Ent. Method)
54
Reid VP at 37.8 C
(psia)
55
True VP at 37.8 C
(psia)
56
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
57
Viscosity Index
(lb/ft3)
38.46
38.46
(USGPS)
0.0000
0.0000
0.3653
0.3653
12.24
12.24
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
0.0000
---
1.117
1.117
2.169
2.169
---
---
0.1866
0.1866
38.22
38.22
(barrel/day)
0.0000
0.0000
1.000
1.000
(ft3/lbmole)
0.4544
0.4544
(Btu/lb)
-827.2
---
0.0000
1.0000
(dyne/cm)
23.13
23.13
(Btu/hr-ft-F)
0.2605
0.2605
0.1120
0.1120
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.94
16.94
0.9950
0.9950
8.726
8.726
0.5124
0.5124
---
---
---
---
---
---
210.5
210.5
210.5
210.5
0.0000
0.0000
---
---
58
COMPOSITION
59 60
Overall Phase
61 62
COMPONENTS
63
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
64
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 216 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 74 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Ammonia
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
24
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
25
Liquid Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
43
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
44
K VALUE
45 46
COMPONENTS
MIXED
LIGHT
HEAVY
47
CO
---
---
---
48
H2O
---
---
---
49
Oxygen
---
---
---
50
Methane
---
---
---
---
---
---
51
H2S
52
Hydrogen
---
---
---
53
Ethane
---
---
---
54
Propane
---
---
---
55
CO2
---
---
---
56
Nitrogen
---
---
---
---
---
---
57
Air
58
Mercury
---
---
---
59
MEAmine
---
---
---
60
Ammonia
0.0000
0.0000
---
61
UNIT OPERATIONS
62 63
FEED TO
64
PRODUCT FROM Component Splitter:
65
LOGICAL CONNECTION X-101
UTILITIES
66 67
( No utilities reference this stream )
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 217 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 74 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROCESS UTILITY
10 11 12
DYNAMICS
13 14
Pressure Specification
(Active):
15
Flow Specification
(Inactive) Molar:
* 4820 psia
0.0000 lbmole/hrMass:
16
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
17 18
NOTES
19 20 21
Description
22 23 24
Material Stream: 75
25 26 27
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
28 29
Overall
30
Vapour / Phase Fraction
31
Temperature:
32
Pressure:
33
Molar Flow
34
Mass Flow
35
Std Ideal Liq Vol Flow
(barrel/day)
36
Molar Enthalpy
(Btu/lbmole)
37
Molar Entropy
(Btu/lbmole-F)
38
Heat Flow
39
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
90.98
90.98
(psia)
4565
4565
512.0
512.0
8974
8974
(lbmole/hr) (lb/hr)
(Btu/hr)
1011 -2.901e+004 20.67 -1.485e+007 1040*
(barrel/day)
40
1011 -2.901e+004 20.67 -1.485e+007 1040
PROPERTIES
41 42
Overall
Liquid Phase
43
Molecular Weight
44
Molar Density
45
Mass Density
46
Act. Volume Flow
47
Mass Enthalpy
48
Mass Entropy
49
Heat Capacity
50
Mass Heat Capacity
51
LHV Molar Basis (Std)
(Btu/lbmole)
1.384e+005
1.384e+005
52
HHV Molar Basis (Std)
(Btu/lbmole)
1.641e+005
1.641e+005
53
HHV Mass Basis (Std)
54
CO2 Loading
55
CO2 App ML Con
(lbmole/ft3)
1.691e-002
1.691e-002
56
CO2 App WT Con
(lbmol/lb)
4.616e-004
4.616e-004
57
LHV Mass Basis (Std)
58
(lbmole/ft3) (lb/ft3)
17.53
17.53
2.090
2.090
36.64
36.64
(barrel/day)
1047
1047
(Btu/lb)
-1655
-1655
(Btu/lb-F)
1.179
1.179
18.77
18.77
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.071
1.071
9364
9364
20.97
20.97
7894
7894
Phase Fraction [Vol. Basis]
0.0000
1.000
59
Phase Fraction [Mass Basis]
0.0000
1.000
60
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
61
Mass Exergy
(Btu/lb)
176.0
---
62
Partial Pressure of CO2
(psia)
0.0000
---
63
Cost Based on Flow
(Cost/s)
0.0000
0.0000
64
Act. Gas Flow
65
Avg. Liq. Density
66 67 68
Std. Ideal Liq. Mass Density
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
2.164
2.164
Specific Heat
(Btu/lbmole-F)
18.77
18.77
Std. Gas Flow
(MMSCFD)
4.654
4.654
37.92
37.92
Licensed to: LEGENDS
(lb/ft3)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 218 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 75 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Act. Liq. Flow
13
Z Factor
14
Watson K
15
User Property
16
Partial Pressure of H2S
17
Cp/(Cp - R)
18
Cp/Cv
19
Heat of Vap.
20
Kinematic Viscosity
21
Liq. Mass Density (Std. Cond)
22
Liq. Vol. Flow (Std. Cond)
23
Liquid Fraction
24
Molar Volume
25
Mass Heat of Vap.
26
Phase Fraction [Molar Basis]
27
Surface Tension
28
Thermal Conductivity
29
Viscosity
30
Cv (Semi-Ideal)
31
Mass Cv (Semi-Ideal)
32
Cv
33
Mass Cv
34
Cv (Ent. Method)
35
Mass Cv (Ent. Method)
36
Cp/Cv (Ent. Method)
37
Reid VP at 37.8 C
(psia)
38
True VP at 37.8 C
(psia)
39
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
40
Viscosity Index
(USGPS)
(psia)
(Btu/lbmole)
Liquid Phase 0.5089
0.5089
0.3695
0.3695
12.20
12.20
---
---
0.0000
---
1.118
1.118
2.009
2.009
---
---
(cSt)
0.1720
0.1720
(lb/ft3)
36.90
36.90
(barrel/day)
1040
1040
1.000
1.000
(ft3/lbmole)
0.4784
0.4784
(Btu/lb)
-803.7
---
0.0000
1.0000
(dyne/cm)
22.70
22.70
(Btu/hr-ft-F)
0.2383
0.2383
0.1010
0.1010
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.78
16.78
0.9574
0.9574
9.343
9.343
0.5331
0.5331
8.428
8.428
0.4808
0.4808
2.227
2.227
407.7
407.7
2750
2750
1040
1040
---
---
41
COMPOSITION
42 43
Overall Phase
44 45
COMPONENTS
46
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
47
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
48
H2O
3.3148
0.0065
59.7169
0.0067
4.0972
0.0041
49
Oxygen
9.5615
0.0187
305.9667
0.0341
18.4150
0.0182
50
Methane
6.9652
0.0136
111.7423
0.0125
25.5560
0.0253
51
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
Hydrogen
7.9795
0.0156
16.0867
0.0018
15.7675
0.0156
53
Ethane
5.5617
0.0109
167.2411
0.0186
32.1957
0.0318
54
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
CO2
4.1418
0.0081
182.2807
0.0203
15.1227
0.0150
56
Nitrogen
3.8311
0.0075
107.3196
0.0120
9.1130
0.0090
57
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
MEAmine
0.1976
0.0004
12.0674
0.0013
0.8125
0.0008
60
Ammonia
470.4139
0.9188
8011.1497
0.8927
890.3957
0.8803
61
Total
511.9730
1.0000
8973.7359
1.0000
1011.4894
1.0000
62
Liquid Phase
63 64
COMPONENTS
65
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
66
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
67
H2O
3.3148
0.0065
59.7169
0.0067
4.0972
0.0041
68
Oxygen
9.5615
0.0187
305.9667
0.0341
18.4150
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0182
Page 219 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 75 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Methane
6.9652
0.0136
111.7423
0.0125
25.5560
0.0253
16
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Hydrogen
7.9795
0.0156
16.0867
0.0018
15.7675
0.0156
18
Ethane
5.5617
0.0109
167.2411
0.0186
32.1957
0.0318
19
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
CO2
4.1418
0.0081
182.2807
0.0203
15.1227
0.0150
21
Nitrogen
3.8311
0.0075
107.3196
0.0120
9.1130
0.0090
22
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
MEAmine
0.1976
0.0004
12.0674
0.0013
0.8125
0.0008
25
Ammonia
470.4139
0.9188
8011.1497
0.8927
890.3957
0.8803
26
Total
511.9730
1.0000
8973.7359
1.0000
1011.4894
1.0000
27
K VALUE
28 29
COMPONENTS
MIXED
LIGHT
HEAVY
30
CO
0.0000
0.0000
---
31
H2O
0.0000
0.0000
---
32
Oxygen
0.0000
0.0000
---
33
Methane
0.0000
0.0000
---
---
---
---
34
H2S
35
Hydrogen
0.0000
0.0000
---
36
Ethane
0.0000
0.0000
---
37
Propane
---
---
---
38
CO2
0.0000
0.0000
---
39
Nitrogen
0.0000
0.0000
---
---
---
---
40
Air
41
Mercury
---
---
---
42
MEAmine
0.0000
0.0000
---
43
Ammonia
0.0000
0.0000
---
44
UNIT OPERATIONS
45 46 47
FEED TO
PRODUCT FROM
Valve:
VLV-102 Mixer:
48
LOGICAL CONNECTION MIX-103
UTILITIES
49 50
( No utilities reference this stream )
51
PROCESS UTILITY
52 53 54
DYNAMICS
55 56
Pressure Specification
(Inactive):
57
Flow Specification
(Inactive) Molar:
58
4565 psia 512.0 lbmole/hrMass:
8974 lb/hr Std Ideal Liq Volume:
1011 barrel/day
User Variables
59 60
NOTES
61 62 63
Description
64 65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 220 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 76
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0728
0.0728
0.9272
(F)
90.84
90.84
90.84
(psia)
579.7*
579.7
579.7
512.0
37.26
474.7
8974
693.0
8281
1011
86.59
924.9
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-2.901e+004 21.45 -1.485e+007 1040*
(barrel/day)
22
-1.541e+004 33.22 -5.744e+005 6.015e+004
-3.008e+004 20.53 -1.428e+007 926.0
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase
Liquid Phase
17.53
18.60
17.44
0.9015
0.1088
2.104
15.80
2.024
36.71
(barrel/day)
2428
1463
964.3
Mass Enthalpy
(Btu/lb)
-1655
-828.9
-1724
30
Mass Entropy
(Btu/lb-F)
1.224
1.786
1.177
31
Heat Capacity
19.92
9.204
20.76
32
Mass Heat Capacity
1.136
0.4949
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.384e+005
1.301e+005
1.390e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.641e+005
1.491e+005
1.653e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
8.560e-002
8.560e-002
0.9144
41
Phase Fraction [Mass Basis]
7.722e-002
7.722e-002
0.9228
42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.190
9364
8017
9477
---
---
17.58
(lbmole/ft3)
---
---
1.540e-002
(lbmol/lb)
---
---
4.195e-004
(Btu/lb)
7894
6997
7969
0.6028
0.6028
0.3972
(Btu/lb)
152.0
---
---
(psia)
10.40
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
5.706
5.706
---
(lbmole/ft3)
2.164
1.840
2.194
Specific Heat
(Btu/lbmole-F)
19.92
9.204
20.76
Std. Gas Flow
(MMSCFD)
4.654
0.3387
4.315
(lb/ft3)
37.92
34.21
38.27
(USGPS)
0.4687
---
0.4687
Licensed to: LEGENDS
(psia)
(Btu/lbmole)
---
0.9015
12.20
11.15
12.26
---
---
---
0.0000
---
---
1.111
1.275
1.106
1.022
1.505
2.315
1.592e+004
4.663e-002
---
---
0.4047
0.1900
(cSt)
---
(lb/ft3)
36.90
4.925e-002
38.23
1040
6.015e+004
926.0
(barrel/day) (ft3/lbmole) (Btu/lb)
0.9272
0.0000
1.000
1.109
9.187
0.4752
908.5
---
---
0.0728
0.0728
0.9272
(dyne/cm)
23.80
(Btu/hr-ft-F)
---
(cP)
---
---
23.80
2.664e-002
0.2547
1.312e-002
0.1117
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 221 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 76 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Liquid Phase
17.93
7.218
18.78
1.023
0.3881
1.076
19.49
6.114
8.970
1.112
0.3288
0.5142
---
---
5.381
(Btu/lb-F)
---
---
0.3085
---
---
3.859
Reid VP at 37.8 C
(psia)
407.7
---
269.3
20
True VP at 37.8 C
(psia)
2750
---
590.3
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
6.107e+004 ---
6.015e+004 ---
23
926.0 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0728
LIQUID VOLUME FRACTION
29
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
30
H2O
3.3148
0.0065
59.7169
0.0067
4.0972
0.0041
31
Oxygen
9.5615
0.0187
305.9667
0.0341
18.4150
0.0182
32
Methane
6.9652
0.0136
111.7423
0.0125
25.5560
0.0253
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
7.9795
0.0156
16.0867
0.0018
15.7675
0.0156
35
Ethane
5.5617
0.0109
167.2411
0.0186
32.1957
0.0318
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
4.1418
0.0081
182.2807
0.0203
15.1227
0.0150
38
Nitrogen
3.8311
0.0075
107.3196
0.0120
9.1130
0.0090
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1976
0.0004
12.0674
0.0013
0.8125
0.0008
42
Ammonia
470.4139
0.9188
8011.1497
0.8927
890.3957
0.8803
43
Total
511.9730
1.0000
8973.7359
1.0000
1011.4894
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
7.278e-002 LIQUID VOLUME FRACTION
48
CO
0.0051
0.0001
0.1420
0.0002
0.0122
0.0001
49
H2O
0.0003
0.0000
0.0046
0.0000
0.0003
0.0000
50
Oxygen
6.5747
0.1764
210.3910
0.3036
12.6627
0.1462
51
Methane
4.2266
0.1134
67.8069
0.0978
15.5078
0.1791
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
7.2567
0.1947
14.6295
0.0211
14.3392
0.1656
54
Ethane
1.2394
0.0333
37.2682
0.0538
7.1745
0.0829
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6684
0.0179
29.4143
0.0424
2.4403
0.0282
57
Nitrogen
3.5360
0.0949
99.0533
0.1429
8.4111
0.0971
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
61
Ammonia
13.7564
0.3692
234.2714
0.3381
26.0380
0.3007
62
Total
37.2635
1.0000
692.9812
1.0000
86.5860
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0008
0.0000
0.0228
0.0000
0.0020
68
H2O
3.3146
0.0070
59.7123
0.0072
4.0969
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.9272 LIQUID VOLUME FRACTION 0.0000 0.0044
Page 222 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 76 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9272 LIQUID VOLUME FRACTION
15
Oxygen
2.9867
0.0063
95.5757
0.0115
5.7524
0.0062
16
Methane
2.7386
0.0058
43.9354
0.0053
10.0482
0.0109
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.7228
0.0015
1.4572
0.0002
1.4283
0.0015
19
Ethane
4.3224
0.0091
129.9730
0.0157
25.0212
0.0271
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
3.4735
0.0073
152.8664
0.0185
12.6824
0.0137
22
Nitrogen
0.2951
0.0006
8.2663
0.0010
0.7019
0.0008
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
26
Ammonia
456.6575
0.9620
7776.8783
0.9392
864.3577
0.9345
27
Total
474.7096
1.0000
8280.7547
1.0000
924.9034
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
28.04
28.04
---
34
Methane
19.66
19.66
---
---
---
---
35
79.22
79.22
9.790e-004
H2S
---
9.790e-004
---
36
Hydrogen
127.9
127.9
---
37
Ethane
3.653
3.653
---
38
Propane
---
---
---
39
CO2
2.451
2.451
---
40
Nitrogen
152.7
152.7
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
1.015e-004 0.3838
45
---
0.3838
---
UNIT OPERATIONS
46 47 48
1.015e-004
FEED TO
PRODUCT FROM
Separator:
D-6
49
Valve:
LOGICAL CONNECTION VLV-102
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Active):
58
Flow Specification
(Inactive) Molar:
59
* 579.7 psia
512.0 lbmole/hrMass:
8974 lb/hr Std Ideal Liq Volume:
1011 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 223 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 77
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
1.0000
1.0000
0.0000
(F)
90.84
90.84
90.84
(psia)
579.7
579.7
579.7
37.26
37.26
0.0000
693.0
693.0
0.0000
86.59
86.59
(lbmole/hr) (lb/hr)
-1.541e+004 33.22
-1.541e+004 33.22
0.0000 -3.008e+004 20.53
(Btu/hr)
-5.744e+005
-5.744e+005
0.0000
(barrel/day)
* 6.015e+004
6.015e+004
0.0000
22
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29 30 31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.301e+005
1.301e+005
1.390e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.491e+005
1.491e+005
1.653e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41 42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48
Specific Heat
(Btu/lbmole-F)
9.204
9.204
20.76
49
Std. Gas Flow
(MMSCFD)
0.3387
0.3387
0.0000
50
Std. Ideal Liq. Mass Density
(lb/ft3)
34.21
34.21
38.27
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
---
0.9015
53
Watson K
11.15
11.15
12.26
54
User Property
---
---
---
55
Partial Pressure of H2S
0.0000
---
---
56
Cp/(Cp - R)
1.275
1.275
1.106
57
Cp/Cv
1.505
1.505
2.315
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
18.60
18.60
17.44
0.1088
0.1088
2.104
2.024
2.024
36.71
(barrel/day)
1463
1463
0.0000
Mass Enthalpy
(Btu/lb)
-828.9
-828.9
-1724
Mass Entropy
(Btu/lb-F)
1.786
1.786
1.177
9.204
9.204
20.76
0.4949
0.4949
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
8017
8017
9477
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
6997
6997
7969
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
Licensed to: LEGENDS
(Btu/lb)
1.190
1.000
1.000
0.0000
(Btu/lb)
204.7
---
---
(psia)
10.40
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
5.706
5.706
---
(lbmole/ft3)
1.840
1.840
2.194
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP)
1.027e+004 0.4047
--4.663e-002
---
---
0.4047
0.1900
4.925e-002
4.925e-002
38.23
6.015e+004
6.015e+004
0.0000
0.0000
0.0000
1.000
9.187
9.187
0.4752
552.4
---
---
1.0000
1.0000
0.0000
---
---
23.80
2.664e-002
2.664e-002
0.2547
1.312e-002
1.312e-002
0.1117
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 224 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 77 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
7.218
7.218
18.78
0.3881
0.3881
1.076
6.114
6.114
8.970
0.3288
0.3288
0.5142
---
---
5.381
---
---
0.3085
---
---
3.859
---
---
269.3
---
---
6.015e+004 ---
6.015e+004 ---
23
590.3 0.0000 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.0051
0.0001
0.1420
0.0002
0.0122
0.0001
30
H2O
0.0003
0.0000
0.0046
0.0000
0.0003
0.0000
31
Oxygen
6.5747
0.1764
210.3910
0.3036
12.6627
0.1462
32
Methane
4.2266
0.1134
67.8069
0.0978
15.5078
0.1791
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
7.2567
0.1947
14.6295
0.0211
14.3392
0.1656
35
Ethane
1.2394
0.0333
37.2682
0.0538
7.1745
0.0829
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.6684
0.0179
29.4143
0.0424
2.4403
0.0282
38
Nitrogen
3.5360
0.0949
99.0533
0.1429
8.4111
0.0971
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
42
Ammonia
13.7564
0.3692
234.2714
0.3381
26.0380
0.3007
43
Total
37.2635
1.0000
692.9812
1.0000
86.5860
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0051
0.0001
0.1420
0.0002
0.0122
0.0001
49
H2O
0.0003
0.0000
0.0046
0.0000
0.0003
0.0000
50
Oxygen
6.5747
0.1764
210.3910
0.3036
12.6627
0.1462
51
Methane
4.2266
0.1134
67.8069
0.0978
15.5078
0.1791
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
7.2567
0.1947
14.6295
0.0211
14.3392
0.1656
54
Ethane
1.2394
0.0333
37.2682
0.0538
7.1745
0.0829
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6684
0.0179
29.4143
0.0424
2.4403
0.0282
57
Nitrogen
3.5360
0.0949
99.0533
0.1429
8.4111
0.0971
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
61
Ammonia
13.7564
0.3692
234.2714
0.3381
26.0380
0.3007
62
Total
37.2635
1.0000
692.9812
1.0000
86.5860
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
0.0000
0.0070
0.0000
0.0072
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000 LIQUID VOLUME FRACTION 0.0000 0.0044
Page 225 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 77 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
Oxygen
0.0000
0.0063
0.0000
0.0115
0.0000
0.0062
16
Methane
0.0000
0.0058
0.0000
0.0053
0.0000
0.0109
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0000
0.0015
0.0000
0.0002
0.0000
0.0015
19
Ethane
0.0000
0.0091
0.0000
0.0157
0.0000
0.0271
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0000
0.0073
0.0000
0.0185
0.0000
0.0137
22
Nitrogen
0.0000
0.0006
0.0000
0.0010
0.0000
0.0008
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0000
0.0004
0.0000
0.0015
0.0000
0.0009
26
Ammonia
0.0000
0.9620
0.0000
0.9392
0.0000
0.9345
27
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
28.04
28.04
---
34
Methane
19.66
19.66
---
---
---
---
35
79.22
79.22
9.790e-004
H2S
---
9.790e-004
---
36
Hydrogen
127.9
127.9
---
37
Ethane
3.653
3.653
---
38
Propane
---
---
---
39
CO2
2.451
2.451
---
40
Nitrogen
152.7
152.7
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
1.015e-004 0.3838
45
---
0.3838
---
UNIT OPERATIONS
46 47 48
1.015e-004
FEED TO
PRODUCT FROM
Mixer:
MIX-104 Separator:
49
LOGICAL CONNECTION D-6
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
579.7 psia 37.26 lbmole/hrMass:
693.0 lb/hr Std Ideal Liq Volume:
86.59 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 226 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 78
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
90.84
90.84
90.84
(psia)
579.7
579.7
579.7
474.7
0.0000
474.7
8281
0.0000
8281
924.9
0.0000
924.9
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-3.008e+004 20.53 -1.428e+007 926.0*
(barrel/day)
22
-1.541e+004 33.22 0.0000 0.0000
-3.008e+004 20.53 -1.428e+007 926.0
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase
Liquid Phase
17.44
18.60
17.44
2.104
0.1088
2.104
36.71
2.024
36.71
(barrel/day)
964.3
0.0000
964.3
Mass Enthalpy
(Btu/lb)
-1724
-828.9
-1724
30
Mass Entropy
(Btu/lb-F)
1.177
1.786
1.177
31
Heat Capacity
20.76
9.204
20.76
32
Mass Heat Capacity
1.190
0.4949
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.390e+005
1.301e+005
1.390e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.653e+005
1.491e+005
1.653e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
1.540e-002
---
1.540e-002
38
CO2 App WT Con
(lbmol/lb)
4.195e-004
---
4.195e-004
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
41 42 43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.190
9477
8017
9477
17.58
---
17.58
7969
6997
7969
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
(Btu/lb)
140.9
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.194
1.840
2.194
Specific Heat
(Btu/lbmole-F)
20.76
9.204
20.76
Std. Gas Flow
(MMSCFD)
4.315
0.0000
4.315
(lb/ft3)
38.27
34.21
38.27
(USGPS)
0.4687
---
0.4687
Licensed to: LEGENDS
---
0.9015
12.26
11.15
12.26
---
---
---
0.0000
---
---
1.106
1.275
1.106
2.315
1.505
2.315
8988
---
---
(cSt)
0.1900
0.4047
0.1900
(lb/ft3)
38.23
(psia)
(Btu/lbmole)
(barrel/day) (ft3/lbmole) (Btu/lb)
4.925e-002
4.663e-002
38.23
926.0
0.0000
1.000
0.0000
926.0 1.000
0.4752
9.187
0.4752
515.2
---
---
0.0000
0.0000
1.0000
(dyne/cm)
23.80
(Btu/hr-ft-F)
0.2547
2.664e-002
0.2547
0.1117
1.312e-002
0.1117
(cP)
---
23.80
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 227 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 78 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
18.78
7.218
18.78
1.076
0.3881
1.076
8.970
6.114
8.970
0.5142
0.3288
0.5142
5.381
---
5.381
0.3085
---
0.3085
3.859
---
3.859
269.3
---
269.3
590.3
---
590.3
926.0
0.0000
926.0
---
---
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.0008
0.0000
0.0228
0.0000
0.0020
0.0000
30
H2O
3.3146
0.0070
59.7123
0.0072
4.0969
0.0044
31
Oxygen
2.9867
0.0063
95.5757
0.0115
5.7524
0.0062
32
Methane
2.7386
0.0058
43.9354
0.0053
10.0482
0.0109
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.7228
0.0015
1.4572
0.0002
1.4283
0.0015
35
Ethane
4.3224
0.0091
129.9730
0.0157
25.0212
0.0271
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
3.4735
0.0073
152.8664
0.0185
12.6824
0.0137
38
Nitrogen
0.2951
0.0006
8.2663
0.0010
0.7019
0.0008
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
42
Ammonia
456.6575
0.9620
7776.8783
0.9392
864.3577
0.9345
43
Total
474.7096
1.0000
8280.7547
1.0000
924.9034
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.1764
0.0000
0.3036
0.0000
0.1462
51
Methane
0.0000
0.1134
0.0000
0.0978
0.0000
0.1791
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.1947
0.0000
0.0211
0.0000
0.1656
54
Ethane
0.0000
0.0333
0.0000
0.0538
0.0000
0.0829
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0179
0.0000
0.0424
0.0000
0.0282
57
Nitrogen
0.0000
0.0949
0.0000
0.1429
0.0000
0.0971
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.3692
0.0000
0.3381
0.0000
0.3007
62
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0008
0.0000
0.0228
0.0000
0.0020
68
H2O
3.3146
0.0070
59.7123
0.0072
4.0969
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.000 LIQUID VOLUME FRACTION 0.0000 0.0044
Page 228 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 78 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Oxygen
2.9867
0.0063
95.5757
0.0115
5.7524
0.0062
16
Methane
2.7386
0.0058
43.9354
0.0053
10.0482
0.0109
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.7228
0.0015
1.4572
0.0002
1.4283
0.0015
19
Ethane
4.3224
0.0091
129.9730
0.0157
25.0212
0.0271
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
3.4735
0.0073
152.8664
0.0185
12.6824
0.0137
22
Nitrogen
0.2951
0.0006
8.2663
0.0010
0.7019
0.0008
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
26
Ammonia
456.6575
0.9620
7776.8783
0.9392
864.3577
0.9345
27
Total
474.7096
1.0000
8280.7547
1.0000
924.9034
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
28.04
28.04
---
34
Methane
19.66
19.66
---
---
---
---
35
79.22
79.22
9.790e-004
H2S
---
9.790e-004
---
36
Hydrogen
127.9
127.9
---
37
Ethane
3.653
3.653
---
38
Propane
---
---
---
39
CO2
2.451
2.451
---
40
Nitrogen
152.7
152.7
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
1.015e-004 0.3838
45
---
0.3838
---
UNIT OPERATIONS
46 47 48
1.015e-004
FEED TO
PRODUCT FROM
Valve:
VLV-103 Separator:
49
LOGICAL CONNECTION D-6
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
579.7 psia 474.7 lbmole/hrMass:
8281 lb/hr Std Ideal Liq Volume:
924.9 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 229 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 79
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Vapour Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
2069
2050
18
Molar Enthalpy
(Btu/lbmole)
-8420
-8168
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Liquid Phase
0.9888
0.9888
0.0112
(F)
30.80
30.80
30.80
(psia)
579.7
579.7
579.7
902.4
892.3
10.13
(lbmole/hr) (lb/hr)
1.519e+004
29.61
1.501e+004
29.74
(Btu/hr)
-7.598e+006
-7.289e+006
(barrel/day)
* 1.460e+006
1.443e+006
22
175.7 19.65 -3.058e+004 18.14 -3.097e+005 19.69
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-500.3
-485.5
-1762
30
Mass Entropy
(Btu/lb-F)
1.759
1.767
1.045
31
Heat Capacity
8.064
7.940
18.96
32
Mass Heat Capacity
0.4791
0.4719
33
LHV Molar Basis (Std)
(Btu/lbmole)
9.858e+004
9.812e+004
1.388e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.127e+005
1.121e+005
1.652e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
16.83
16.82
17.35
0.1160
0.1147
2.281
1.952
1.930
39.58
3.326e+004
3.324e+004
18.98
1.093
6698
6665
9519
---
---
252.0
(lbmole/ft3)
---
---
1.498e-002
(lbmol/lb)
---
---
3.786e-004
(Btu/lb)
5857
5832
Phase Fraction [Vol. Basis]
0.9905
0.9905
9.496e-003
41
Phase Fraction [Mass Basis]
0.9884
0.9884
1.157e-002
42
Phase Fraction [Act. Vol. Basis]
0.9994
0.9994
5.706e-004
43
Mass Exergy
(Btu/lb)
232.3
---
44
Partial Pressure of CO2
(psia)
5.407
---
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
8001
---
(ACFM)
129.6
129.6
---
(lbmole/ft3)
1.864
1.861
2.203
Specific Heat
(Btu/lbmole-F)
8.064
7.940
Std. Gas Flow
(MMSCFD)
8.203
8.111
31.38
31.31
Licensed to: LEGENDS
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
9.226e-003
(Btu/lb)
9.226e-003 4.829e-002
---
0.9599 10.42
12.26
---
---
---
0.0000
---
---
1.327
1.334
1.117
1.451
1.469
2.291
6672
---
---
---
0.4158
0.2542
4.448e-002
4.446e-002
38.14
1.460e+006
1.443e+006
19.69
8.623
0.0000
1.000
8.715
0.4384
396.4
---
---
0.9888
0.9888
0.0112
(dyne/cm)
31.44
(Btu/hr-ft-F)
---
(cP)
38.23
---
10.46
1.122e-002 (ft3/lbmole)
18.96 9.205e-002
---
---
31.44
3.163e-002
0.3003
1.286e-002
0.1612
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 230 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 79 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
6.078
5.954
16.98
0.3611
0.3539
0.9782
5.556
5.406
8.276
0.3302
0.3213
0.4769
---
---
7.024
---
---
0.4047
---
---
2.700
---
---
256.1
---
---
535.2
1.443e+006 ---
1.443e+006 ---
23
19.69 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9888
LIQUID VOLUME FRACTION
29
CO
0.1879
0.0002
5.2641
0.0003
0.4509
0.0002
30
H2O
0.0113
0.0000
0.2043
0.0000
0.0140
0.0000
31
Oxygen
127.8998
0.1417
4092.7930
0.2695
246.3303
0.1190
32
Methane
76.1493
0.0844
1221.6554
0.0804
279.3984
0.1350
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
326.1304
0.3614
657.4789
0.0433
644.4320
0.3114
35
Ethane
18.8221
0.0209
565.9774
0.0373
108.9568
0.0527
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
8.3890
0.0093
369.1980
0.0243
30.6300
0.0148
38
Nitrogen
218.7696
0.2424
6128.3941
0.4035
520.3894
0.2515
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0003
0.0000
0.0161
0.0000
0.0011
0.0000
42
Ammonia
126.0805
0.1397
2147.1509
0.1414
238.6441
0.1153
43
Total
902.4402
1.0000
15188.1323
1.0000
2069.2471
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9888 LIQUID VOLUME FRACTION
48
CO
0.1879
0.0002
5.2636
0.0004
0.4509
0.0002
49
H2O
0.0001
0.0000
0.0011
0.0000
0.0001
0.0000
50
Oxygen
127.8563
0.1433
4091.4026
0.2725
246.2467
0.1201
51
Methane
76.1105
0.0853
1221.0333
0.0813
279.2561
0.1362
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
326.1148
0.3655
657.4474
0.0438
644.4012
0.3144
54
Ethane
18.7457
0.0210
563.6823
0.0375
108.5149
0.0529
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
8.3225
0.0093
366.2700
0.0244
30.3871
0.0148
57
Nitrogen
218.7617
0.2452
6128.1726
0.4082
520.3706
0.2539
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
116.2143
0.1302
1979.1303
0.1318
219.9696
0.1073
62
Total
892.3139
1.0000
15012.4032
1.0000
2049.5970
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0005
0.0000
0.0000
68
H2O
0.0113
0.0011
0.2032
0.0012
0.0139
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.122e-002 LIQUID VOLUME FRACTION 0.0000 0.0007
Page 231 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 79 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.122e-002 LIQUID VOLUME FRACTION
15
Oxygen
0.0435
0.0043
1.3905
0.0079
0.0837
0.0043
16
Methane
0.0388
0.0038
0.6221
0.0035
0.1423
0.0072
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0156
0.0015
0.0315
0.0002
0.0309
0.0016
19
Ethane
0.0763
0.0075
2.2951
0.0131
0.4418
0.0225
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0665
0.0066
2.9280
0.0167
0.2429
0.0124
22
Nitrogen
0.0079
0.0008
0.2215
0.0013
0.0188
0.0010
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0003
0.0000
0.0161
0.0001
0.0011
0.0001
26
Ammonia
9.8662
0.9743
168.0206
0.9561
18.6746
0.9504
27
Total
10.1263
1.0000
175.7291
1.0000
19.6500
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
33.39
33.39
---
34
Methane
22.27
22.27
---
---
---
---
35
H2S
124.0
124.0
6.284e-005
---
6.284e-005
---
36
Hydrogen
236.9
236.9
---
37
Ethane
2.787
2.787
---
38
Propane
---
---
---
39
CO2
1.420
1.420
---
40
Nitrogen
313.9
313.9
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
45
3.801e-006
0.1337
---
0.1337
---
UNIT OPERATIONS
46 47 48
3.801e-006
FEED TO
PRODUCT FROM
Mixer:
MIX-107 Mixer:
49
LOGICAL CONNECTION MIX-104
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
579.7 psia 902.4 lbmole/hrMass:
1.519e+004 lb/hrStd Ideal Liq Volume:
2069 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 232 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 80
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0450
0.0450
0.9550
(F)
79.29
79.29
79.29
(psia)
229.7*
229.7
229.7
474.7
21.38
453.3
8281
423.1
7858
924.9
49.93
875.0
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-3.008e+004 20.62 -1.428e+007 926.0*
(barrel/day)
22
-2.368e+004 36.78 -5.063e+005 58.99
-3.038e+004 19.86 -1.377e+007 873.7
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase 17.44
(lbmole/ft3) (lb/ft3)
0.6827
19.79 4.403e-002
Liquid Phase 17.33 2.161
11.91
0.8712
37.47
(barrel/day)
2972
2076
896.5
Mass Enthalpy
(Btu/lb)
-1724
-1197
-1753
30
Mass Entropy
(Btu/lb-F)
1.182
1.859
1.146
31
Heat Capacity
19.96
9.556
20.45
32
Mass Heat Capacity
1.144
0.4829
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.390e+005
1.596e+005
1.380e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.653e+005
1.840e+005
1.644e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
5.399e-002
5.399e-002
0.9460
41
Phase Fraction [Mass Basis]
5.110e-002
5.110e-002
0.9489
42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.180
9477
9297
9487
---
---
14.19
(lbmole/ft3)
---
---
1.336e-002
(lbmol/lb)
---
---
3.567e-004
(Btu/lb)
7969
8065
7964
0.6984
0.6984
0.3016
(Btu/lb)
138.1
---
---
(psia)
7.202
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
8.094
8.094
---
(lbmole/ft3)
2.194
1.831
2.215
Specific Heat
(Btu/lbmole-F)
19.96
9.556
20.45
Std. Gas Flow
(MMSCFD)
4.315
0.1944
4.121
(lb/ft3)
38.27
36.22
38.39
(USGPS)
0.4358
---
0.4358
Licensed to: LEGENDS
(psia)
(Btu/lbmole)
---
0.9020
12.26
12.02
12.27
---
---
---
0.0000
---
---
1.110
1.262
1.108
1.010
1.434
2.319
1.781e+004
1.837e-002
---
---
(cSt)
---
0.7361
0.2063
(lb/ft3)
38.23
30.66
38.45
926.0
58.99
873.7
0.9550
0.0000
1.000
1.465
22.71
0.4626
(barrel/day) (ft3/lbmole) (Btu/lb)
1021
---
---
0.0450
0.0450
0.9550
(dyne/cm)
25.66
(Btu/hr-ft-F)
---
(cP)
---
---
25.66
1.775e-002
0.2688
1.027e-002
0.1238
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 233 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 80 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F)
Vapour Phase
Liquid Phase
17.98
7.570
18.47
1.030
0.3826
1.065
19.76
6.664
8.820
1.133
0.3368
0.5088
---
---
---
---
---
---
---
---
---
(psia)
269.3
1139
234.0
(psia)
590.3
4258
287.9
932.6
58.99
873.7
-95.12
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0450
LIQUID VOLUME FRACTION
29
CO
0.0008
0.0000
0.0228
0.0000
0.0020
0.0000
30
H2O
3.3146
0.0070
59.7123
0.0072
4.0969
0.0044
31
Oxygen
2.9867
0.0063
95.5757
0.0115
5.7524
0.0062
32
Methane
2.7386
0.0058
43.9354
0.0053
10.0482
0.0109
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.7228
0.0015
1.4572
0.0002
1.4283
0.0015
35
Ethane
4.3224
0.0091
129.9730
0.0157
25.0212
0.0271
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
3.4735
0.0073
152.8664
0.0185
12.6824
0.0137
38
Nitrogen
0.2951
0.0006
8.2663
0.0010
0.7019
0.0008
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
42
Ammonia
456.6575
0.9620
7776.8783
0.9392
864.3577
0.9345
43
Total
474.7096
1.0000
8280.7547
1.0000
924.9034
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
4.504e-002 LIQUID VOLUME FRACTION
48
CO
0.0007
0.0000
0.0208
0.0000
0.0018
0.0000
49
H2O
0.0002
0.0000
0.0030
0.0000
0.0002
0.0000
50
Oxygen
2.3046
0.1078
73.7467
0.1743
4.4385
0.0889
51
Methane
1.9138
0.0895
30.7036
0.0726
7.0221
0.1406
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.6839
0.0320
1.3788
0.0033
1.3514
0.0271
54
Ethane
1.1831
0.0553
35.5767
0.0841
6.8489
0.1372
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6704
0.0314
29.5045
0.0697
2.4478
0.0490
57
Nitrogen
0.2817
0.0132
7.8902
0.0186
0.6700
0.0134
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
14.3442
0.6708
244.2812
0.5774
27.1505
0.5438
62
Total
21.3826
1.0000
423.1056
1.0000
49.9312
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0001
0.0000
0.0020
0.0000
0.0002
68
H2O
3.3144
0.0073
59.7093
0.0076
4.0967
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.9550 LIQUID VOLUME FRACTION 0.0000 0.0047
Page 234 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 80 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9550 LIQUID VOLUME FRACTION
15
Oxygen
0.6822
0.0015
21.8290
0.0028
1.3138
0.0015
16
Methane
0.8248
0.0018
13.2318
0.0017
3.0262
0.0035
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0389
0.0001
0.0784
0.0000
0.0769
0.0001
19
Ethane
3.1392
0.0069
94.3963
0.0120
18.1723
0.0208
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
2.8031
0.0062
123.3618
0.0157
10.2345
0.0117
22
Nitrogen
0.0134
0.0000
0.3761
0.0000
0.0319
0.0000
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
26
Ammonia
442.3134
0.9757
7532.5971
0.9586
837.2072
0.9568
27
Total
453.3270
1.0000
7857.6491
1.0000
874.9722
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
71.62
71.62
---
34
Methane
49.19
49.19
---
---
---
---
35
218.0
218.0
1.068e-003
H2S
---
1.068e-003
---
36
Hydrogen
372.7
372.7
---
37
Ethane
7.990
7.990
---
38
Propane
---
---
---
39
CO2
5.071
5.071
---
40
Nitrogen
444.8
444.8
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
8.673e-005 0.6875
45
---
0.6875
---
UNIT OPERATIONS
46 47 48
8.673e-005
FEED TO
PRODUCT FROM
Separator:
D-7
49
Valve:
LOGICAL CONNECTION VLV-103
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Active):
58
Flow Specification
(Inactive) Molar:
59
* 229.7 psia
474.7 lbmole/hrMass:
8281 lb/hr Std Ideal Liq Volume:
924.9 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 235 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 81
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
1.0000
1.0000
0.0000
(F)
79.29
79.29
79.29
(psia)
229.7
229.7
229.7
21.38
21.38
0.0000
423.1
423.1
0.0000
49.93
49.93
(lbmole/hr) (lb/hr)
(Btu/hr)
-2.368e+004 36.78 -5.063e+005 58.99*
(barrel/day)
22
-2.368e+004 36.78 -5.063e+005 58.99
0.0000 -3.038e+004 19.86 0.0000 0.0000
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29 30 31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.596e+005
1.596e+005
1.380e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.840e+005
1.840e+005
1.644e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41 42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48
Specific Heat
(Btu/lbmole-F)
9.556
9.556
20.45
49
Std. Gas Flow
(MMSCFD)
0.1944
0.1944
0.0000
50
Std. Ideal Liq. Mass Density
(lb/ft3)
36.22
36.22
38.39
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
---
0.9020
53
Watson K
12.02
12.02
12.27
54
User Property
---
---
---
55
Partial Pressure of H2S
0.0000
---
---
56
Cp/(Cp - R)
1.262
1.262
1.108
57
Cp/Cv
1.434
1.434
2.319
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
19.79 (lbmole/ft3) (lb/ft3)
4.403e-002
19.79 4.403e-002
17.33 2.161
0.8712
0.8712
37.47
(barrel/day)
2076
2076
0.0000
Mass Enthalpy
(Btu/lb)
-1197
-1197
-1753
Mass Entropy
(Btu/lb-F)
1.859
1.859
1.146
9.556
9.556
20.45
0.4829
0.4829
(Btu/lbmole-F) (Btu/lb-F)
9297
9297
9487
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
8065
8065
7964
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
Licensed to: LEGENDS
(Btu/lb)
1.180
1.000
1.000
0.0000
(Btu/lb)
143.2
---
---
(psia)
7.202
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
8.094
8.094
---
(lbmole/ft3)
1.831
1.831
2.215
(psia)
(Btu/lbmole)
1.458e+004
--1.837e-002
---
--0.2063
(cSt)
0.7361
0.7361
(lb/ft3)
30.66
30.66
38.45
58.99
58.99
0.0000
0.0000
0.0000
1.000
22.71
22.71
0.4626
(barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP)
736.9
---
---
1.0000
1.0000
0.0000
---
---
25.66
1.775e-002
1.775e-002
0.2688
1.027e-002
1.027e-002
0.1238
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 236 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 81 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
7.570
7.570
18.47
0.3826
0.3826
1.065
6.664
6.664
8.820
0.3368
0.3368
0.5088
---
---
---
---
---
---
---
---
---
1139
1139
234.0
4258
4258
287.9
58.99
58.99
0.0000
---
---
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.0007
0.0000
0.0208
0.0000
0.0018
0.0000
30
H2O
0.0002
0.0000
0.0030
0.0000
0.0002
0.0000
31
Oxygen
2.3046
0.1078
73.7467
0.1743
4.4385
0.0889
32
Methane
1.9138
0.0895
30.7036
0.0726
7.0221
0.1406
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.6839
0.0320
1.3788
0.0033
1.3514
0.0271
35
Ethane
1.1831
0.0553
35.5767
0.0841
6.8489
0.1372
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.6704
0.0314
29.5045
0.0697
2.4478
0.0490
38
Nitrogen
0.2817
0.0132
7.8902
0.0186
0.6700
0.0134
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
14.3442
0.6708
244.2812
0.5774
27.1505
0.5438
43
Total
21.3826
1.0000
423.1056
1.0000
49.9312
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0007
0.0000
0.0208
0.0000
0.0018
0.0000
49
H2O
0.0002
0.0000
0.0030
0.0000
0.0002
0.0000
50
Oxygen
2.3046
0.1078
73.7467
0.1743
4.4385
0.0889
51
Methane
1.9138
0.0895
30.7036
0.0726
7.0221
0.1406
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.6839
0.0320
1.3788
0.0033
1.3514
0.0271
54
Ethane
1.1831
0.0553
35.5767
0.0841
6.8489
0.1372
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6704
0.0314
29.5045
0.0697
2.4478
0.0490
57
Nitrogen
0.2817
0.0132
7.8902
0.0186
0.6700
0.0134
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
14.3442
0.6708
244.2812
0.5774
27.1505
0.5438
62
Total
21.3826
1.0000
423.1056
1.0000
49.9312
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
0.0000
0.0073
0.0000
0.0076
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000 LIQUID VOLUME FRACTION 0.0000 0.0047
Page 237 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 81 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
Oxygen
0.0000
0.0015
0.0000
0.0028
0.0000
0.0015
16
Methane
0.0000
0.0018
0.0000
0.0017
0.0000
0.0035
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0000
0.0001
0.0000
0.0000
0.0000
0.0001
19
Ethane
0.0000
0.0069
0.0000
0.0120
0.0000
0.0208
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0000
0.0062
0.0000
0.0157
0.0000
0.0117
22
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0000
0.0004
0.0000
0.0015
0.0000
0.0009
26
Ammonia
0.0000
0.9757
0.0000
0.9586
0.0000
0.9568
27
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
71.62
71.62
---
34
Methane
49.19
49.19
---
---
---
---
35
218.0
218.0
1.068e-003
H2S
---
1.068e-003
---
36
Hydrogen
372.7
372.7
---
37
Ethane
7.990
7.990
---
38
Propane
---
---
---
39
CO2
5.071
5.071
---
40
Nitrogen
444.8
444.8
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
8.673e-005 0.6875
45
---
0.6875
---
UNIT OPERATIONS
46 47 48
8.673e-005
FEED TO
PRODUCT FROM
Mixer:
MIX-107 Separator:
49
LOGICAL CONNECTION D-7
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
229.7 psia 21.38 lbmole/hrMass:
423.1 lb/hr Std Ideal Liq Volume:
49.93 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 238 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 82
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
79.29
79.29
79.29
(psia)
229.7
229.7
229.7
453.3
0.0000
453.3
7858
0.0000
7858
875.0
0.0000
875.0
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-3.038e+004 19.86 -1.377e+007 873.7*
(barrel/day)
22
-2.368e+004 36.78 0.0000 0.0000
-3.038e+004 19.86 -1.377e+007 873.7
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase 17.33
(lbmole/ft3) (lb/ft3)
2.161
19.79 4.403e-002
Liquid Phase 17.33 2.161
37.47
0.8712
37.47
(barrel/day)
896.5
0.0000
896.5
Mass Enthalpy
(Btu/lb)
-1753
-1197
-1753
30
Mass Entropy
(Btu/lb-F)
1.146
1.859
1.146
31
Heat Capacity
20.45
9.556
20.45
32
Mass Heat Capacity
1.180
0.4829
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.380e+005
1.596e+005
1.380e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.644e+005
1.840e+005
1.644e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
1.336e-002
---
1.336e-002
38
CO2 App WT Con
(lbmol/lb)
3.567e-004
---
3.567e-004
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
41 42 43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.180
9487
9297
9487
14.19
---
14.19
7964
8065
7964
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
(Btu/lb)
135.7
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.215
1.831
2.215
Specific Heat
(Btu/lbmole-F)
20.45
9.556
20.45
Std. Gas Flow
(MMSCFD)
4.121
0.0000
4.121
(lb/ft3)
38.39
36.22
38.39
(USGPS)
0.4358
---
0.4358
Licensed to: LEGENDS
---
0.9020
12.27
12.02
12.27
---
---
---
0.0000
---
---
1.108
1.262
1.108
2.319
1.434
2.319
9450
---
---
(cSt)
0.2063
0.7361
0.2063
(lb/ft3)
38.45
30.66
38.45
873.7
0.0000
873.7
1.000
0.0000
1.000
0.4626
22.71
0.4626
(psia)
(Btu/lbmole)
(barrel/day) (ft3/lbmole) (Btu/lb)
1.837e-002
545.2
---
---
0.0000
0.0000
1.0000
(dyne/cm)
25.66
(Btu/hr-ft-F)
0.2688
1.775e-002
0.2688
0.1238
1.027e-002
0.1238
(cP)
---
25.66
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 239 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 82 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Liquid Phase
18.47
7.570
18.47
1.065
0.3826
1.065
8.820
6.664
8.820
0.5088
0.3368
0.5088
5.936
---
---
0.3425
---
---
3.445
---
---
(psia)
234.0
1139
234.0
(psia)
287.9
4258
287.9
873.7
0.0000
873.7
-62.73
---
---
(Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.0001
0.0000
0.0020
0.0000
0.0002
0.0000
30
H2O
3.3144
0.0073
59.7093
0.0076
4.0967
0.0047
31
Oxygen
0.6822
0.0015
21.8290
0.0028
1.3138
0.0015
32
Methane
0.8248
0.0018
13.2318
0.0017
3.0262
0.0035
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0389
0.0001
0.0784
0.0000
0.0769
0.0001
35
Ethane
3.1392
0.0069
94.3963
0.0120
18.1723
0.0208
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
2.8031
0.0062
123.3618
0.0157
10.2345
0.0117
38
Nitrogen
0.0134
0.0000
0.3761
0.0000
0.0319
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
42
Ammonia
442.3134
0.9757
7532.5971
0.9586
837.2072
0.9568
43
Total
453.3270
1.0000
7857.6491
1.0000
874.9722
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.1078
0.0000
0.1743
0.0000
0.0889
51
Methane
0.0000
0.0895
0.0000
0.0726
0.0000
0.1406
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0320
0.0000
0.0033
0.0000
0.0271
54
Ethane
0.0000
0.0553
0.0000
0.0841
0.0000
0.1372
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0314
0.0000
0.0697
0.0000
0.0490
57
Nitrogen
0.0000
0.0132
0.0000
0.0186
0.0000
0.0134
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.6708
0.0000
0.5774
0.0000
0.5438
62
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0001
0.0000
0.0020
0.0000
0.0002
68
H2O
3.3144
0.0073
59.7093
0.0076
4.0967
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.000 LIQUID VOLUME FRACTION 0.0000 0.0047
Page 240 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 82 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Oxygen
0.6822
0.0015
21.8290
0.0028
1.3138
0.0015
16
Methane
0.8248
0.0018
13.2318
0.0017
3.0262
0.0035
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0389
0.0001
0.0784
0.0000
0.0769
0.0001
19
Ethane
3.1392
0.0069
94.3963
0.0120
18.1723
0.0208
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
2.8031
0.0062
123.3618
0.0157
10.2345
0.0117
22
Nitrogen
0.0134
0.0000
0.3761
0.0000
0.0319
0.0000
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
26
Ammonia
442.3134
0.9757
7532.5971
0.9586
837.2072
0.9568
27
Total
453.3270
1.0000
7857.6491
1.0000
874.9722
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
71.62
71.62
---
34
Methane
49.19
49.19
---
---
---
---
35
218.0
218.0
1.068e-003
H2S
---
1.068e-003
---
36
Hydrogen
372.7
372.7
---
37
Ethane
7.990
7.990
---
38
Propane
---
---
---
39
CO2
5.071
5.071
---
40
Nitrogen
444.8
444.8
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
8.673e-005 0.6875
45
---
0.6875
---
UNIT OPERATIONS
46 47 48
8.673e-005
FEED TO
PRODUCT FROM
Tee:
TEE-105 Separator:
49
LOGICAL CONNECTION D-7
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
229.7 psia 453.3 lbmole/hrMass:
7858 lb/hr Std Ideal Liq Volume:
875.0 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 241 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 83
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18 19 20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.9999
0.9999
0.0001
(F)
6.086
6.086
6.086
(psia)
229.7
229.7
229.7
923.8
923.7
0.1169
(lbmole/hr) (lb/hr)
1.561e+004
1.561e+004
(barrel/day)
2119
2119
Molar Enthalpy
(Btu/lbmole)
-8773
-8769
Molar Entropy
(Btu/lbmole-F)
31.55
31.55
2.022 0.2166 -3.862e+004 16.32
(Btu/hr)
-8.104e+006
-8.100e+006
-4514
(barrel/day)
* 1.494e+006
1.494e+006
0.2158
22
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-519.1
-518.9
-2233
30
Mass Entropy
(Btu/lb-F)
1.867
1.867
0.9436
31
Heat Capacity
7.605
7.603
18.49
32
Mass Heat Capacity
0.4500
0.4499
33
LHV Molar Basis (Std)
(Btu/lbmole)
9.999e+004
9.998e+004
1.261e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.144e+005
1.144e+005
1.519e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
16.90 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
4.708e-002 0.7956 8.388e+004
16.90 4.708e-002 0.7955 8.388e+004
17.30 2.448 42.35 0.2041
1.069
6768
6768
8780
---
---
1.229
(lbmole/ft3)
---
---
6.601e-003
(lbmol/lb)
---
---
1.559e-004
(Btu/lb)
5917
5917
Phase Fraction [Vol. Basis]
0.9999
0.9999
1.022e-004
41
Phase Fraction [Mass Basis]
0.9999
0.9999
1.295e-004
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
2.433e-006
43
Mass Exergy
(Btu/lb)
174.9
---
44
Partial Pressure of CO2
(psia)
2.253
---
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
7292
---
(ACFM)
327.0
327.0
---
(lbmole/ft3)
1.863
1.863
2.307
Specific Heat
(Btu/lbmole-F)
7.605
7.603
Std. Gas Flow
(MMSCFD)
8.398
8.397
31.49
31.49
Licensed to: LEGENDS
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
9.920e-005
(Btu/lb)
9.920e-005 1.877e-002
---
0.9762 10.51
12.19
---
---
---
0.0000
---
---
1.353
1.354
1.120
1.419
1.419
1.939
6761
---
---
---
0.9345
0.3524
4.466e-002
4.466e-002
40.04
1.494e+006
1.494e+006
0.2158
21.24
0.0000
1.000
21.24
0.4084
400.1
---
---
0.9999
0.9999
0.0001
(dyne/cm)
38.74
(Btu/hr-ft-F)
---
(cP)
39.90
---
10.51
1.265e-004 (ft3/lbmole)
18.49 1.062e-003
---
---
38.74
2.875e-002
0.3254
1.191e-002
0.2391
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 242 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 83 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
5.619
5.617
16.51
0.3325
0.3324
0.9543
5.359
5.357
9.538
0.3171
0.3170
0.5514
---
---
8.582
---
---
0.4961
---
---
2.155
---
---
218.7
---
---
1.494e+006 -40.52
23
1.494e+006 ---
292.8 0.2158 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9999
LIQUID VOLUME FRACTION
29
CO
0.1887
0.0002
5.2849
0.0003
0.4527
0.0002
30
H2O
0.0115
0.0000
0.2074
0.0000
0.0142
0.0000
31
Oxygen
130.2044
0.1409
4166.5397
0.2669
250.7689
0.1183
32
Methane
78.0631
0.0845
1252.3590
0.0802
286.4204
0.1352
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
326.8143
0.3538
658.8577
0.0422
645.7834
0.3047
35
Ethane
20.0052
0.0217
601.5541
0.0385
115.8057
0.0546
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
9.0594
0.0098
398.7025
0.0255
33.0778
0.0156
38
Nitrogen
219.0513
0.2371
6136.2843
0.3931
521.0594
0.2459
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0003
0.0000
0.0162
0.0000
0.0011
0.0000
42
Ammonia
140.4247
0.1520
2391.4321
0.1532
265.7947
0.1254
43
Total
923.8228
1.0000
15611.2379
1.0000
2119.1783
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9999 LIQUID VOLUME FRACTION
48
CO
0.1887
0.0002
5.2849
0.0003
0.4527
0.0002
49
H2O
0.0021
0.0000
0.0377
0.0000
0.0026
0.0000
50
Oxygen
130.2043
0.1410
4166.5366
0.2669
250.7687
0.1183
51
Methane
78.0631
0.0845
1252.3582
0.0802
286.4202
0.1352
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
326.8143
0.3538
658.8576
0.0422
645.7834
0.3048
54
Ethane
20.0051
0.0217
601.5518
0.0385
115.8052
0.0547
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
9.0591
0.0098
398.6886
0.0255
33.0767
0.0156
57
Nitrogen
219.0513
0.2371
6136.2838
0.3931
521.0593
0.2459
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0005
0.0000
0.0000
0.0000
61
Ammonia
140.3180
0.1519
2389.6165
0.1531
265.5929
0.1253
62
Total
923.7060
1.0000
15609.2162
1.0000
2118.9617
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
0.0094
0.0806
0.1697
0.0839
0.0116
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.265e-004 LIQUID VOLUME FRACTION 0.0000 0.0537
Page 243 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 83 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.265e-004 LIQUID VOLUME FRACTION
15
Oxygen
0.0001
0.0008
0.0031
0.0015
0.0002
0.0009
16
Methane
0.0001
0.0004
0.0008
0.0004
0.0002
0.0009
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0000
0.0002
0.0001
0.0000
0.0001
0.0003
19
Ethane
0.0001
0.0007
0.0024
0.0012
0.0005
0.0021
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0003
0.0027
0.0139
0.0069
0.0012
0.0053
22
Nitrogen
0.0000
0.0001
0.0005
0.0002
0.0000
0.0002
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0003
0.0022
0.0157
0.0077
0.0011
0.0049
26
Ammonia
0.1066
0.9122
1.8157
0.8981
0.2018
0.9318
27
Total
0.1169
1.0000
2.0217
1.0000
0.2166
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
169.2
169.2
---
34
Methane
194.3
194.3
---
---
---
---
35
744.8
744.8
2.811e-005
H2S
---
2.811e-005
---
36
Hydrogen
1481
1481
---
37
Ethane
32.10
32.10
---
38
Propane
---
---
---
39
CO2
3.638
3.638
---
40
Nitrogen
1626
1626
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
4.239e-006 0.1665
45
---
0.1665
---
UNIT OPERATIONS
46 47 48
4.239e-006
FEED TO
PRODUCT FROM
Absorber:
T-101
49
Mixer:
LOGICAL CONNECTION MIX-107
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
229.7 psia 923.8 lbmole/hrMass:
1.561e+004 lb/hrStd Ideal Liq Volume:
2119 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 244 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 84
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
79.29
79.29
79.29
(psia)
229.7
229.7
229.7
203.0
0.0000
203.0
3518
0.0000
3518
391.8
0.0000
391.8
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-3.038e+004 19.86 -6.167e+006 391.2*
(barrel/day)
22
-2.368e+004 36.78 0.0000 0.0000
-3.038e+004 19.86 -6.167e+006 391.2
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase 17.33
(lbmole/ft3) (lb/ft3)
2.161
19.79 4.403e-002
Liquid Phase 17.33 2.161
37.47
0.8712
37.47
(barrel/day)
401.4
0.0000
401.4
Mass Enthalpy
(Btu/lb)
-1753
-1197
-1753
30
Mass Entropy
(Btu/lb-F)
1.146
1.859
1.146
31
Heat Capacity
20.45
9.556
20.45
32
Mass Heat Capacity
1.180
0.4829
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.380e+005
1.596e+005
1.380e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.644e+005
1.840e+005
1.644e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
1.336e-002
---
1.336e-002
38
CO2 App WT Con
(lbmol/lb)
3.567e-004
---
3.567e-004
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
41 42 43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.180
9487
9297
9487
14.19
---
14.19
7964
8065
7964
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
(Btu/lb)
135.7
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.215
1.831
2.215
Specific Heat
(Btu/lbmole-F)
20.45
9.556
20.45
Std. Gas Flow
(MMSCFD)
1.845
0.0000
1.845
(lb/ft3)
38.39
36.22
38.39
(USGPS)
0.1951
---
0.1951
Licensed to: LEGENDS
---
0.9020
12.27
12.02
12.27
---
---
---
0.0000
---
---
1.108
1.262
1.108
2.319
1.434
2.319
9450
---
---
(cSt)
0.2063
0.7361
0.2063
(lb/ft3)
38.45
30.66
38.45
391.2
0.0000
391.2
1.000
0.0000
1.000
0.4626
22.71
0.4626
(psia)
(Btu/lbmole)
(barrel/day) (ft3/lbmole) (Btu/lb)
1.837e-002
545.2
---
---
0.0000
0.0000
1.0000
(dyne/cm)
25.66
(Btu/hr-ft-F)
0.2688
1.775e-002
0.2688
0.1238
1.027e-002
0.1238
(cP)
---
25.66
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 245 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 84 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Liquid Phase
18.47
7.570
18.47
1.065
0.3826
1.065
8.820
6.664
8.820
0.5088
0.3368
0.5088
5.936
---
---
0.3425
---
---
3.445
---
---
(psia)
234.0
1139
234.0
(psia)
287.9
4258
287.9
391.2
0.0000
391.2
-62.73
---
---
(Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0009
0.0000
0.0001
0.0000
30
H2O
1.4840
0.0073
26.7342
0.0076
1.8343
0.0047
31
Oxygen
0.3054
0.0015
9.7737
0.0028
0.5882
0.0015
32
Methane
0.3693
0.0018
5.9244
0.0017
1.3549
0.0035
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0174
0.0001
0.0351
0.0000
0.0344
0.0001
35
Ethane
1.4056
0.0069
42.2649
0.0120
8.1365
0.0208
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
1.2550
0.0062
55.2339
0.0157
4.5824
0.0117
38
Nitrogen
0.0060
0.0000
0.1684
0.0000
0.0143
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0885
0.0004
5.4030
0.0015
0.3638
0.0009
42
Ammonia
198.0410
0.9757
3372.6386
0.9586
374.8504
0.9568
43
Total
202.9722
1.0000
3518.1772
1.0000
391.7593
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.1078
0.0000
0.1743
0.0000
0.0889
51
Methane
0.0000
0.0895
0.0000
0.0726
0.0000
0.1406
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0320
0.0000
0.0033
0.0000
0.0271
54
Ethane
0.0000
0.0553
0.0000
0.0841
0.0000
0.1372
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0314
0.0000
0.0697
0.0000
0.0490
57
Nitrogen
0.0000
0.0132
0.0000
0.0186
0.0000
0.0134
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.6708
0.0000
0.5774
0.0000
0.5438
62
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0009
0.0000
0.0001
68
H2O
1.4840
0.0073
26.7342
0.0076
1.8343
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.000 LIQUID VOLUME FRACTION 0.0000 0.0047
Page 246 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 84 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Oxygen
0.3054
0.0015
9.7737
0.0028
0.5882
0.0015
16
Methane
0.3693
0.0018
5.9244
0.0017
1.3549
0.0035
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0174
0.0001
0.0351
0.0000
0.0344
0.0001
19
Ethane
1.4056
0.0069
42.2649
0.0120
8.1365
0.0208
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
1.2550
0.0062
55.2339
0.0157
4.5824
0.0117
22
Nitrogen
0.0060
0.0000
0.1684
0.0000
0.0143
0.0000
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0885
0.0004
5.4030
0.0015
0.3638
0.0009
26
Ammonia
198.0410
0.9757
3372.6386
0.9586
374.8504
0.9568
27
Total
202.9722
1.0000
3518.1772
1.0000
391.7593
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
71.62
71.62
---
34
Methane
49.19
49.19
---
---
---
---
35
218.0
218.0
1.068e-003
H2S
---
1.068e-003
---
36
Hydrogen
372.7
372.7
---
37
Ethane
7.990
7.990
---
38
Propane
---
---
---
39
CO2
5.071
5.071
---
40
Nitrogen
444.8
444.8
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
8.673e-005 0.6875
45
---
0.6875
---
UNIT OPERATIONS
46 47 48
8.673e-005
FEED TO
PRODUCT FROM
Distillation:
T-7
49
Tee:
LOGICAL CONNECTION TEE-105
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
229.7 psia 203.0 lbmole/hrMass:
3518 lb/hr Std Ideal Liq Volume:
391.8 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 247 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 85
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
79.29
79.29
79.29
(psia)
229.7
229.7
229.7
250.4*
0.0000
250.4
4339
0.0000
4339
483.2
0.0000
483.2
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-3.038e+004 19.86 -7.606e+006 482.5*
(barrel/day)
22
-2.368e+004 36.78 0.0000 0.0000
-3.038e+004 19.86 -7.606e+006 482.5
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase 17.33
(lbmole/ft3) (lb/ft3)
2.161
19.79 4.403e-002
Liquid Phase 17.33 2.161
37.47
0.8712
37.47
(barrel/day)
495.1
0.0000
495.1
Mass Enthalpy
(Btu/lb)
-1753
-1197
-1753
30
Mass Entropy
(Btu/lb-F)
1.146
1.859
1.146
31
Heat Capacity
20.45
9.556
20.45
32
Mass Heat Capacity
1.180
0.4829
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.380e+005
1.596e+005
1.380e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.644e+005
1.840e+005
1.644e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
1.336e-002
---
1.336e-002
38
CO2 App WT Con
(lbmol/lb)
3.567e-004
---
3.567e-004
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
41 42 43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.180
9487
9297
9487
14.19
---
14.19
7964
8065
7964
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
(Btu/lb)
135.7
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.215
1.831
2.215
Specific Heat
(Btu/lbmole-F)
20.45
9.556
20.45
Std. Gas Flow
(MMSCFD)
2.276
0.0000
2.276
(lb/ft3)
38.39
36.22
38.39
(USGPS)
0.2407
---
0.2407
Licensed to: LEGENDS
---
0.9020
12.27
12.02
12.27
---
---
---
0.0000
---
---
1.108
1.262
1.108
2.319
1.434
2.319
9450
---
---
(cSt)
0.2063
0.7361
0.2063
(lb/ft3)
38.45
30.66
38.45
482.5
0.0000
482.5
1.000
0.0000
1.000
0.4626
22.71
0.4626
(psia)
(Btu/lbmole)
(barrel/day) (ft3/lbmole) (Btu/lb)
1.837e-002
545.2
---
---
0.0000
0.0000
1.0000
(dyne/cm)
25.66
(Btu/hr-ft-F)
0.2688
1.775e-002
0.2688
0.1238
1.027e-002
0.1238
(cP)
---
25.66
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 248 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 85 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Liquid Phase
18.47
7.570
18.47
1.065
0.3826
1.065
8.820
6.664
8.820
0.5088
0.3368
0.5088
5.936
---
---
0.3425
---
---
3.445
---
---
(psia)
234.0
1139
234.0
(psia)
287.9
4258
287.9
482.5
0.0000
482.5
-62.73
---
---
(Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
30
H2O
1.8304
0.0073
32.9751
0.0076
2.2625
0.0047
31
Oxygen
0.3767
0.0015
12.0553
0.0028
0.7256
0.0015
32
Methane
0.4555
0.0018
7.3074
0.0017
1.6712
0.0035
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0215
0.0001
0.0433
0.0000
0.0425
0.0001
35
Ethane
1.7337
0.0069
52.1314
0.0120
10.0359
0.0208
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
1.5480
0.0062
68.1279
0.0157
5.6521
0.0117
38
Nitrogen
0.0074
0.0000
0.2077
0.0000
0.0176
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1091
0.0004
6.6643
0.0015
0.4487
0.0009
42
Ammonia
244.2724
0.9757
4159.9584
0.9586
462.3567
0.9568
43
Total
250.3547
1.0000
4339.4720
1.0000
483.2129
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.1078
0.0000
0.1743
0.0000
0.0889
51
Methane
0.0000
0.0895
0.0000
0.0726
0.0000
0.1406
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0320
0.0000
0.0033
0.0000
0.0271
54
Ethane
0.0000
0.0553
0.0000
0.0841
0.0000
0.1372
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0314
0.0000
0.0697
0.0000
0.0490
57
Nitrogen
0.0000
0.0132
0.0000
0.0186
0.0000
0.0134
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.6708
0.0000
0.5774
0.0000
0.5438
62
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0011
0.0000
0.0001
68
H2O
1.8304
0.0073
32.9751
0.0076
2.2625
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.000 LIQUID VOLUME FRACTION 0.0000 0.0047
Page 249 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 85 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Oxygen
0.3767
0.0015
12.0553
0.0028
0.7256
0.0015
16
Methane
0.4555
0.0018
7.3074
0.0017
1.6712
0.0035
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0215
0.0001
0.0433
0.0000
0.0425
0.0001
19
Ethane
1.7337
0.0069
52.1314
0.0120
10.0359
0.0208
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
1.5480
0.0062
68.1279
0.0157
5.6521
0.0117
22
Nitrogen
0.0074
0.0000
0.2077
0.0000
0.0176
0.0000
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.1091
0.0004
6.6643
0.0015
0.4487
0.0009
26
Ammonia
244.2724
0.9757
4159.9584
0.9586
462.3567
0.9568
27
Total
250.3547
1.0000
4339.4720
1.0000
483.2129
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
71.62
71.62
---
34
Methane
49.19
49.19
---
---
---
---
35
H2S
218.0
218.0
1.068e-003
---
1.068e-003
---
36
Hydrogen
372.7
372.7
---
37
Ethane
7.990
7.990
---
38
Propane
---
---
---
39
CO2
5.071
5.071
---
40
Nitrogen
444.8
444.8
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
45
8.673e-005
0.6875
---
0.6875
---
UNIT OPERATIONS
46 47 48
8.673e-005
FEED TO
PRODUCT FROM
Mixer:
MIX-108 Tee:
49
LOGICAL CONNECTION TEE-105
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Active)
59
229.7 psia Molar:
* Mass: 250.4 lbmole/hr
4339 lb/hr Std Ideal Liq Volume:
483.2 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 250 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 86
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
132.8
132.8
(psia)
117.7*
117.7
(lbmole/hr) (lb/hr)
(Btu/hr)
1087 1.946e+004 1430 -1.112e+005 15.61 -1.209e+008 1399*
(barrel/day)
22
1087 1.946e+004 1430 -1.112e+005 15.61 -1.209e+008 1399
PROPERTIES
23 24
Overall
Aqueous Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
30
Mass Entropy
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.642e+004
1.642e+004
34
HHV Molar Basis (Std)
(Btu/lbmole)
3.511e+004
3.511e+004
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
8.102e-005
8.102e-005
38
CO2 App WT Con
(lbmol/lb)
1.412e-006
1.412e-006
39
LHV Mass Basis (Std)
40
(lbmole/ft3) (lb/ft3)
17.90
17.90
3.205
3.205
57.36
57.36
(barrel/day)
1450
1450
(Btu/lb)
-6213
-6213
(Btu/lb-F)
0.8721
0.8721
18.90
18.90
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.056
1.056
1962
1962
581.5
581.5
917.3
917.3
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
3.237
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
3.250
3.250
Specific Heat
(Btu/lbmole-F)
18.90
18.90
Std. Gas Flow
(MMSCFD)
9.883
9.883
Licensed to: LEGENDS
(lb/ft3)
58.17
58.17
(USGPS)
0.7049
0.7049
5.776e-003
(psia)
(Btu/lbmole)
5.776e-003
12.24
12.24
---
---
0.0000
---
1.117
1.117
1.187
1.187
1.725e+004
---
(cSt)
0.4624
0.4624
(lb/ft3)
59.44
59.44
(barrel/day)
1399
1399
1.000
1.000
(ft3/lbmole)
0.3120
0.3120
(Btu/lb)
963.9
---
0.0000
1.0000
(dyne/cm)
60.88
60.88
(Btu/hr-ft-F)
0.3561
0.3561
0.4249
0.4249
(cP)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 251 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 86 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Aqueous Phase 16.91
16.91
0.9451
0.9451
15.92
15.92
0.8895
0.8895
15.87
15.87
0.8870
0.8870
1.191
1.191
211.7
211.7
128.5
128.5
1399
1399
-10.20
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
29
CO
0.0000
0.0000
30
H2O
956.1739
0.8794
31
Oxygen
0.0114
0.0000
32
Methane
0.0001
33
H2S
34
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8852
1181.8636
0.8264
0.3640
0.0000
0.0219
0.0000
0.0000
0.0012
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0117
0.0000
0.0236
0.0000
0.0231
0.0000
35
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.0275
0.0000
1.2095
0.0001
0.1003
0.0001
38
Nitrogen
0.0199
0.0000
0.5585
0.0000
0.0474
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0029
0.0000
0.0002
0.0000
42
Ammonia
131.0322
0.1205
2231.4778
0.1147
248.0166
0.1734
43
Total
1087.2767
1.0000
19459.2060
1.0000
1430.0736
1.0000
44
0.0002
Vapour Fraction
17225.5682
Aqueous Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
48
CO
0.0000
0.0000
49
H2O
956.1739
0.8794
50
Oxygen
0.0114
0.0000
51
Methane
0.0001
52
H2S
53
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8852
1181.8636
0.8264
0.3640
0.0000
0.0219
0.0000
0.0000
0.0012
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0117
0.0000
0.0236
0.0000
0.0231
0.0000
54
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0275
0.0000
1.2095
0.0001
0.1003
0.0001
57
Nitrogen
0.0199
0.0000
0.5585
0.0000
0.0474
0.0000
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0029
0.0000
0.0002
0.0000
61
Ammonia
131.0322
0.1205
2231.4778
0.1147
248.0166
0.1734
62
Total
1087.2767
1.0000
19459.2060
1.0000
1430.0736
1.0000
63
17225.5682
K VALUE
64 65
0.0002
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
0.0000
---
0.0000
67
H2O
0.0000
---
0.0000
68
Oxygen
0.0000
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 252 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 86 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
LIGHT
HEAVY
0.0000
---
---
---
---
Hydrogen
0.0000
---
0.0000
15
Ethane
0.0000
---
0.0000
16
Propane
---
---
---
17
CO2
0.0000
---
0.0000
18
Nitrogen
0.0000
---
0.0000
---
---
---
13
H2S
14
19
Air
0.0000
20
Mercury
---
---
---
21
MEAmine
0.0000
---
0.0000
22
Ammonia
0.0000
---
0.0000
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Component Splitter:
X-102
LOGICAL CONNECTION
Pump:
P-101
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Inactive) Molar:
* 117.7 psia
1087 lbmole/hrMass:
37
1.946e+004 lb/hrStd Ideal Liq Volume:
1430 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 87
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.7600
0.7600
0.2400
(F)
219.6*
219.6
219.6
(psia)
117.7*
117.7
117.7
178.9
136.0
42.93
3095
2332
763.4
307.3
247.6
(lbmole/hr) (lb/hr)
(Btu/hr)
-4.496e+004 34.40 -8.044e+006 302.3*
(barrel/day)
61
-2.791e+004 39.28 -3.796e+006 246.3
59.72 -9.897e+004 18.96 -4.249e+006 58.27
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.30
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
2.211e-002 0.3824 3.459e+004 -2599
17.15 1.683e-002 0.2886 3.453e+004 -1628
Aqueous Phase 17.78 2.863 50.91 64.10 -5566
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 253 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 87 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
9.977e+004
1.211e+005
3.218e+004
16
HHV Molar Basis (Std)
(Btu/lbmole)
1.238e+005
1.466e+005
5.189e+004
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.989
2.291
1.066
11.81
9.312
19.73
0.6828
0.5431
1.109
7159
8548
2918
---
---
9.702
(lbmole/ft3)
---
---
1.373e-006
(lbmol/lb)
---
---
2.697e-008
(Btu/lb)
5767
7063
1809
Phase Fraction [Vol. Basis]
0.8057
0.8057
0.1943
23
Phase Fraction [Mass Basis]
0.7533
0.7533
24
Phase Fraction [Act. Vol. Basis]
0.9981
0.9981
25
Mass Exergy
110.3
---
26
Partial Pressure of CO2
27
Cost Based on Flow
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(Btu/lb) (psia)
2.377e-002
0.2467 1.853e-003 ---
---
--0.0000
(Cost/s)
0.0000
0.0000
(ACFM)
134.6
134.6
---
(lbmole/ft3)
2.489
2.348
3.073
Specific Heat
(Btu/lbmole-F)
11.81
9.312
19.73
Std. Gas Flow
(MMSCFD)
1.626
1.236
0.3902
43.05
40.26
(lb/ft3) (USGPS)
3.116e-002
(psia)
(Btu/lbmole)
54.64
---
3.116e-002 5.640e-003
---
0.9591
12.24
12.24
12.24
---
---
---
0.0000
---
---
1.202
1.271
1.112
1.177
1.333
1.112
2.449e+004
---
---
(cSt)
---
2.326
0.2245
(lb/ft3)
43.77
40.46
56.00
302.3
246.3
58.27
0.2400
0.0000
1.000
45.23
59.40
0.3493
(barrel/day) (ft3/lbmole) (Btu/lb)
1416
---
---
0.7600
0.7600
0.2400
(dyne/cm)
45.81
(Btu/hr-ft-F)
---
2.077e-002
0.3310
---
1.075e-002
0.1830
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
45.81
9.826
7.327
17.74
0.5680
0.4273
0.9977
10.04
6.984
17.74
0.5803
0.4073
0.9977
---
---
---
---
---
---
---
---
---
(psia)
211.7
211.8
210.5
(psia)
219.7
229.6
18.09
304.6
246.3
58.27
---
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0002
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
0.7600
LIQUID VOLUME FRACTION 0.0000
Page 254 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 87 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7600
LIQUID VOLUME FRACTION
15
H2O
47.8087
0.2672
861.2784
0.2783
59.0932
0.1923
16
Oxygen
0.0114
0.0001
0.3640
0.0001
0.0219
0.0001
17
Methane
0.0001
0.0000
0.0012
0.0000
0.0003
0.0000
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0117
0.0001
0.0236
0.0000
0.0231
0.0001
20
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.0275
0.0002
1.2095
0.0004
0.1003
0.0003
23
Nitrogen
0.0199
0.0001
0.5585
0.0002
0.0474
0.0002
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0029
0.0000
0.0002
0.0000
27
Ammonia
131.0322
0.7324
2231.4778
0.7210
248.0166
0.8071
28
Total
178.9115
1.0000
3094.9162
1.0000
307.3031
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7600 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
34
H2O
15.0198
0.1105
270.5830
0.1161
18.5650
0.0750
35
Oxygen
0.0114
0.0001
0.3640
0.0002
0.0219
0.0001
36
Methane
0.0001
0.0000
0.0012
0.0000
0.0003
0.0000
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0117
0.0001
0.0236
0.0000
0.0231
0.0001
39
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0275
0.0002
1.2086
0.0005
0.1003
0.0004
42
Nitrogen
0.0199
0.0001
0.5585
0.0002
0.0474
0.0002
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0028
0.0000
0.0002
0.0000
46
Ammonia
120.8910
0.8890
2058.7740
0.8830
228.8215
0.9242
47
Total
135.9814
1.0000
2331.5159
1.0000
247.5797
1.0000
48
Aqueous Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2400 LIQUID VOLUME FRACTION
52
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
H2O
32.7889
0.7638
590.6954
0.7738
40.5282
0.6786
54
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
0.0000
0.0000
0.0009
0.0000
0.0001
0.0000
61
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
65
Ammonia
10.1412
0.2362
172.7038
0.2262
19.1951
0.3214
66
Total
42.9301
1.0000
763.4003
1.0000
59.7234
1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 255 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 87 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
8990
---
8990
13
H2O
0.1446
---
0.1446
3862
---
14
Oxygen
15
Methane
16
6.526e+004
H2S
17
Hydrogen
3862
---
6.526e+004
---
---
---
8146
---
8146
18
Ethane
19
Propane
---
---
---
20
CO2
421.2
---
421.2
21
Nitrogen
8596
---
8596
---
---
---
22
2.781e+005
Air
---
2.781e+005
23
Mercury
---
---
---
24
MEAmine
6.716
---
6.716
25
Ammonia
3.763
---
3.763
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Distillation:
T-7
Component Splitter:
30
LOGICAL CONNECTION X-102
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 117.7 psia
178.9 lbmole/hrMass:
40
3095 lb/hr Std Ideal Liq Volume:
307.3 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 88
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
13.13
13.13
(psia)
117.7*
117.7
(lbmole/hr) (lb/hr)
(Btu/hr)
908.4 1.636e+004 1123 -1.242e+005 10.47 -1.129e+008 1104*
(barrel/day)
64
908.4 1.636e+004 1123 -1.242e+005 10.47 -1.129e+008 1104
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Aqueous Phase 18.02
18.02
3.582
3.582
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 256 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 88 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
(lb/ft3)
Aqueous Phase 64.53
64.53
(barrel/day)
1084
1084
(Btu/lb)
-6896
-6896
(Btu/lb-F)
0.5811
0.5811
18.66
18.66
(Btu/lbmole-F) (Btu/lb-F)
1.036
1.036
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
19
HHV Molar Basis (Std)
(Btu/lbmole)
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
26
Phase Fraction [Mass Basis]
0.0000
1.000
27
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
28
Mass Exergy
(Btu/lb)
4.628
---
29
Partial Pressure of CO2
(psia)
0.0000
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
---
---
39
User Property
---
---
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63 64
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
18.66
18.66
Std. Gas Flow
(MMSCFD)
8.257
8.257
(lb/ft3)
62.30
62.30
(USGPS)
0.5270
0.5270
6.476e-003
(psia)
(Btu/lbmole)
6.476e-003
0.0000
---
1.119
1.119
1.118
1.118
1.603e+004
---
(cSt)
1.958
1.958
(lb/ft3)
63.35
63.35
(barrel/day)
1104
1104
1.000
1.000
(ft3/lbmole)
0.2792
0.2792
(Btu/lb)
889.6
---
0.0000
1.0000
(dyne/cm)
78.19
78.19
(Btu/hr-ft-F)
0.3193
0.3193
2.024
2.024
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
16.67
16.67
0.9254
0.9254
16.68
16.68
0.9260
0.9260
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
1104
1104
Viscosity Index
11.18
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 257 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 88 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
908.3652
1.0000
17
Oxygen
0.0000
0.0000
18
Methane
0.0000
19
H2S
20
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1122.7705
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
908.3652
1.0000
1.0000
1122.7705
1.0000
30
0.0000
Vapour Fraction
16364.2898
16364.2898
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
34
CO
0.0000
0.0000
35
H2O
908.3652
1.0000
36
Oxygen
0.0000
0.0000
37
Methane
0.0000
38
H2S
39
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1122.7705
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
908.3652
1.0000
1.0000
1122.7705
1.0000
49
16364.2898
16364.2898
K VALUE
50 51
0.0000
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
0.0000
---
0.0000
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 258 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 88 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
LOGICAL CONNECTION
Component Splitter:
13
X-102
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 117.7 psia
908.4 lbmole/hrMass:
23
1.636e+004 lb/hrStd Ideal Liq Volume:
1123 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 89
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Liquid Phase
Vapour Phase
* 0.0000
1.0000
0.0000
(F)
76.75
76.75
76.75
(psia)
114.7*
114.7
114.7
281.9
281.9
0.0000
4853
4853
0.0000
501.4
501.4
(lbmole/hr) (lb/hr)
(Btu/hr)
-4.601e+004 18.22 -1.297e+007 496.1*
(barrel/day)
47
-4.601e+004 18.22 -1.297e+007 496.1
0.0000 -1.988e+004 36.42 0.0000 0.0000
PROPERTIES
48 49
Overall
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
(lbmole/ft3)
17.22
2.385
2.385
Vapour Phase 17.03 2.140e-002
41.06
41.06
0.3644
(barrel/day)
505.2
505.2
0.0000
Mass Enthalpy
(Btu/lb)
-2672
-2672
-1167
55
Mass Entropy
(Btu/lb-F)
1.058
1.058
2.139
56
Heat Capacity
19.31
19.31
9.159
57
Mass Heat Capacity
1.122
1.122
0.5378
58
LHV Molar Basis (Std)
(Btu/lbmole)
1.125e+005
1.125e+005
1.362e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
1.375e+005
1.375e+005
1.626e+005
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
Phase Fraction [Vol. Basis]
66
Phase Fraction [Mass Basis]
67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
Liquid Phase 17.22
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
7984
7984
9549
1.381e-006
1.381e-006
---
(lbmole/ft3)
1.034e-009
1.034e-009
---
(lbmol/lb)
2.519e-011
2.519e-011
(Btu/lb)
(Btu/lb)
6537
6537
--7996
---
1.000
---
0.0000
1.000
0.0000
0.0000
1.000
0.0000
77.63
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 259 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 89 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Liquid Phase
Vapour Phase
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.403
2.403
2.259
Specific Heat
(Btu/lbmole-F)
19.31
19.31
9.159
Std. Gas Flow
(MMSCFD)
2.562
2.562
0.0000 38.46
(lb/ft3)
41.38
41.38
(USGPS)
0.2456
0.2456
---
(psia)
(Btu/lbmole)
8.354e-003
--0.9311
12.24
12.24
12.24
---
---
---
0.0000
---
---
1.115
1.115
1.277
1.115
1.115
1.386
1.284e+004
---
--1.458
(cSt)
0.2700
0.2700
(lb/ft3)
41.81
41.81
38.23
(barrel/day)
496.1
496.1
0.0000
1.000
1.000
0.0000
(ft3/lbmole)
0.4193
0.4193
46.73
(Btu/lb)
745.6
---
---
0.0000
1.0000
0.0000
(dyne/cm)
34.13
34.13
(Btu/hr-ft-F)
0.2894
0.2894
1.599e-002
0.1776
0.1776
8.509e-003
17.33
17.33
7.173
1.006
1.006
0.4212
17.33
17.33
6.610
1.006
1.006
0.3881
---
---
---
---
---
---
---
---
---
(psia)
210.4
210.4
210.5
(psia)
168.2
168.2
210.4
496.1
496.1
0.0000
-28.18
---
---
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
* 0.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
56
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
67
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
68
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 260 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 89 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
28
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
29
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.0003
0.0000
0.0003
0.0000
0.0002
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.9997
0.0000
0.9997
0.0000
0.9998
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
53
H2O
54
Oxygen
473.4
473.4
---
55
Methane
812.2
812.2
---
---
---
---
56
H2S
1471 1.519e-003
1471 1.519e-003
-----
57
Hydrogen
2097
2097
---
58
Ethane
304.6
304.6
---
59
Propane
---
---
---
60
CO2
22.60
22.60
---
61
Nitrogen
2083
2083
---
---
---
---
---
---
---
62
Air
63
Mercury
64
MEAmine
65
Ammonia
9.855e-004 1.212
9.855e-004 1.212
-----
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 261 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 89 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Pump:
P-102
Cooler:
LOGICAL CONNECTION E-107
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 114.7 psia
281.9 lbmole/hrMass:
23
501.4 barrel/day
User Variables
24 25
NOTES
26 27
4853 lb/hr Std Ideal Liq Volume:
29285
28 29
(Last modified Mon Dec 17, 2018, 15:26)
30 31
Description
32 33 34
Material Stream: 90
35 36 37
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
38 39
Overall
40
Vapour / Phase Fraction
41
Temperature:
42
Pressure:
43
Molar Flow
44
Mass Flow
45
Std Ideal Liq Vol Flow
46
Molar Enthalpy
(Btu/lbmole)
47
Molar Entropy
(Btu/lbmole-F)
48
Heat Flow
49
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
77.06
77.06
(psia)
214.7*
214.7
281.9
281.9
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
4853
4853
501.4
501.4
-4.600e+004 18.22 -1.297e+007 496.1*
(barrel/day)
50
-4.600e+004 18.22 -1.297e+007 496.1
PROPERTIES
51 52
Overall
53
Molecular Weight
54
Molar Density
55
Mass Density
56
Act. Volume Flow
57
Liquid Phase 17.22
17.22
2.385
2.385
41.07
41.07
(barrel/day)
505.1
505.1
Mass Enthalpy
(Btu/lb)
-2672
-2672
58
Mass Entropy
(Btu/lb-F)
1.058
1.058
59
Heat Capacity
19.30
19.30
60
Mass Heat Capacity
61
LHV Molar Basis (Std)
(Btu/lbmole)
1.125e+005
1.125e+005
62
HHV Molar Basis (Std)
(Btu/lbmole)
1.375e+005
1.375e+005
63
HHV Mass Basis (Std)
64
CO2 Loading
65
CO2 App ML Con
66
CO2 App WT Con
67
LHV Mass Basis (Std)
68
Phase Fraction [Vol. Basis]
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.121
7984
1.121
7984
1.381e-006
1.381e-006
(lbmole/ft3)
1.034e-009
1.034e-009
(lbmol/lb)
2.519e-011
2.519e-011
(Btu/lb)
6537
6537
0.0000
1.000
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 262 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 90 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Liquid Phase
12
Phase Fraction [Mass Basis]
0.0000
1.000
13
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
14
Mass Exergy
(Btu/lb)
78.12
---
15
Partial Pressure of CO2
(psia)
0.0000
---
16
Cost Based on Flow
(Cost/s)
0.0000
0.0000
17
Act. Gas Flow
18
Avg. Liq. Density
19 20 21
Std. Ideal Liq. Mass Density
22
Act. Liq. Flow
23
Z Factor
24
Watson K
25
User Property
26
Partial Pressure of H2S
27
Cp/(Cp - R)
28
Cp/Cv
29
Heat of Vap.
30
Kinematic Viscosity
31
Liq. Mass Density (Std. Cond)
32
Liq. Vol. Flow (Std. Cond)
33
Liquid Fraction
34
Molar Volume
35
Mass Heat of Vap.
36
Phase Fraction [Molar Basis]
37
Surface Tension
38
Thermal Conductivity
39
Viscosity
40
Cv (Semi-Ideal)
41
Mass Cv (Semi-Ideal)
42
Cv
43
Mass Cv
44
Cv (Ent. Method)
45
Mass Cv (Ent. Method)
46
Cp/Cv (Ent. Method)
47
Reid VP at 37.8 C
(psia)
48
True VP at 37.8 C
(psia)
49 50
(ACFM)
---
---
(lbmole/ft3)
2.403
2.403
Specific Heat
(Btu/lbmole-F)
19.30
19.30
Std. Gas Flow
(MMSCFD)
2.562
2.562
(lb/ft3)
41.38
41.38
(USGPS)
0.2455
0.2455
1.563e-002
(psia)
(Btu/lbmole)
1.563e-002
12.24
12.24
---
---
0.0000
---
1.115
1.115
1.732
1.732
1.227e+004
---
(cSt)
0.2695
0.2695
(lb/ft3)
41.81
41.81
496.1
496.1
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4192
0.4192
712.8
---
0.0000
1.0000
(dyne/cm)
34.09
34.09
(Btu/hr-ft-F)
0.2892
0.2892
0.1773
0.1773
17.31
17.31
1.006
1.006
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
11.14
11.14
0.6471
0.6471
11.78
11.78
0.6844
0.6844
1.638
1.638
210.4
210.4
168.2
168.2
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
496.1
496.1
Viscosity Index
-28.28
---
(Btu/lb-F)
51
COMPOSITION
52 53
Overall Phase
54 55
COMPONENTS
56
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
57
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
59
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 263 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 90 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
16
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
17
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
1.0000
18
Liquid Phase
19 20
COMPONENTS
MOLAR FLOW (lbmole/hr)
21
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
22
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
24
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
35
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
36
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
1.0000
37
K VALUE
38 39
COMPONENTS
MIXED
LIGHT
HEAVY
40
CO
0.0000
0.0000
---
41
H2O
0.0000
0.0000
---
42
Oxygen
0.0000
0.0000
---
43
Methane
0.0000
0.0000
---
---
---
---
44
H2S
45
Hydrogen
0.0000
0.0000
---
46
Ethane
0.0000
0.0000
---
47
Propane
---
---
---
48
CO2
0.0000
0.0000
---
49
Nitrogen
0.0000
0.0000
---
---
---
---
50
Air
51
Mercury
---
---
---
52
MEAmine
0.0000
0.0000
---
53
Ammonia
0.0000
0.0000
---
54
UNIT OPERATIONS
55 56 57
FEED TO
PRODUCT FROM
Recycle:
RCY-3
58
Pump:
LOGICAL CONNECTION P-102
UTILITIES
59 60
( No utilities reference this stream )
61
PROCESS UTILITY
62 63 64
DYNAMICS
65 66
Pressure Specification
(Active):
67
Flow Specification
(Inactive) Molar:
* 214.7 psia
281.9 lbmole/hrMass:
4853 lb/hr Std Ideal Liq Volume:
501.4 barrel/day
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 264 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 90 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
User Variables
10 11
NOTES
12 13 14
Description
15 16 17
Material Stream: 91
18 19 20
CONDITIONS
21 22
Overall
23
Vapour / Phase Fraction
24
Temperature:
25
Pressure:
26
Molar Flow
27
Mass Flow
28
Std Ideal Liq Vol Flow
29
Molar Enthalpy
(Btu/lbmole)
30
Molar Entropy
(Btu/lbmole-F)
31
Heat Flow
32
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
77.06*
77.06
(psia)
214.7*
214.7
281.9*
281.9
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
4853
4853
501.4
501.4
-4.600e+004 18.22 -1.297e+007 496.1*
(barrel/day)
33
-4.600e+004 18.22 -1.297e+007 496.1
PROPERTIES
34 35
Overall
36
Molecular Weight
37
Molar Density
38
Mass Density
39
Act. Volume Flow
40
Liquid Phase 17.22
17.22
2.385
2.385
41.07
41.07
(barrel/day)
505.1
505.1
Mass Enthalpy
(Btu/lb)
-2672
-2672
41
Mass Entropy
(Btu/lb-F)
1.058
1.058
42
Heat Capacity
19.30
19.30
43
Mass Heat Capacity
44
LHV Molar Basis (Std)
(Btu/lbmole)
1.125e+005
1.125e+005
45
HHV Molar Basis (Std)
(Btu/lbmole)
1.375e+005
1.375e+005
46
HHV Mass Basis (Std)
47
CO2 Loading
48
CO2 App ML Con
49
CO2 App WT Con
50
LHV Mass Basis (Std)
51
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.121
7984
1.121
7984
1.381e-006
1.381e-006
(lbmole/ft3)
1.034e-009
1.034e-009
(lbmol/lb)
2.519e-011
2.519e-011
(Btu/lb)
6537
6537
Phase Fraction [Vol. Basis]
0.0000
1.000
52
Phase Fraction [Mass Basis]
0.0000
1.000
53
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
54
Mass Exergy
(Btu/lb)
78.12
---
55
Partial Pressure of CO2
(psia)
0.0000
---
56
Cost Based on Flow
(Cost/s)
0.0000
0.0000
57
Act. Gas Flow
58
Avg. Liq. Density
59 60 61
Std. Ideal Liq. Mass Density
62
Act. Liq. Flow
63
Z Factor
64
Watson K
65
User Property
66
Partial Pressure of H2S
67
(ACFM)
---
---
(lbmole/ft3)
2.403
2.403
Specific Heat
(Btu/lbmole-F)
19.30
19.30
Std. Gas Flow
(MMSCFD)
2.562
2.562
(lb/ft3)
41.38
41.38
(USGPS)
0.2455
0.2455
1.563e-002
12.24
---
---
0.0000
---
Cp/(Cp - R)
1.115
1.115
68
Cp/Cv
1.732
1.732
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
1.563e-002
12.24
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 265 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 91 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Heat of Vap.
13
Kinematic Viscosity
14
Liq. Mass Density (Std. Cond)
15
Liq. Vol. Flow (Std. Cond)
16
Liquid Fraction
17
Molar Volume
18
Mass Heat of Vap.
19
Phase Fraction [Molar Basis]
20
Surface Tension
21
Thermal Conductivity
22
Viscosity
23
Cv (Semi-Ideal)
24
Mass Cv (Semi-Ideal)
25
Cv
26
Mass Cv
27
Cv (Ent. Method)
28
Mass Cv (Ent. Method)
29
Cp/Cv (Ent. Method)
30
Reid VP at 37.8 C
(psia)
31
True VP at 37.8 C
(psia)
32 33
(Btu/lbmole)
Liquid Phase
1.227e+004
---
(cSt)
0.2695
0.2695
(lb/ft3)
41.81
41.81
496.1
496.1
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4192
0.4192
712.8
---
0.0000
1.0000
(dyne/cm)
34.09
34.09
(Btu/hr-ft-F)
0.2892
0.2892
0.1773
0.1773
17.31
17.31
1.006
1.006
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
11.14
11.14
0.6471
0.6471
11.78
11.78
0.6843
0.6843
1.638
1.638
210.4
210.4
168.2
168.2
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
496.1
496.1
Viscosity Index
-28.28
---
(Btu/lb-F)
34
COMPOSITION
35 36
Overall Phase
37 38
COMPONENTS
39 40
CO
41
H2O
42
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 49.2854
* 0.1748
* 887.8813
* 0.1830
* 60.9184
* 0.1215
Oxygen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
43
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
44
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
45
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
46
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
47
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
48
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
49
Nitrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
50
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
51
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
52
MEAmine
* 0.0885
* 0.0003
* 5.4059
* 0.0011
* 0.3640
* 0.0007
53
Ammonia
* 232.5108
* 0.8248
* 3959.6584
* 0.8159
* 440.0945
* 0.8778
54
Total
281.8847
1.0000
4852.9456
1.0000
501.3769
1.0000
55
Liquid Phase
56 57
COMPONENTS
58
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
59
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
H2O
49.2854
0.1748
887.8813
0.1830
60.9184
0.1215
61
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 266 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 91 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
18
Ammonia
232.5108
0.8248
3959.6584
0.8159
440.0945
0.8778
19
Total
281.8847
1.0000
4852.9456
1.0000
501.3769
1.0000
20
K VALUE
21 22
COMPONENTS
MIXED
LIGHT
HEAVY
23
CO
0.0000
0.0000
---
24
H2O
0.0000
0.0000
---
25
Oxygen
0.0000
0.0000
---
26
Methane
0.0000
0.0000
---
---
---
---
27
H2S
28
Hydrogen
0.0000
0.0000
---
29
Ethane
0.0000
0.0000
---
30
Propane
---
---
---
31
CO2
0.0000
0.0000
---
32
Nitrogen
0.0000
0.0000
---
---
---
---
33
Air
34
Mercury
---
---
---
35
MEAmine
0.0000
0.0000
---
36
Ammonia
0.0000
0.0000
---
37
UNIT OPERATIONS
38 39
FEED TO
PRODUCT FROM
40
Recycle:
LOGICAL CONNECTION RCY-3
41
UTILITIES
42 43
( No utilities reference this stream )
44
PROCESS UTILITY
45 46 47
DYNAMICS
48 49
Pressure Specification
(Inactive):
50
Flow Specification
(Inactive) Molar:
* 214.7 psia * Mass: 281.9 lbmole/hr
51
4853 lb/hr Std Ideal Liq Volume:
501.4 barrel/day
User Variables
52 53
NOTES
54 55 56
Description
57 58 59
Material Stream: 92
60 61 62
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
63 64
Overall
65
Vapour / Phase Fraction
66
Temperature:
67
Pressure:
68
Molar Flow
69
Aspen Technology Inc. Licensed to: LEGENDS
Aqueous Phase 0.0000
1.0000
(F)
310.0
310.0
(psia)
364.7
364.7
479.6
479.6
(lbmole/hr)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 267 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 92 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Mass Flow
13
Std Ideal Liq Vol Flow
14
Molar Enthalpy
(Btu/lbmole)
15
Molar Entropy
(Btu/lbmole-F)
16
Heat Flow
17
Liq Vol Flow @Std Cond
(lb/hr) (barrel/day)
(Btu/hr)
Aqueous Phase 8640
8640
592.8
592.8
-1.186e+005 19.63 -5.689e+007 583.0*
(barrel/day)
18
-1.186e+005 19.63 -5.689e+007 583.0
PROPERTIES
19 20
Overall
21
Molecular Weight
22
Molar Density
23
Mass Density
24
Act. Volume Flow
25
Aqueous Phase 18.02
18.02
3.122
3.122
56.24
56.24
(barrel/day)
656.7
656.7
Mass Enthalpy
(Btu/lb)
-6585
-6585
26
Mass Entropy
(Btu/lb-F)
1.089
1.089
27
Heat Capacity
19.72
19.72
28
Mass Heat Capacity
29
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
1.095
1.095
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
30
HHV Molar Basis (Std)
(Btu/lbmole)
31
HHV Mass Basis (Std)
32
CO2 Loading
33
CO2 App ML Con
34
CO2 App WT Con
35
LHV Mass Basis (Std)
36
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
37
Phase Fraction [Mass Basis]
0.0000
1.000
38
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
39
Mass Exergy
(Btu/lb)
43.03
---
40
Partial Pressure of CO2
(psia)
0.0000
---
41
Cost Based on Flow
(Cost/s)
0.0000
0.0000
42
Act. Gas Flow
43
Avg. Liq. Density
44 45 46
Std. Ideal Liq. Mass Density
47
Act. Liq. Flow
48
Z Factor
49
Watson K
---
---
50
User Property
---
---
51
Partial Pressure of H2S
52
Cp/(Cp - R)
53
Cp/Cv
54
Heat of Vap.
55
Kinematic Viscosity
56
Liq. Mass Density (Std. Cond)
57
Liq. Vol. Flow (Std. Cond)
58
Liquid Fraction
59
Molar Volume
60
Mass Heat of Vap.
61
Phase Fraction [Molar Basis]
62
Surface Tension
63
Thermal Conductivity
64
Viscosity
65
Cv (Semi-Ideal)
66
Mass Cv (Semi-Ideal)
67
Cv
68
Mass Cv
69
Fluid Package:
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.72
19.72
Std. Gas Flow
(MMSCFD)
4.360
4.360
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
62.30
62.30
(USGPS)
0.3192
0.3192
1.414e-002
(psia)
(Btu/lbmole)
1.414e-002
0.0000
---
1.112
1.112
1.188
1.188
1.445e+004
---
(cSt)
0.1949
0.1949
(lb/ft3)
63.35
63.35
583.0
583.0
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.3203
0.3203
802.3
---
0.0000
1.0000
(dyne/cm)
47.75
47.75
(Btu/hr-ft-F)
0.3962
0.3962
0.1755
0.1755
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
17.73
17.73
0.9844
0.9844
16.60
16.60
0.9216
0.9216
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 268 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 92 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Ent. Method)
13
Mass Cv (Ent. Method)
14
Cp/Cv (Ent. Method)
15
Reid VP at 37.8 C
16
True VP at 37.8 C
17
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
18
Viscosity Index
(Btu/lbmole-F)
Aqueous Phase ---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
583.0
583.0
---
---
(Btu/lb-F)
19
COMPOSITION
20 21
Overall Phase
22 23
COMPONENTS
24
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
25
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
H2O
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
27
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Total
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
40
Aqueous Phase
41 42
COMPONENTS
43
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
44
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
H2O
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
46
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Total
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
59
K VALUE
60 61
COMPONENTS
MIXED
LIGHT
HEAVY
62
CO
---
---
---
63
H2O
0.0000
---
0.0000
64
Oxygen
---
---
---
65
Methane
---
---
---
---
---
-----
66
H2S
67
Hydrogen
---
---
68
Ethane
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 269 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 92 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
Propane
---
---
---
13
CO2
---
---
---
14
Nitrogen
---
---
---
---
---
---
15
Air
16
Mercury
---
---
---
17
MEAmine
---
---
---
18
Ammonia
---
---
---
19
UNIT OPERATIONS
20 21 22
FEED TO
PRODUCT FROM
Component Splitter:
D-4A
Tee:
LOGICAL CONNECTION TEE-106
23
UTILITIES
24 25
( No utilities reference this stream )
26
PROCESS UTILITY
27 28 29
DYNAMICS
30 31
Pressure Specification
(Inactive):
32
Flow Specification
(Inactive) Molar:
364.7 psia 479.6 lbmole/hrMass:
33
8640 lb/hr Std Ideal Liq Volume:
592.8 barrel/day
User Variables
34 35
NOTES
36 37 38
Description
39 40 41
Material Stream: 93
42 43 44
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
45 46
Overall
47
Vapour / Phase Fraction
48
Temperature:
49
Pressure:
50
Molar Flow
51
Mass Flow
52
Std Ideal Liq Vol Flow
53
Molar Enthalpy
(Btu/lbmole)
54
Molar Entropy
(Btu/lbmole-F)
55
Heat Flow
56
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
310.0
310.0
(psia)
364.7
364.7
479.6
479.6
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
8640*
8640
592.8
592.8
-1.186e+005 19.63 -5.689e+007 583.0*
(barrel/day)
57
-1.186e+005 19.63 -5.689e+007 583.0
PROPERTIES
58 59
Overall
60
Molecular Weight
61
Molar Density
62
Mass Density
63
Act. Volume Flow
64
Aqueous Phase 18.02
18.02
3.122
3.122
56.24
56.24
(barrel/day)
656.7
656.7
Mass Enthalpy
(Btu/lb)
-6585
-6585
65
Mass Entropy
(Btu/lb-F)
1.089
1.089
66
Heat Capacity
19.72
19.72
67
Mass Heat Capacity
68
LHV Molar Basis (Std)
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
1.095
1.095
(Btu/lbmole)
0.0000
0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 270 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 93 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
HHV Molar Basis (Std)
13
HHV Mass Basis (Std)
14
CO2 Loading
15
CO2 App ML Con
16
CO2 App WT Con
17
LHV Mass Basis (Std)
18
(Btu/lbmole) (Btu/lb)
Aqueous Phase
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
19
Phase Fraction [Mass Basis]
0.0000
1.000
20
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
21
Mass Exergy
(Btu/lb)
43.03
---
22
Partial Pressure of CO2
(psia)
0.0000
---
23
Cost Based on Flow
(Cost/s)
0.0000
0.0000
24
Act. Gas Flow
25
Avg. Liq. Density
26 27 28
Std. Ideal Liq. Mass Density
29
Act. Liq. Flow
30
Z Factor
31
Watson K
---
---
32
User Property
---
---
33
Partial Pressure of H2S
34
Cp/(Cp - R)
35
Cp/Cv
36
Heat of Vap.
37
Kinematic Viscosity
38
Liq. Mass Density (Std. Cond)
39
Liq. Vol. Flow (Std. Cond)
40
Liquid Fraction
41
Molar Volume
42
Mass Heat of Vap.
43
Phase Fraction [Molar Basis]
44
Surface Tension
45
Thermal Conductivity
46
Viscosity
47
Cv (Semi-Ideal)
48
Mass Cv (Semi-Ideal)
49
Cv
50
Mass Cv
51
Cv (Ent. Method)
52
Mass Cv (Ent. Method)
53
Cp/Cv (Ent. Method)
54
Reid VP at 37.8 C
55
True VP at 37.8 C
56
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
57
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.72
19.72
Std. Gas Flow
(MMSCFD)
4.360
4.360
(lb/ft3)
62.30
62.30
(USGPS)
0.3192
0.3192
1.414e-002
(psia)
(Btu/lbmole)
1.414e-002
0.0000
---
1.112
1.112
1.188
1.188
1.445e+004
---
(cSt)
0.1949
0.1949
(lb/ft3)
63.35
63.35
583.0
583.0
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.3203
0.3203
802.3
---
0.0000
1.0000
(dyne/cm)
47.75
47.75
(Btu/hr-ft-F)
0.3962
0.3962
0.1755
0.1755
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
17.73
17.73
0.9844
0.9844
16.60
16.60
0.9216
0.9216
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
583.0
583.0
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
58
COMPOSITION
59 60
Overall Phase
61 62
COMPONENTS
63
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
64
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
H2O
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
66
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 271 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 93 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Total
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
25
Aqueous Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
H2O
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
44
K VALUE
45 46
COMPONENTS
MIXED
LIGHT
HEAVY
47
CO
---
---
---
48
H2O
0.0000
---
0.0000
49
Oxygen
---
---
---
50
Methane
---
---
---
---
---
---
51
H2S
52
Hydrogen
---
---
---
53
Ethane
---
---
---
54
Propane
---
---
---
55
CO2
---
---
---
56
Nitrogen
---
---
---
---
---
---
57
Air
58
Mercury
---
---
---
59
MEAmine
---
---
---
60
Ammonia
---
---
---
61
UNIT OPERATIONS
62 63 64
FEED TO Component Splitter:
65
PRODUCT FROM D-4B
Tee:
LOGICAL CONNECTION TEE-106
UTILITIES
66 67
( No utilities reference this stream )
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 272 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 93 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROCESS UTILITY
10 11 12
DYNAMICS
13 14
Pressure Specification
(Inactive):
15
Flow Specification
(Active)
364.7 psia Molar:
* Std Ideal Liq Volume: 8640 lb/hr
479.6 lbmole/hrMass:
16
592.8 barrel/day
User Variables
17 18
NOTES
19 20 21
Description
22 23 24
Material Stream: 1000
25 26 27
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
28 29
Overall
30
Vapour / Phase Fraction
31
Temperature:
32
Pressure:
33
Molar Flow
34
Mass Flow
35
Std Ideal Liq Vol Flow
(barrel/day)
36
Molar Enthalpy
(Btu/lbmole)
37
Molar Entropy
(Btu/lbmole-F)
38
Heat Flow
39
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
Liquid Phase
0.0003
0.0003
0.9789
0.0208
(F)
-289.4
-289.4
-289.4
-289.4
(psia)
114.7
114.7
114.7
114.7
97.89
2.079
1702
57.79
(lbmole/hr)
100.0
(lb/hr)
(Btu/hr)
1760 197.7 -3.735e+004 -0.8232 -3.735e+006 196.4*
(barrel/day)
40
2.995e-002 0.1299 5.997e-002 -2698 18.74 -80.83 48.51
187.6 -3.731e+004 -1.142 -3.653e+006 187.8
10.04 -3.973e+004 13.91 -8.262e+004 3346
PROPERTIES
41 42
Overall
43
Molecular Weight
44
Molar Density
45
Mass Density
46
Act. Volume Flow
47
Vapour Phase 17.60
(lbmole/ft3)
6.426e-002
Liquid Phase
Liquid Phase
17.39
27.79
2.996
1.514
51.00
0.2787
52.10
42.07
(barrel/day)
147.5
1.993
139.7
5.872
Mass Enthalpy
(Btu/lb)
-2122
-622.2
-2146
48
Mass Entropy
(Btu/lb-F)
49
Heat Capacity
50
Mass Heat Capacity
51
LHV Molar Basis (Std)
(Btu/lbmole)
1.415e+005
9.715e+004
1.344e+005
4.727e+005
52
HHV Molar Basis (Std)
(Btu/lbmole)
1.679e+005
1.135e+005
1.605e+005
5.144e+005
53
HHV Mass Basis (Std)
54
CO2 Loading
55
CO2 App ML Con
56
CO2 App WT Con
57
LHV Mass Basis (Std)
58
Phase Fraction [Vol. Basis]
59
Phase Fraction [Mass Basis]
60
Phase Fraction [Act. Vol. Basis]
61
Mass Exergy
62
Partial Pressure of CO2
63
Cost Based on Flow
64
Act. Gas Flow
65
Avg. Liq. Density
66
Specific Heat
(Btu/lbmole-F)
18.78
67
Std. Gas Flow
(MMSCFD)
0.9090
68
Std. Ideal Liq. Mass Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
2.898
4.337
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
-4.677e-002
4.321
-6.569e-002
-1430 0.5007
18.78
6.926
18.89
13.94
1.067
1.597
1.086
0.5015
9538
2.617e+004
9232
1.851e+004
9.966e+008
---
9.956e+008
9.532e+011
(lbmole/ft3)
3.716e-002
---
3.921e-002
1.006e-003
(lbmol/lb)
7.286e-004
---
7.526e-004
(Btu/lb)
(Btu/lb) (psia) (Cost/s) (ACFM) (lbmole/ft3)
(lb/ft3)
8037
2.392e-005
2.240e+004
7732
1.701e+004
3.033e-004
3.033e-004
0.9489
5.077e-002
7.380e-005
7.380e-005
0.9671
3.283e-002
1.351e-002
1.351e-002
0.9467
3.980e-002
397.7 7.982e-006 0.0000 7.769e-003 2.162
38.06
---
---
---
---
---
0.0000
0.0000
0.0000
7.769e-003 2.135 6.926 2.723e-004 9.260
---
---
---
2.231
0.8856
18.89 0.8898 38.79
Aspen HYSYS Version 8.8 (34.0.0.8909)
13.94 1.890e-002 24.61
Page 273 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1000 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Act. Liq. Flow
13
Z Factor
14
Watson K
15
User Property
16
Partial Pressure of H2S
17
Cp/(Cp - R)
18
Cp/Cv
19
Heat of Vap.
20
Kinematic Viscosity
21
Liq. Mass Density (Std. Cond)
22
Liq. Vol. Flow (Std. Cond)
23
Liquid Fraction
24
Molar Volume
25
Mass Heat of Vap.
26
Phase Fraction [Molar Basis]
27
Surface Tension
28
Thermal Conductivity
29
Viscosity
30
Cv (Semi-Ideal)
31
Mass Cv (Semi-Ideal)
32
Cv
33
Mass Cv
34
Cv (Ent. Method)
35
Mass Cv (Ent. Method)
36
Cp/Cv (Ent. Method)
37
Reid VP at 37.8 C
38
True VP at 37.8 C
39 40
(USGPS)
Vapour Phase
7.074e-002
(psia)
(Btu/lbmole)
Liquid Phase
6.789e-002
2.854e-003
---
0.9771
2.096e-002
4.148e-002
12.30
24.03
12.12
16.79
---
---
---
---
0.0000
---
---
---
1.118
1.402
1.117
1.166
1.000
1.462
1.000
1.357
---
---
---
0.8471
12.41
0.9411
1.808e+004
(cSt)
---
(lb/ft3)
38.32
(barrel/day)
Liquid Phase
---
1.145e-002
38.75
7.384e-002
196.4
48.51
187.8
3346
0.9997
0.0000
1.000
1.000
(ft3/lbmole)
0.3451
15.56
0.3337
0.6606
(Btu/lb)
1027
---
---
---
0.0003
0.0003
0.9789
0.0208
(dyne/cm)
---
73.26
27.79
(Btu/hr-ft-F)
---
3.351e-002
0.5407
0.1267
---
3.781e-003
(cP)
---
10.36
0.6342
16.79
4.941
16.90
---
0.9541
1.139
0.9719
---
18.78
4.738
18.89
---
1.067
1.092
1.086
---
---
---
17.04
---
---
---
0.9798
---
---
---
1.109
---
(psia)
259.4
---
223.8
---
(psia)
383.4
---
232.8
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
236.3
48.51
187.8
0.0000
Viscosity Index
24.35
---
---
---
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
41
COMPOSITION
42 43
Overall Phase
44 45
COMPONENTS
46
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0003
LIQUID VOLUME FRACTION
47
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
48
H2O
0.0073
0.0001
0.1314
0.0001
0.0090
0.0000
49
Oxygen
0.3167
0.0032
10.1331
0.0058
0.6099
0.0031
50
Methane
0.3692
0.0037
5.9229
0.0034
1.3546
0.0069
51
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
Hydrogen
0.0290
0.0003
0.0585
0.0000
0.0574
0.0003
53
Ethane
1.4056
0.0141
42.2649
0.0240
8.1365
0.0412
54
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
CO2
1.2825
0.0128
56.4434
0.0321
4.6828
0.0237
56
Nitrogen
0.0259
0.0003
0.7247
0.0004
0.0615
0.0003
57
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Ammonia
96.5630
0.9656
1644.4678
0.9343
182.7736
0.9246
61
Total
99.9992
1.0000
1760.1478
1.0000
197.6853
1.0000
62
Vapour Phase
63 64
COMPONENTS
65
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
2.995e-004 LIQUID VOLUME FRACTION
66
CO
0.0000
0.0000
0.0000
0.0002
0.0000
0.0000
67
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Oxygen
0.0011
0.0370
0.0355
0.2731
0.0021
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0356
Page 274 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1000 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
2.995e-004 LIQUID VOLUME FRACTION
15
Methane
0.0002
0.0061
0.0030
0.0227
0.0007
0.0113
16
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Hydrogen
0.0274
0.9136
0.0552
0.4247
0.0541
0.9017
18
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Nitrogen
0.0013
0.0432
0.0363
0.2793
0.0031
0.0514
22
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Total
0.0300
1.0000
0.1299
1.0000
0.0600
1.0000
27
Liquid Phase
28 29
COMPONENTS
30
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9789 LIQUID VOLUME FRACTION
31
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
H2O
0.0073
0.0001
0.1314
0.0001
0.0090
0.0000
33
Oxygen
0.0296
0.0003
0.9487
0.0006
0.0571
0.0003
34
Methane
0.0052
0.0001
0.0833
0.0000
0.0191
0.0001
35
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Ethane
0.0117
0.0001
0.3518
0.0002
0.0677
0.0004
38
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
CO2
1.2811
0.0131
56.3825
0.0331
4.6777
0.0249
40
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Ammonia
96.5547
0.9864
1644.3272
0.9660
182.7580
0.9742
45
Total
97.8897
1.0000
1702.2250
1.0000
187.5886
1.0000
46
Liquid Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
2.079e-002 LIQUID VOLUME FRACTION
50
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
51
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
Oxygen
0.2859
0.1375
9.1489
0.1583
0.5506
0.0549
53
Methane
0.3638
0.1750
5.8366
0.1010
1.3349
0.1330
54
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Hydrogen
0.0017
0.0008
0.0033
0.0001
0.0033
0.0003
56
Ethane
1.3939
0.6703
41.9131
0.7252
8.0687
0.8039
57
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
CO2
0.0014
0.0007
0.0608
0.0011
0.0050
0.0005
59
Nitrogen
0.0246
0.0118
0.6884
0.0119
0.0585
0.0058
60
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Ammonia
0.0083
0.0040
0.1406
0.0024
0.0156
0.0016
64
Total
2.0795
1.0000
57.7928
1.0000
10.0367
1.0000
65
K VALUE
66 67
COMPONENTS
68 69
MIXED CO
Aspen Technology Inc. Licensed to: LEGENDS
LIGHT 70.80
Aspen HYSYS Version 8.8 (34.0.0.8909)
HEAVY 2.002e+004
1.478
Page 275 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1000 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
H2O
13
Oxygen
11.73
122.2
14
Methane
1.664
115.8
15
4.996e-027
H2S
16
4.892e-027
---
0.2692 3.510e-002
---
---
Hydrogen
5.480e+004
7.090e+006
17
Ethane
3.473e-004
4.085e-002
18
Propane
19
CO2
20
Nitrogen
21
---
1149 7.284e-006
---
5.425e-006
---
5.317e-006
175.9
Air
1.518e-004
1.047e-004
1.182e+007
---
---
---
---
3.659 ---
22
Mercury
23
MEAmine
2.394e-033
2.344e-033
4.419e-029
24
Ammonia
1.067e-010
1.045e-010
2.596e-008
25
---
UNIT OPERATIONS
26 27
FEED TO
PRODUCT FROM
28
Distillation:
LOGICAL CONNECTION T-7
29
UTILITIES
30 31
( No utilities reference this stream )
32
PROCESS UTILITY
33 34 35
DYNAMICS
36 37
Pressure Specification
(Inactive):
38
Flow Specification
(Inactive) Molar:
114.7 psia 100.0 lbmole/hrMass:
39
1760 lb/hr Std Ideal Liq Volume:
197.7 barrel/day
User Variables
40 41
NOTES
42 43 44
Description
45 46 47
Material Stream: 1001
48 49 50
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
51 52
Overall
53
Vapour / Phase Fraction
54
Temperature:
55
Pressure:
56
Molar Flow
57
Mass Flow
58
Std Ideal Liq Vol Flow
59
Molar Enthalpy
(Btu/lbmole)
60
Molar Entropy
(Btu/lbmole-F)
61
Heat Flow
62
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
76.75
76.75
(psia)
114.7
114.7
281.9
281.9
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
4853
4853
501.4
501.4
-4.601e+004 18.22 -1.297e+007 496.1*
(barrel/day)
63
-4.601e+004 18.22 -1.297e+007 496.1
PROPERTIES
64 65
Overall
66
Molecular Weight
67
Molar Density
68
Mass Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
Liquid Phase 17.22
17.22
2.385
2.385
41.06
41.06
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 276 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1001 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Act. Volume Flow
13
Liquid Phase
(barrel/day)
505.2
505.2
Mass Enthalpy
(Btu/lb)
-2672
-2672
14
Mass Entropy
(Btu/lb-F)
1.058
1.058
15
Heat Capacity
19.31
19.31
16
Mass Heat Capacity
17
LHV Molar Basis (Std)
(Btu/lbmole)
1.125e+005
1.125e+005
18
HHV Molar Basis (Std)
(Btu/lbmole)
1.375e+005
1.375e+005
19
HHV Mass Basis (Std)
20
CO2 Loading
21
CO2 App ML Con
22
CO2 App WT Con
23
LHV Mass Basis (Std)
24
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.122
7984
1.122
7984
1.381e-006
1.381e-006
(lbmole/ft3)
1.034e-009
1.034e-009
(lbmol/lb)
2.519e-011
2.519e-011
(Btu/lb)
6537
6537
Phase Fraction [Vol. Basis]
0.0000
1.000
25
Phase Fraction [Mass Basis]
0.0000
1.000
26
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
27
Mass Exergy
(Btu/lb)
77.63
---
28
Partial Pressure of CO2
(psia)
0.0000
---
29
Cost Based on Flow
(Cost/s)
0.0000
0.0000
30
Act. Gas Flow
31
Avg. Liq. Density
32 33 34
Std. Ideal Liq. Mass Density
35
Act. Liq. Flow
36
Z Factor
37
Watson K
38
User Property
39
Partial Pressure of H2S
40
Cp/(Cp - R)
41
Cp/Cv
42
Heat of Vap.
43
Kinematic Viscosity
44
Liq. Mass Density (Std. Cond)
45
Liq. Vol. Flow (Std. Cond)
46
Liquid Fraction
47
Molar Volume
48
Mass Heat of Vap.
49
Phase Fraction [Molar Basis]
50
Surface Tension
51
Thermal Conductivity
52
Viscosity
53
Cv (Semi-Ideal)
54
Mass Cv (Semi-Ideal)
55
Cv
56
Mass Cv
57
Cv (Ent. Method)
58
Mass Cv (Ent. Method)
59
Cp/Cv (Ent. Method)
60
Reid VP at 37.8 C
61
True VP at 37.8 C
62
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
63
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
2.403
2.403
Specific Heat
(Btu/lbmole-F)
19.31
19.31
Std. Gas Flow
(MMSCFD)
2.562
2.562
(lb/ft3)
41.38
41.38
(USGPS)
0.2456
0.2456
8.354e-003
(psia)
(Btu/lbmole)
8.354e-003
12.24
12.24
---
---
0.0000
---
1.115
1.115
1.115
1.115
1.284e+004
---
(cSt)
0.2700
0.2700
(lb/ft3)
41.81
41.81
496.1
496.1
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4193
0.4193
745.6
---
0.0000
1.0000
(dyne/cm)
34.13
34.13
(Btu/hr-ft-F)
0.2894
0.2894
0.1776
0.1776
17.33
17.33
1.006
1.006
17.33
17.33
1.006
1.006
---
---
---
---
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
---
(psia)
210.4
210.4
(psia)
168.2
168.2
496.1
496.1
-28.18
---
64 65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 277 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1001 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
28
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
29
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
47
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
48
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
0.0000
0.0000
---
53
H2O
0.0000
0.0000
---
54
Oxygen
0.0000
0.0000
---
55
Methane
0.0000
0.0000
---
---
---
---
56
H2S
57
Hydrogen
0.0000
0.0000
---
58
Ethane
0.0000
0.0000
---
59
Propane
---
---
---
60
CO2
0.0000
0.0000
---
61
Nitrogen
0.0000
0.0000
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
0.0000
0.0000
---
65
Ammonia
0.0000
0.0000
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 278 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1001 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Cooler:
E-107
Distillation:
LOGICAL CONNECTION T-7
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
114.7 psia 281.9 lbmole/hrMass:
23
4853 lb/hr Std Ideal Liq Volume:
501.4 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 94-
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
110.0*
110.0
(psia)
229.7*
229.7
2349*
(lbmole/hr) (lb/hr)
3.772e+004 5579 -2.337e+004 31.08
2349 3.772e+004 5579 -2.337e+004 31.08
(Btu/hr)
-5.489e+007
-5.489e+007
(barrel/day)
* 3.801e+006
3.801e+006
47
PROPERTIES
48 49
Overall
Vapour Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-1455
-1455
55
Mass Entropy
(Btu/lb-F)
1.935
1.935
56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
7.748e+004
7.748e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
8.874e+004
8.874e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66
16.06 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
0.6049 2.665e+005
16.06 3.767e-002 0.6049 2.665e+005
7.431
7.431
0.4627
0.4627
5525
5525
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
4824
4824
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
67
Phase Fraction [Act. Vol. Basis]
1.000
1.000
68
Mass Exergy
182.6
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
3.767e-002
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 279 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 94- (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
(psia)
27.40
---
(Cost/s)
0.0000
0.0000
(ACFM)
1039
1039
(lbmole/ft3)
1.799
1.799
Specific Heat
(Btu/lbmole-F)
7.431
7.431
Std. Gas Flow
(MMSCFD)
21.35
21.35
(lb/ft3)
28.90
28.90
(USGPS)
---
---
0.9975
0.9975
10.51
10.51
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.365
1.365
1.390
1.390
5705
---
1.407
1.407
4.242e-002
4.242e-002
3.801e+006
3.801e+006
0.0000
0.0000
(ft3/lbmole)
26.55
26.55
(Btu/lb)
355.2
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
4.304e-002
4.304e-002
1.363e-002
1.363e-002
5.445
5.445
0.3391
0.3391
5.344
5.344
0.3328
0.3328
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.801e+006 -30.27
48
3.801e+006 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
54
CO
* 58.9761
* 0.0251
* 1651.9750
* 0.0438
* 141.5025
* 0.0254
55
H2O
* 14.4510
* 0.0062
* 260.3363
* 0.0069
* 17.8619
* 0.0032
56
Oxygen
* 134.8287
* 0.0574
* 4314.5184
* 0.1144
* 259.6752
* 0.0465
57
Methane
* 75.8667
* 0.0323
* 1217.1211
* 0.0323
* 278.3614
* 0.0499
58
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
59
Hydrogen
60
Ethane
61
Propane
62
* 0.0000
* 1234.9677
* 0.5258
* 2489.6950
* 0.0660
* 2440.2900
* 0.4374
* 32.8159
* 0.0140
* 986.7710
* 0.0262
* 189.9641
* 0.0340
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
CO2
* 280.2107
* 0.1193
* 12331.9893
* 0.3269
* 1023.1072
* 0.1834
63
Nitrogen
* 516.4873
* 0.2199
* 14468.3579
* 0.3836
* 1228.5731
* 0.2202
64
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
65
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
66
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
67
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
68
Total
69
Aspen Technology Inc. Licensed to: LEGENDS
2348.6041
1.0000
37720.7641
1.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
5579.3353
1.0000
Page 280 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 94- (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
16
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
17
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
18
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
21
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
24
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
37720.7641
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Stream Cutter:
94-Cutter Recycle:
51
LOGICAL CONNECTION RCY-4
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Inactive) Molar:
61
* 229.7 psia * Mass: 2349 lbmole/hr
3.772e+004 lb/hrStd Ideal Liq Volume:
5579 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 281 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 94+
7 8 9
Fluid Package:
Basis-2
Property Package:
Acid Gas
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.9999
0.9999
0.0001
(F)
110.0
110.0
110.0
(psia)
229.7
229.7
229.7
2349
2348
0.2814
(lbmole/hr) (lb/hr)
3.772e+004
(barrel/day)
8648 -2.334e+004 -2.978
3.772e+004 8647 -2.333e+004 -2.974
(Btu/hr)
-5.483e+007
-5.479e+007
(barrel/day)
* 1.142e+004
1.142e+004
22
5.075 0.3484 -1.223e+005 -37.88 -3.442e+004 0.3481
PROPERTIES
23 24
Overall
Vapour Phase
Aqueous Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-1453
-1453
-6782
30
Mass Entropy
(Btu/lb-F)
-0.1854
-0.1852
-2.101
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
7.745e+004
7.746e+004
34
HHV Molar Basis (Std)
(Btu/lbmole)
8.871e+004
8.872e+004
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
38
CO2 App WT Con
(lbmol/lb)
39
LHV Mass Basis (Std)
(Btu/lb)
40
Phase Fraction [Vol. Basis]
1.000
1.000
4.029e-005
41
Phase Fraction [Mass Basis]
0.9999
0.9999
1.345e-004
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
1.315e-006
43
Mass Exergy
(Btu/lb)
182.8
---
44
Partial Pressure of CO2
(psia)
27.41
---
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
16.06 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.757e-002 0.6034 2.672e+005
16.06 3.757e-002 0.6033 2.672e+005
18.03 3.424 61.75 0.3513
7.454
7.452
18.00
0.4641
0.4640
0.9981 17.82 1.764e+004
5523
5524
---
---
977.9
---
---
2.497e-003
---
---
4.044e-005
4822
4823
---
0.9880
---
(ACFM)
1042
1042
---
(lbmole/ft3)
1.161
1.161
3.452
Specific Heat
(Btu/lbmole-F)
7.454
7.452
Std. Gas Flow
(MMSCFD)
21.35
21.35
18.65
18.64
Licensed to: LEGENDS
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
1.708e-004
(Btu/lb)
1.708e-004 1.097e-002
---
1.000 15.79
9.357
---
---
---
0.0000
---
---
1.363
1.363
1.124
1.387
1.387
1.033
---
---
---
---
1.703
0.6340
14.12 1.142e+004 26.62
14.12 1.142e+004
62.32 0.3481
0.0000
1.000
26.62
0.2920
-877.1
---
---
0.9999
0.9999
0.0001
(dyne/cm)
69.12
(Btu/hr-ft-F)
---
(cP)
62.26
---
15.79
1.198e-004 (ft3/lbmole)
18.00 2.558e-003
---
---
69.12
4.864e-002
0.3388
1.646e-002
0.6271
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 282 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 94+ (continued)
7 8 9
Fluid Package:
Basis-2
Property Package:
Acid Gas
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Aqueous Phase
5.468
5.466
16.01
0.3404
0.3404
0.8879
5.373
5.372
17.43
0.3346
0.3345
0.9666
---
---
14.46
(Btu/lb-F)
---
---
0.8017
---
---
1.245
Reid VP at 37.8 C
(psia)
5181
5181
1958
20
True VP at 37.8 C
(psia)
---
---
220.8
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
23
pH[Ele]
24
Ionic Strength[Ele]
25
Heat Capacity[Ele]
26
pOH[Ele]
27
Osmotic Coefficient[Ele]
(lbmol/lb) (Btu/lbmole-F)
1.142e+004
1.142e+004
0.3481
---
---
---
3.872
---
3.872
2.465e-006
---
2.465e-006
7.454
7.452
9.591
---
9.591
0.9995
---
0.9995
28
18.00
COMPOSITION
29 30
Overall Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
0.9999
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
34
CO
58.9761
0.0251
1651.9455
0.0438
216.2805
0.0250
35
H2O
14.4510
0.0062
260.3389
0.0069
17.8605
0.0021
36
Oxygen
134.8287
0.0574
4314.3566
0.1144
494.4511
0.0572
37
Methane
75.8667
0.0323
1217.1105
0.0323
278.2223
0.0322
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1234.9677
0.5258
2489.5468
0.0660
4528.9405
0.5237
40
Ethane
32.8159
0.0140
986.7624
0.0262
190.3468
0.0220
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
280.2107
0.1193
12332.0171
0.3269
1027.6039
0.1188
43
Nitrogen
516.4873
0.2199
14468.6055
0.3836
1894.0900
0.2190
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
2348.6041
1.0000
1.0000
8647.7956
1.0000
48
37720.6835
Vapour Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
0.9999
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
52
CO
58.9761
0.0251
1651.9454
0.0438
216.2805
0.0250
53
H2O
14.1698
0.0060
255.2737
0.0068
17.5130
0.0020
54
Oxygen
134.8287
0.0574
4314.3565
0.1144
494.4511
0.0572
55
Methane
75.8667
0.0323
1217.1105
0.0323
278.2223
0.0322
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
1234.9677
0.5259
2489.5467
0.0660
4528.9404
0.5237
58
Ethane
32.8159
0.0140
986.7624
0.0262
190.3468
0.0220
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
280.2105
0.1193
12332.0081
0.3270
1027.6031
0.1188
61
Nitrogen
516.4873
0.2199
14468.6053
0.3836
1894.0900
0.2190
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Total
2348.3227
1.0000
1.0000
8647.4472
1.0000
37715.6086
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 283 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 94+ (continued)
7 8 9
Fluid Package:
Basis-2
Property Package:
Acid Gas
COMPOSITION
10 11
Aqueous Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.198e-004 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.2812
0.9991
5.0653
0.9981
0.3475
0.9973
17
Oxygen
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0001
0.0001
0.0000
0.0001
0.0003
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0002
0.0007
0.0090
0.0018
0.0008
0.0022
24
Nitrogen
0.0000
0.0000
0.0003
0.0001
0.0000
0.0001
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
0.2814
1.0000
5.0749
1.0000
0.3484
1.0000
29
K VALUE
30 31
COMPONENTS
MIXED
32
CO
33
H2O
LIGHT 4732
HEAVY ---
6.039e-003
4732
---
6.039e-003
34
Oxygen
3636
---
3636
35
Methane
3452
---
3452
---
---
---
Hydrogen
4847
---
4847
38
Ethane
3225
---
3225
39
Propane
---
---
---
40
CO2
163.6
---
163.6
41
Nitrogen
6799
---
6799
---
---
---
36
H2S
37
42
Air
43
Mercury
---
---
---
44
MEAmine
---
---
---
45
UNIT OPERATIONS
46 47 48
FEED TO
PRODUCT FROM
Absorber:
T-100
49
Stream Cutter:
LOGICAL CONNECTION 94-Cutter
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
229.7 psia 2349 lbmole/hrMass:
3.772e+004 lb/hrStd Ideal Liq Volume:
8648 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 284 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: a
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Aqueous Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
1.839e+005
1.839e+005
18
Molar Enthalpy
(Btu/lbmole)
-1.224e+005
-1.224e+005
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
0.0000
1.0000
(F)
110.1
110.1
(psia)
274.7*
(lbmole/hr) (lb/hr)
274.7
1.486e+005
1.486e+005
2.679e+006
2.679e+006
13.95
13.95
(Btu/hr)
-1.820e+010
-1.820e+010
(barrel/day)
* 1.807e+005
1.807e+005
22
PROPERTIES
23 24
Overall
Aqueous Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-6791
-6791
30
Mass Entropy
(Btu/lb-F)
0.7735
0.7735
31
Heat Capacity
32
Mass Heat Capacity
33
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F)
18.03
18.03
3.442
3.442
62.06 1.845e+005
62.06 1.845e+005
18.57
18.57
(Btu/lb-F)
1.030
1.030
LHV Molar Basis (Std)
(Btu/lbmole)
1.714
34
HHV Molar Basis (Std)
(Btu/lbmole)
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
2.053e-003
2.053e-003
38
CO2 App WT Con
(lbmol/lb)
3.308e-005
3.308e-005
39
LHV Mass Basis (Std)
(Btu/lb)
9.508e-002
9.508e-002
40
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
1.938
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lb)
1.762e+004 977.3 ---
1.714 1.762e+004 977.3 ---
(ACFM)
---
---
(lbmole/ft3)
3.454
3.454
Specific Heat
(Btu/lbmole-F)
18.57
18.57
Std. Gas Flow
(MMSCFD)
1351
1351
62.28
62.28
Licensed to: LEGENDS
(lb/ft3) (USGPS)
89.71 1.305e-002
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb)
89.71 1.305e-002
8.466
8.466
---
---
0.0000
---
1.120
1.120
1.157
1.157
1.579e+004 0.6154 63.37 1.807e+005
--0.6154 63.37 1.807e+005
1.000
1.000
0.2905
0.2905
875.6
---
0.0000
1.0000
(dyne/cm)
68.86
68.86
(Btu/hr-ft-F)
0.3673
0.3673
0.6118
0.6118
(cP)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 285 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: a (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Aqueous Phase
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
---
---
20
True VP at 37.8 C
(psia)
232.7
232.7
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.58
16.58
0.9196
0.9196
16.05
16.05
0.8900
0.8900
15.78
15.78
0.8753
0.8753
1.176
1.176
1.807e+005
1.807e+005
-4.392
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
30
H2O
31
Oxygen
0.6059
0.0000
19.3875
0.0000
1.1669
0.0000
32
Methane
0.0012
0.0000
0.0186
0.0000
0.0043
0.0000
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
2.2934
0.0000
4.6235
0.0000
4.5317
0.0000
35
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
88.6369
0.0006
3900.8838
0.0015
323.6317
0.0018
38
Nitrogen
5.0873
0.0000
142.5111
0.0001
12.1013
0.0001
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
0.1299 148503.7872
148600.5418
0.0000
3.6398
0.9993
2.675310649e+06
1.0000
44
2.679381713e+06
0.0000
0.3118
0.9985
1.0000
46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
0.9981
183897.5147
Aqueous Phase
45
0.0000
183555.7671
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
49
H2O
50
Oxygen
0.6059
0.0000
19.3875
0.0000
1.1669
0.0000
51
Methane
0.0012
0.0000
0.0186
0.0000
0.0043
0.0000
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
2.2934
0.0000
4.6235
0.0000
4.5317
0.0000
54
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
88.6369
0.0006
3900.8838
0.0015
323.6317
0.0018
57
Nitrogen
5.0873
0.0000
142.5111
0.0001
12.1013
0.0001
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
0.1299 148503.7872
148600.5418
0.0000 0.9993
1.0000
63
2.679381713e+06
0.0000
0.3118
0.9985
0.0000
183555.7671
1.0000
0.9981
183897.5147
1.0000
K VALUE
64 65
3.6398 2.675310649e+06
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
0.0000
---
0.0000
67
H2O
0.0000
---
0.0000
68
Oxygen
0.0000
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 286 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: a (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
LIGHT
HEAVY
0.0000
---
---
---
---
Hydrogen
0.0000
---
0.0000
15
Ethane
0.0000
---
0.0000
16
Propane
---
---
---
17
CO2
0.0000
---
0.0000
18
Nitrogen
0.0000
---
0.0000
---
---
---
13
H2S
14
19
Air
0.0000
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Recycle:
RCY-1
Pump:
LOGICAL CONNECTION P-100
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Inactive) Molar:
* 274.7 psia
1.486e+005 lbmole/hr Mass:
37
2.679e+006 lb/hrStd Ideal Liq Volume: 1.839e+005 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: ACIDO NITRICO
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
205.2
205.2
(psia)
114.7
114.7
(lbmole/hr) (lb/hr)
896.0 1.524e+004 1999 -1.660e+004 35.61
896.0 1.524e+004 1999 -1.660e+004 35.61
(Btu/hr)
-1.488e+007
-1.488e+007
(barrel/day)
* 1.449e+006
1.449e+006
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.01
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
1.613e-002 0.2744 2.374e+005 -976.3
17.01 1.613e-002 0.2744 2.374e+005 -976.3
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 287 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: ACIDO NITRICO (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
8.317e+004
8.317e+004
16
HHV Molar Basis (Std)
(Btu/lbmole)
9.616e+004
9.616e+004
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22 23
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.094
2.094
7.595
7.595
0.4466
0.4466
5654
5654
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
4890
4890
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
24
Phase Fraction [Act. Vol. Basis]
1.000
1.000
25
Mass Exergy
(Btu/lb)
138.6
---
26
Partial Pressure of CO2
(psia)
1.156
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30
(ACFM)
925.6
925.6
(lbmole/ft3)
1.916
1.916
Specific Heat
(Btu/lbmole-F)
7.595
7.595
31
Std. Gas Flow
(MMSCFD)
8.145
8.145
32
Std. Ideal Liq. Mass Density
(lb/ft3)
32.59
32.59
33
Act. Liq. Flow
(USGPS)
---
---
34
Z Factor
0.9963
0.9963
35
Watson K
9.936
9.936
36
User Property
---
---
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(psia)
(Btu/lbmole) (cSt)
0.0000
---
1.354
1.354
1.370
1.370
1.077e+004 3.502
(lb/ft3) (barrel/day)
--3.502
4.497e-002
4.497e-002
1.449e+006
1.449e+006
0.0000
0.0000
(ft3/lbmole)
61.98
61.98
(Btu/lb)
633.3
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
3.840e-002
3.840e-002
1.539e-002
1.539e-002
5.609
5.609
0.3298
0.3298
5.542
5.542
0.3259
0.3259
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.449e+006 -15.65
62
1.449e+006 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.1887
MOLE FRACTION 0.0002
MASS FLOW (lb/hr) 5.2847
Vapour Fraction MASS FRACTION 0.0003
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.4527
1.0000
LIQUID VOLUME FRACTION 0.0002
Page 288 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: ACIDO NITRICO (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
H2O
103.3251
0.1153
1861.4115
0.1221
127.7133
0.0639
16
Oxygen
130.1930
0.1453
4166.1757
0.2734
250.7470
0.1255
17
Methane
78.0631
0.0871
1252.3578
0.0822
286.4202
0.1433
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
326.8026
0.3647
658.8341
0.0432
645.7603
0.3231
20
Ethane
20.0052
0.0223
601.5541
0.0395
115.8057
0.0579
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
9.0319
0.0101
397.4930
0.0261
32.9775
0.0165
23
Nitrogen
219.0314
0.2444
6135.7258
0.4026
521.0120
0.2607
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0002
0.0000
0.0133
0.0000
0.0009
0.0000
27
Ammonia
9.3925
0.0105
159.9543
0.0105
17.7780
0.0089
28
Total
896.0336
1.0000
15238.8043
1.0000
1998.6675
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
33
CO
0.1887
0.0002
5.2847
0.0003
0.4527
0.0002
34
H2O
103.3251
0.1153
1861.4115
0.1221
127.7133
0.0639
35
Oxygen
130.1930
0.1453
4166.1757
0.2734
250.7470
0.1255
36
Methane
78.0631
0.0871
1252.3578
0.0822
286.4202
0.1433
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
326.8026
0.3647
658.8341
0.0432
645.7603
0.3231
39
Ethane
20.0052
0.0223
601.5541
0.0395
115.8057
0.0579
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
9.0319
0.0101
397.4930
0.0261
32.9775
0.0165
42
Nitrogen
219.0314
0.2444
6135.7258
0.4026
521.0120
0.2607
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0002
0.0000
0.0133
0.0000
0.0009
0.0000
46
Ammonia
9.3925
0.0105
159.9543
0.0105
17.7780
0.0089
47
Total
896.0336
1.0000
15238.8043
1.0000
1998.6675
1.0000
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
---
---
---
52
H2O
---
---
---
53
Oxygen
---
---
---
54
Methane
---
---
---
---
---
---
55
H2S
56
Hydrogen
---
---
---
57
Ethane
---
---
---
58
Propane
---
---
---
59
CO2
---
---
---
60
Nitrogen
---
---
---
---
---
---
61
Air
62
Mercury
---
---
---
63
MEAmine
---
---
---
64
Ammonia
---
---
---
65
UNIT OPERATIONS
66 67
FEED TO
68 69
PRODUCT FROM Absorber:
Aspen Technology Inc. Licensed to: LEGENDS
LOGICAL CONNECTION T-101
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 289 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: ACIDO NITRICO (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Inactive):
18
Flow Specification
(Inactive) Molar:
114.7 psia 896.0 lbmole/hrMass:
19
1.524e+004 lb/hrStd Ideal Liq Volume:
1999 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: Aire-1
28 29 30
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
Vapour Phase
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
1470
39
Molar Enthalpy
(Btu/lbmole)
1417
1417
40
Molar Entropy
(Btu/lbmole-F)
32.81
32.81
41
Heat Flow
42
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
282.0*
282.0
(psia)
254.7*
254.7
643.9*
(lbmole/hr) (lb/hr)
1.858e+004
643.9 1.858e+004 1470
(Btu/hr)
9.123e+005
9.123e+005
(barrel/day)
* 1.042e+006
1.042e+006
43
PROPERTIES
44 45
Overall
Vapour Phase
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Mass Enthalpy
(Btu/lb)
49.11
49.11
51
Mass Entropy
(Btu/lb-F)
1.137
1.137
52
Heat Capacity
53
Mass Heat Capacity
54 55 56
HHV Mass Basis (Std)
57
CO2 Loading
58
CO2 App ML Con
59
CO2 App WT Con
60
LHV Mass Basis (Std)
61 62
28.85 (lbmole/ft3) (lb/ft3) (barrel/day)
0.9211 8.620e+004
28.85 3.193e-002 0.9211 8.620e+004
7.238
7.238
(Btu/lb-F)
0.2509
0.2509
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
HHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
0.0000
0.0000
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
63
Phase Fraction [Act. Vol. Basis]
1.000
1.000
64
Mass Exergy
(Btu/lb)
112.9
---
65
Partial Pressure of CO2
(psia)
0.0000
---
66
Cost Based on Flow
(Cost/s)
0.0000
0.0000
67
Act. Gas Flow
(ACFM)
336.1
336.1
68
Avg. Liq. Density
(lbmole/ft3)
1.872
1.872
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lbmole-F)
3.193e-002
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 290 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Aire-1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Specific Heat
(Btu/lbmole-F)
7.238
7.238
13
Std. Gas Flow
(MMSCFD)
5.853
5.853
14
Std. Ideal Liq. Mass Density
(lb/ft3)
54.00
54.00
15
Act. Liq. Flow
(USGPS)
---
---
16
Z Factor
1.002
1.002
17
Watson K
6.042
6.042
18
User Property
---
---
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
41
True VP at 37.8 C
42
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
43
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.378
1.378
1.400
1.400
1632
---
1.627
1.627
7.622e-002
7.622e-002
1.042e+006
1.042e+006
0.0000
0.0000
(ft3/lbmole)
31.32
31.32
(Btu/lb)
56.57
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.980e-002
1.980e-002
2.400e-002
2.400e-002
5.252
5.252
0.1820
0.1820
5.169
5.169
0.1792
0.1792
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.042e+006 -24.67
44
1.042e+006 ---
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
50
CO
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
51
H2O
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
52
Oxygen
* 135.2105
* 0.2100
* 0.2329
* 260.4106
* 0.1771
53
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
54
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
55
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
56
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
57
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
58
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
59
Nitrogen
* 508.6491
* 0.7900
60
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
61
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
62
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
63
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
64
Total
643.8596
1.0000
* 4326.7368
* 14248.7881
18575.5250
* 0.7671
1.0000
* 1209.9284
1470.3390
* 0.8229
1.0000
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 291 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Aire-1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
135.2105
0.2100
4326.7368
0.2329
260.4106
0.1771
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
508.6491
0.7900
0.7671
1209.9284
0.8229
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
643.8596
1.0000
1.0000
1470.3390
1.0000
14248.7881
18575.5250
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Mixer:
LOGICAL CONNECTION
MIX-100
51
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Active):
60
Flow Specification
(Active)
61
* 254.7 psia
Molar:
* Mass: 643.9 lbmole/hr
1.858e+004 lb/hrStd Ideal Liq Volume:
1470 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 292 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: AMINA
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Liquid Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
2.054e+004
2.054e+004
18
Molar Enthalpy
(Btu/lbmole)
-1.007e+005
-1.007e+005
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
0.0000
1.0000
(F)
407.7
407.7
(psia)
190.0
190.0
(lbmole/hr) (lb/hr)
5020 3.033e+005
24.43
5020 3.033e+005
24.43
(Btu/hr)
-5.054e+008
-5.054e+008
(barrel/day)
* 2.041e+004
2.041e+004
22
PROPERTIES
23 24
Overall
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-1666
-1666
30
Mass Entropy
(Btu/lb-F)
0.4044
0.4044
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
5.668e+005
5.668e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
6.265e+005
6.265e+005
35
HHV Mass Basis (Std)
1.037e+004
1.037e+004
36
CO2 Loading
3.103e-002
3.103e-002
37
CO2 App ML Con
(lbmole/ft3)
2.356e-002
2.356e-002
38
CO2 App WT Con
(lbmol/lb)
4.963e-004
4.963e-004
39
LHV Mass Basis (Std)
40
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
60.42
60.42
0.7855
0.7855
47.46 2.732e+004
47.46 2.732e+004
53.34
53.34
0.8828
0.8828
9380
9380
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
58.93
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
1.045
1.045
Specific Heat
(Btu/lbmole-F)
53.34
53.34
Std. Gas Flow
(MMSCFD)
45.63
45.63
(lb/ft3)
63.12
63.12
(USGPS)
13.28
Licensed to: LEGENDS
2.598e-002
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
13.28 2.598e-002
9.099
9.099
---
---
0.0000
---
1.039
1.039
1.039
1.039
2.081e+004 0.9731 63.54 2.041e+004
--0.9731 63.54 2.041e+004
1.000
1.000
(ft3/lbmole)
1.273
1.273
(Btu/lb)
344.3
---
0.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
17.31 7.049e-002 0.7398
17.31 7.049e-002 0.7398
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 293 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: AMINA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Liquid Phase 51.36
51.36
0.8499
0.8499
51.36
51.36
0.8499
0.8499
---
---
---
---
---
---
21.16
21.16
37.71
37.71
2.041e+004
2.041e+004
2.873
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
30
H2O
14.4510
0.0029
260.3363
0.0009
17.8619
0.0009
31
Oxygen
0.0005
0.0000
0.0151
0.0000
0.0009
0.0000
32
Methane
0.0046
0.0000
0.0743
0.0000
0.0170
0.0000
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
3.8453
0.0008
115.6287
0.0004
22.2598
0.0011
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
150.5434
0.0300
6625.3710
0.0218
549.6652
0.0268
38
Nitrogen
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
4850.9181
0.9664
42
Ammonia
0.0000
0.0000
43
Total
5019.7630
1.0000
44
296312.9955 0.0000 303314.4222
0.9769
19950.8243
0.0000 1.0000
46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
0.0000
20540.6292
Liquid Phase
45
0.9713
0.0000
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
49
H2O
14.4510
0.0029
260.3363
0.0009
17.8619
0.0009
50
Oxygen
0.0005
0.0000
0.0151
0.0000
0.0009
0.0000
51
Methane
0.0046
0.0000
0.0743
0.0000
0.0170
0.0000
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
3.8453
0.0008
115.6287
0.0004
22.2598
0.0011
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
150.5434
0.0300
6625.3710
0.0218
549.6652
0.0268
57
Nitrogen
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
4850.9181
0.9664
61
Ammonia
0.0000
0.0000
62
Total
5019.7630
1.0000
63
0.0000 303314.4222
0.9769
19950.8243
0.0000
0.9713
0.0000
1.0000
0.0000
20540.6292
1.0000
K VALUE
64 65
296312.9955
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
0.0000
0.0000
---
67
H2O
0.0000
0.0000
---
68
Oxygen
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 294 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: AMINA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
0.0000
0.0000
---
---
---
---
14
Hydrogen
0.0000
0.0000
---
15
Ethane
0.0000
0.0000
---
16
Propane
---
---
---
17
CO2
0.0000
0.0000
---
18
Nitrogen
0.0000
0.0000
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
0.0000
0.0000
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Valve:
VLV-104 Distillation:
LOGICAL CONNECTION T-102
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
190.0 psia 5020 lbmole/hrMass:
37
3.033e+005 lb/hrStd Ideal Liq Volume: 2.054e+004 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: Anmonia
46 47 48
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
132.8
132.8
(psia)
114.7
114.7
(lbmole/hr) (lb/hr)
(Btu/hr)
1087 1.946e+004 1430 -1.112e+005 15.61 -1.209e+008 1399*
(barrel/day)
61
1087 1.946e+004 1430 -1.112e+005 15.61 -1.209e+008 1399
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
Aqueous Phase 17.90
17.90
3.205
3.205
57.36
57.36
(barrel/day)
1450
1450
(Btu/lb)
-6213
-6213
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 295 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Anmonia (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Aqueous Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
1.642e+004
1.642e+004
16
HHV Molar Basis (Std)
(Btu/lbmole)
3.511e+004
3.511e+004
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
(lbmole/ft3)
8.102e-005
8.102e-005
20
CO2 App WT Con
(lbmol/lb)
1.412e-006
1.412e-006
21
LHV Mass Basis (Std)
22
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
0.8721
0.8721
18.90
18.90
1.056
1.056
1962
1962
581.5
581.5
917.3
917.3
Phase Fraction [Vol. Basis]
0.0000
1.000
23
Phase Fraction [Mass Basis]
0.0000
1.000
24
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
25
Mass Exergy
(Btu/lb)
3.225
---
26
Partial Pressure of CO2
(psia)
0.0000
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
(psia)
59
True VP at 37.8 C
(psia)
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
3.250
3.250
Specific Heat
(Btu/lbmole-F)
18.90
18.90
Std. Gas Flow
(MMSCFD)
9.883
9.883
(lb/ft3)
58.17
58.17
(USGPS)
0.7049
0.7049
5.628e-003
(psia)
(Btu/lbmole)
5.628e-003
12.24
12.24
---
---
0.0000
---
1.117
1.117
1.187
1.187
1.732e+004
---
(cSt)
0.4624
0.4624
(lb/ft3)
59.44
59.44
(barrel/day)
1399
1399
1.000
1.000
(ft3/lbmole)
0.3120
0.3120
(Btu/lb)
967.9
---
0.0000
1.0000
(dyne/cm)
60.88
60.88
(Btu/hr-ft-F)
0.3561
0.3561
0.4249
0.4249
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.91
16.91
0.9451
0.9451
15.92
15.92
0.8895
0.8895
15.87
15.87
0.8870
0.8870
1.191
1.191
211.7
211.7
128.5
128.5
1399
1399
-10.20
---
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0002
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
0.0000
LIQUID VOLUME FRACTION 0.0000
Page 296 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Anmonia (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
0.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
H2O
956.1739
0.8794
0.8852
1181.8636
0.8264
16
Oxygen
0.0114
0.0000
0.3640
0.0000
0.0219
0.0000
17
Methane
0.0001
0.0000
0.0012
0.0000
0.0003
0.0000
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0117
0.0000
0.0236
0.0000
0.0231
0.0000
20
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.0275
0.0000
1.2095
0.0001
0.1003
0.0001
23
Nitrogen
0.0199
0.0000
0.5585
0.0000
0.0474
0.0000
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0029
0.0000
0.0002
0.0000
27
Ammonia
131.0322
0.1205
2231.4778
0.1147
248.0166
0.1734
28
Total
1087.2767
1.0000
19459.2060
1.0000
1430.0736
1.0000
29
17225.5682
Aqueous Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
33
CO
0.0000
0.0000
34
H2O
956.1739
0.8794
35
Oxygen
0.0114
0.0000
36
Methane
0.0001
37
H2S
38
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
0.0002
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8852
1181.8636
0.8264
0.3640
0.0000
0.0219
0.0000
0.0000
0.0012
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0117
0.0000
0.0236
0.0000
0.0231
0.0000
39
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0275
0.0000
1.2095
0.0001
0.1003
0.0001
42
Nitrogen
0.0199
0.0000
0.5585
0.0000
0.0474
0.0000
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0029
0.0000
0.0002
0.0000
46
Ammonia
131.0322
0.1205
2231.4778
0.1147
248.0166
0.1734
47
Total
1087.2767
1.0000
19459.2060
1.0000
1430.0736
1.0000
17225.5682
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
0.0000
---
0.0000
52
H2O
0.0000
---
0.0000
53
Oxygen
0.0000
---
0.0000
54
Methane
0.0000
---
0.0000
---
---
---
Hydrogen
0.0000
---
0.0000
57
Ethane
0.0000
---
0.0000
58
Propane
---
---
---
59
CO2
0.0000
---
0.0000
60
Nitrogen
0.0000
---
0.0000
---
---
---
55
H2S
56
61
Air
62
Mercury
---
---
---
63
MEAmine
0.0000
---
0.0000
64
Ammonia
0.0000
---
0.0000
65
UNIT OPERATIONS
66 67 68 69
FEED TO Pump:
Aspen Technology Inc. Licensed to: LEGENDS
PRODUCT FROM P-101
Absorber:
LOGICAL CONNECTION T-101
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 297 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Anmonia (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Inactive):
18
Flow Specification
(Inactive) Molar:
114.7 psia 1087 lbmole/hrMass:
19
1.946e+004 lb/hrStd Ideal Liq Volume:
1430 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: CONDENSADO #1
28 29 30
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
Aqueous Phase
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
1.823e+005
1.823e+005
39
Molar Enthalpy
(Btu/lbmole)
-1.225e+005
-1.225e+005
40
Molar Entropy
(Btu/lbmole-F)
41
Heat Flow
42
Liq Vol Flow @Std Cond
0.0000
1.0000
(F)
110.1*
110.1
(psia)
274.7*
(lbmole/hr) (lb/hr)
274.7
1.473e+005
1.473e+005
* 2.656e+006
2.656e+006
13.95
13.95
(Btu/hr)
-1.804e+010
-1.804e+010
(barrel/day)
* 1.792e+005
1.792e+005
43
PROPERTIES
44 45
Overall
Aqueous Phase
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Mass Enthalpy
(Btu/lb)
-6790
-6790
51
Mass Entropy
(Btu/lb-F)
0.7736
0.7736
52
Heat Capacity
53
Mass Heat Capacity
54
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F)
18.03
18.03
3.442
3.442
62.06 1.830e+005
62.06 1.830e+005
18.57
18.57
(Btu/lb-F)
1.030
1.030
LHV Molar Basis (Std)
(Btu/lbmole)
1.868
55
HHV Molar Basis (Std)
(Btu/lbmole)
56
HHV Mass Basis (Std)
57
CO2 Loading
58
CO2 App ML Con
(lbmole/ft3)
2.424e-003
2.424e-003
59
CO2 App WT Con
(lbmol/lb)
3.906e-005
3.906e-005
60
LHV Mass Basis (Std)
61
(Btu/lb)
1.762e+004 977.1 ---
977.1 ---
0.1036
Phase Fraction [Vol. Basis]
0.0000
1.000
62
Phase Fraction [Mass Basis]
0.0000
1.000
63
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
64
Mass Exergy
(Btu/lb)
1.943
---
65
Partial Pressure of CO2
(psia)
0.0000
---
66
Cost Based on Flow
(Cost/s)
0.0000
0.0000
67
Act. Gas Flow
68
Avg. Liq. Density
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
1.868 1.762e+004
0.1036
69
Fluid Package:
(ACFM)
---
---
(lbmole/ft3)
3.453
3.453
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 298 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: CONDENSADO #1 (continued)Property Package:
7 8 9
Basis-1 Peng-Robinson
PROPERTIES
10 11
Overall
Aqueous Phase
12
Specific Heat
(Btu/lbmole-F)
18.57
13
Std. Gas Flow
(MMSCFD)
1339
1339
14
Std. Ideal Liq. Mass Density
62.28
62.28
15
Act. Liq. Flow
16
Z Factor
17
Watson K
18
User Property
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
(psia)
---
---
41
True VP at 37.8 C
(psia)
238.9
238.9
42
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
43
Viscosity Index
(lb/ft3) (USGPS)
88.94 1.305e-002
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
8.489
---
---
0.0000
---
1.120
1.120
1.157
1.157
1.591e+004 63.37
(ft3/lbmole) (Btu/lb)
88.94 1.305e-002
8.489
0.6154
(barrel/day)
18.57
1.792e+005
--0.6154 63.37 1.792e+005
1.000
1.000
0.2906
0.2906
882.5
---
0.0000
1.0000
(dyne/cm)
68.85
68.85
(Btu/hr-ft-F)
0.3673
0.3673
0.6118
0.6118
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.58
16.58
0.9194
0.9194
16.05
16.05
0.8898
0.8898
15.84
15.84
0.8784
0.8784
1.172
1.172
1.792e+005 -4.393
44
1.792e+005 ---
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr) * 0.1396
MOLE FRACTION
H2O
52
Oxygen
* 0.2240
* 0.0000
* 7.1691
* 0.0000
* 0.4315
* 0.0000
53
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
54
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
55
Hydrogen
* 2.4818
* 0.0000
* 5.0032
* 0.0000
* 4.9040
* 0.0000
56
Ethane
* 0.0000
* 0.0000
* 0.0004
* 0.0000
* 0.0001
* 0.0000
57
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
58
CO2
* 103.7602
* 0.0007
* 4566.4535
* 0.0017
* 378.8498
* 0.0021
59
Nitrogen
* 4.9861
* 0.0000
* 139.6763
* 0.0001
* 11.8605
* 0.0001
60
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
61
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
62
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
63
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
64
Total
147299.3457
1.0000
2.656324390e+06
* 0.9982
1.0000
* 0.3349
LIQUID VOLUME FRACTION
CO
* 2.651602178e+06
* 0.0000
LIQUID VOLUME FLOW (barrel/day)
51
* 0.9992
* 3.9096
MASS FRACTION
0.0000
50
* 147187.7540
* 0.0000
MASS FLOW (lb/hr)
Vapour Fraction
* 181929.1050
182325.4857
* 0.0000 * 0.9978
1.0000
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 299 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: CONDENSADO #1 (continued)Property Package:
7 8 9
Basis-1 Peng-Robinson
COMPOSITION
10 11
Aqueous Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
16
H2O
17
Oxygen
0.2240
0.0000
7.1691
0.0000
0.4315
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
2.4818
0.0000
5.0032
0.0000
4.9040
0.0000
21
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
103.7602
0.0007
4566.4535
0.0017
378.8498
0.0021
24
Nitrogen
4.9861
0.0000
139.6763
0.0001
11.8605
0.0001
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.1396
0.0000
147187.7540
3.9096
0.9992
147299.3457
0.0000
2.651602178e+06
1.0000
2.656324390e+06
30
0.3349
0.9982
0.0000
181929.1050
1.0000
0.9978
182325.4857
1.0000
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
0.0000
---
0.0000
34
H2O
0.0000
---
0.0000
35
Oxygen
0.0000
---
0.0000
36
Methane
---
---
---
---
---
---
Hydrogen
0.0000
---
0.0000
39
Ethane
0.0000
---
0.0000
40
Propane
---
---
---
41
CO2
0.0000
---
0.0000
42
Nitrogen
0.0000
---
0.0000
---
---
---
37
H2S
38
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO Conversion Reactor:
PRODUCT FROM
H-1 REFORMADOR SECUNDARIO Recycle:
51
LOGICAL CONNECTION RCY-1
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Inactive) Molar:
61
* 274.7 psia
1.473e+005 lbmole/hr Mass:
2.656e+006 *lb/hrStd Ideal Liq Volume: 1.823e+005 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 300 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: DESTILATE WATER
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
213.2*
213.2
(psia)
214.7*
214.7
1059*
(lbmole/hr) (lb/hr)
(Btu/hr)
1.909e+004 1310 -1.205e+005 17.04 -1.277e+008 1288*
(barrel/day)
22
1059 1.909e+004 1310 -1.205e+005 17.04 -1.277e+008 1288
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
30
Mass Entropy
31
Heat Capacity
32
Mass Heat Capacity
33
(lbmole/ft3) (lb/ft3)
Aqueous Phase 18.02
18.02
3.285
3.285
59.18
59.18
(barrel/day)
1379
1379
(Btu/lb)
-6689
-6689
(Btu/lb-F)
0.9461
0.9461
18.91
18.91
(Btu/lbmole-F) (Btu/lb-F)
1.050
1.050
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
34
HHV Molar Basis (Std)
(Btu/lbmole)
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
16.11
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
---
---
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
18.91
18.91
Std. Gas Flow
(MMSCFD)
9.631
9.631
Licensed to: LEGENDS
(lb/ft3)
62.30
62.30
(USGPS)
0.6702
0.6702
9.051e-003
(psia)
(Btu/lbmole)
9.051e-003
0.0000
---
1.117
1.117
1.175
1.175
1.529e+004
---
(cSt)
0.2922
0.2922
(lb/ft3)
63.35
63.35
(barrel/day)
1288
1288
1.000
1.000
(ft3/lbmole)
0.3044
0.3044
(Btu/lb)
849.0
---
0.0000
1.0000
(dyne/cm)
58.48
58.48
(Btu/hr-ft-F)
0.3935
0.3935
0.2770
0.2770
(cP)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 301 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: DESTILATE WATER (continued) Property Package:
7 8 9
Basis-1 Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Aqueous Phase 16.93
16.93
0.9397
0.9397
16.10
16.10
0.8936
0.8936
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
1288
1288
-24.32
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr) * 0.0000
MOLE FRACTION
MASS FLOW (lb/hr)
LIQUID VOLUME FLOW (barrel/day)
CO H2O
31
Oxygen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
32
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
33
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
34
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
35
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
36
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
37
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
38
Nitrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
39
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
40
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
41
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
42
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
43
Total
* 1.0000
* 19086.7724
1.0000
44
19086.7724
* 0.0000
LIQUID VOLUME FRACTION
30
1059.4874
* 0.0000
MASS FRACTION
0.0000
29
* 1059.4874
* 0.0000
Vapour Fraction
* 0.0000
* 1.0000
1.0000
46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
48
CO
0.0000
0.0000
49
H2O
1059.4874
1.0000
50
Oxygen
0.0000
0.0000
51
Methane
0.0000
52
H2S
53
MASS FLOW (lb/hr)
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1309.5627
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
1059.4874
1.0000
1.0000
1309.5627
1.0000
63
19086.7724
19086.7724
K VALUE
64 65
0.0000
* 1.0000
1309.5627
Aqueous Phase
45
* 0.0000
* 1309.5627
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
0.0000
---
0.0000
---
---
68 69
Oxygen
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 302 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: DESTILATE WATER (continued) Property Package:
7 8 9
Basis-1 Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Absorber:
LOGICAL CONNECTION
T-101
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Active)
* 214.7 psia * Mass: 1059 lbmole/hr
Molar:
37
1.909e+004 lb/hrStd Ideal Liq Volume:
1310 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: Entrada de Vapor
46 47 48
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
274.9
274.9
(psia)
364.7*
364.7
(lbmole/hr) (lb/hr)
(Btu/hr)
1918 * 3.456e+004
2371 -1.193e+005 18.72 -2.289e+008 2332*
(barrel/day)
61
1918 3.456e+004 2371 -1.193e+005 18.72 -2.289e+008 2332
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
Aqueous Phase 18.02
18.02
3.184
3.184
57.35
57.35
(barrel/day)
2576
2576
(Btu/lb)
-6623
-6623
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 303 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: Entrada de Vapor (continued)Property Package:
7 8 9
Basis-1 Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
(Btu/lb-F) (Btu/lbmole-F)
Aqueous Phase 1.039
1.039
19.36
19.36
(Btu/lb-F)
1.074
1.074
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
16
HHV Molar Basis (Std)
(Btu/lbmole)
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
23
Phase Fraction [Mass Basis]
0.0000
1.000
24
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
25
Mass Exergy
(Btu/lb)
32.15
---
26
Partial Pressure of CO2
(psia)
0.0000
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
---
---
36
User Property
---
---
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.36
19.36
Std. Gas Flow
(MMSCFD)
17.44
17.44
(lb/ft3)
62.30
62.30
(USGPS)
1.252 1.453e-002
(psia)
(Btu/lbmole)
1.252 1.453e-002
0.0000
---
1.114
1.114
1.182
1.182
1.445e+004
---
(cSt)
0.2207
0.2207
(lb/ft3)
63.35
63.35
(barrel/day)
2332
2332
1.000
1.000
(ft3/lbmole)
0.3141
0.3141
(Btu/lb)
802.3
---
0.0000
1.0000
(dyne/cm)
51.76
51.76
(Btu/hr-ft-F)
0.3975
0.3975
0.2027
0.2027
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
17.37
17.37
0.9642
0.9642
16.37
16.37
0.9089
0.9089
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
2332
2332
-45.55
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) * 0.0000
MOLE FRACTION * 0.0000
MASS FLOW (lb/hr) * 0.0000
Vapour Fraction MASS FRACTION * 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) * 0.0000
0.0000
LIQUID VOLUME FRACTION * 0.0000
Page 304 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: Entrada de Vapor (continued)Property Package:
7 8 9
Basis-1 Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr) * 1918.3906
MOLE FRACTION
MASS FLOW (lb/hr) * 34560.0000
MASS FRACTION
0.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
* 2371.1965
* 1.0000
15
H2O
16
Oxygen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
17
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
18
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
19
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
20
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
21
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
22
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
23
Nitrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
24
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
25
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
26
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
27
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
28
Total
1918.3906
* 1.0000
Vapour Fraction
1.0000
29
34560.0000
* 1.0000
1.0000
2371.1965
Aqueous Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
33
CO
0.0000
0.0000
34
H2O
1918.3906
1.0000
35
Oxygen
0.0000
0.0000
36
Methane
0.0000
37
H2S
38
MASS FLOW (lb/hr) 0.0000
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2371.1965
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
1918.3906
1.0000
1.0000
2371.1965
1.0000
34560.0000
34560.0000
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
---
---
---
52
H2O
0.0000
---
0.0000
53
Oxygen
---
---
---
54
Methane
---
---
---
---
---
---
55
H2S
56
Hydrogen
---
---
---
57
Ethane
---
---
---
58
Propane
---
---
---
59
CO2
---
---
---
60
Nitrogen
---
---
---
---
---
---
61
Air
62
Mercury
---
---
---
63
MEAmine
---
---
---
64
Ammonia
---
---
---
65
UNIT OPERATIONS
66 67 68 69
FEED TO LNG:
Aspen Technology Inc. Licensed to: LEGENDS
PRODUCT FROM
LOGICAL CONNECTION
LNG-101
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 305 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: Entrada de Vapor (continued)Property Package:
7 8 9
Basis-1 Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Active):
18
Flow Specification
(Active)
* 364.7 psia
Molar:
1918 lbmole/hrMass:
19
2371 barrel/day
User Variables
20 21
NOTES
22 23
3.456e+004 *lb/hrStd Ideal Liq Volume:
29285
24 25
(Last modified Tue Dec 11, 2018, 17:29)
26 27
Description
28 29 30
Material Stream: FEED GAS
31 32 33
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
34 35
Overall
36
Vapour / Phase Fraction
37
Temperature:
38
Pressure:
39
Molar Flow
40
Mass Flow
41
Std Ideal Liq Vol Flow
(barrel/day)
42
Molar Enthalpy
(Btu/lbmole)
43
Molar Entropy
(Btu/lbmole-F)
44
Heat Flow
45
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
60.00*
60.00
(psia)
414.7*
414.7
792.2*
(lbmole/hr) (lb/hr)
1.374e+004 3013 -3.254e+004 37.34
792.2 1.374e+004 3013 -3.254e+004 37.34
(Btu/hr)
-2.578e+007
-2.578e+007
(barrel/day)
* 1.279e+006
1.279e+006
46
PROPERTIES
47 48
Overall
Vapour Phase
49
Molecular Weight
50
Molar Density
51
Mass Density
52
Act. Volume Flow
53
Mass Enthalpy
(Btu/lb)
-1876
-1876
54
Mass Entropy
(Btu/lb-F)
2.153
2.153
55
Heat Capacity
56
Mass Heat Capacity
57
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
58
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
59
HHV Mass Basis (Std)
2.274e+004
2.274e+004
60
CO2 Loading
61
CO2 App ML Con
62
CO2 App WT Con
63
LHV Mass Basis (Std)
64
Phase Fraction [Vol. Basis]
1.000
1.000
65
Phase Fraction [Mass Basis]
1.000
1.000
66
Phase Fraction [Act. Vol. Basis]
1.000
1.000
67
Mass Exergy
(Btu/lb)
201.3
---
68
Partial Pressure of CO2
(psia)
0.5811
---
69
Aspen Technology Inc. Licensed to: LEGENDS
17.34 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
8.051e-002 1.396 4.207e+004
17.34 8.051e-002 1.396 4.207e+004
9.668
9.668
0.5575
0.5575
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 306 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: FEED GAS (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Cost Based on Flow
(Cost/s)
6445
6445
13
Act. Gas Flow
(ACFM)
164.0
164.0
14
Avg. Liq. Density
(lbmole/ft3)
1.124
1.124
15
Specific Heat
(Btu/lbmole-F)
9.668
9.668
16
Std. Gas Flow
(MMSCFD)
7.201
7.201
17
Std. Ideal Liq. Mass Density
(lb/ft3)
19.49
19.49
18
Act. Liq. Flow
(USGPS)
---
---
19
Z Factor
0.9237
0.9237
20
Watson K
19.04
19.04
21
User Property
---
---
22
Partial Pressure of H2S
23
Cp/(Cp - R)
24
Cp/Cv
25
Heat of Vap.
26
Kinematic Viscosity
27
Liq. Mass Density (Std. Cond)
28
Liq. Vol. Flow (Std. Cond)
29
Liquid Fraction
30
Molar Volume
31
Mass Heat of Vap.
32
Phase Fraction [Molar Basis]
33
Surface Tension
34
Thermal Conductivity
35
Viscosity
36
Cv (Semi-Ideal)
37
Mass Cv (Semi-Ideal)
38
Cv
39
Mass Cv
40
Cv (Ent. Method)
41
Mass Cv (Ent. Method)
42
Cp/Cv (Ent. Method)
43
Reid VP at 37.8 C
44
True VP at 37.8 C
45
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
46
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.258
1.258
1.406
1.406
2673
---
0.5163
0.5163
4.592e-002
4.592e-002
1.279e+006
1.279e+006
0.0000
0.0000
(ft3/lbmole)
12.42
12.42
(Btu/lb)
154.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.944e-002
1.944e-002
1.155e-002
1.155e-002
7.682
7.682
0.4430
0.4430
6.876
6.876
0.3965
0.3965
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.279e+006 -38.94
47
1.279e+006 ---
COMPOSITION
48 49
Overall Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
53
CO
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
54
H2O
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
55
Oxygen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
56
Methane
* 717.8618
* 0.9061
57
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
58
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
59
Ethane
* 58.9958
* 0.0745
* 0.1291
* 341.5139
* 0.1133
60
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
61
CO2
* 1.1101
* 0.0014
* 48.8568
* 0.0036
* 4.0533
* 0.0013
62
Nitrogen
* 14.2732
* 0.0180
* 399.8347
* 0.0291
* 33.9518
* 0.0113
63
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
64
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
65
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
66
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
67
Total
792.2409
1.0000
* 11516.5851
* 1773.9985
13739.2751
* 0.8382
1.0000
* 2633.8976
3013.4166
* 0.8741
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 307 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: FEED GAS (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
717.8618
0.9061
0.8382
2633.8976
0.8741
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
58.9958
0.0745
1773.9985
0.1291
341.5139
0.1133
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
1.1101
0.0014
48.8568
0.0036
4.0533
0.0013
24
Nitrogen
14.2732
0.0180
399.8347
0.0291
33.9518
0.0113
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
792.2409
1.0000
1.0000
3013.4166
1.0000
11516.5851
13739.2751
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Tee:
LOGICAL CONNECTION
TEE-101
51
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Active):
60
Flow Specification
(Active)
* 414.7 psia
Molar:
61
1.374e+004 lb/hrStd Ideal Liq Volume:
3013 barrel/day
User Variables
62 63
NOTES
64 65
* Mass: 792.2 lbmole/hr
29285
66 67 68 69
(Last modified Tue Dec 11, 2018, 17:24)
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 308 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: FEED GAS (continued)
7 8
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
9 10
Description
11 12 13
Material Stream: gas Acido
14 15 16
CONDITIONS
17 18
Overall
19
Vapour / Phase Fraction
20
Temperature:
21
Pressure:
22
Molar Flow
23
Mass Flow
24
Std Ideal Liq Vol Flow
25
Molar Enthalpy
(Btu/lbmole)
26
Molar Entropy
(Btu/lbmole-F)
27
Heat Flow
28
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
Liquid Phase
0.0384
0.0384
0.3974
0.5642
(F)
-341.2
-341.2
-341.2
-341.2
(psia)
170.0
170.0
170.0
170.0
198.2
7.606
78.79
111.9
7099
17.67
2171
4910
633.0
15.07
210.5
407.4
(lbmole/hr) (lb/hr) (barrel/day)
-1.206e+005 2.718
-3274 14.33
-4.573e+004 9.465
(Btu/hr)
-2.391e+007
-2.490e+004
-3.603e+006
(barrel/day)
* 3.199e+005
1.232e+004
1.274e+005
29
-1.813e+005 -2.824 -2.028e+007 7119
PROPERTIES
30 31
Overall
32
Molecular Weight
33
Molar Density
34
Mass Density
35
Act. Volume Flow
36
Vapour Phase
Liquid Phase
Liquid Phase
35.81
2.324
27.55
43.90
1.370
0.1433
1.898
2.234
49.07
0.3329
52.31
98.06
(barrel/day)
618.4
226.9
177.4
214.1
Mass Enthalpy
(Btu/lb)
-3367
-1409
-1660
37
Mass Entropy
(Btu/lb-F)
6.167
0.3435
38
Heat Capacity
39
Mass Heat Capacity
40
LHV Molar Basis (Std)
(Btu/lbmole)
6.420e+004
1.038e+005
1.504e+005
773.4
41
HHV Molar Basis (Std)
(Btu/lbmole)
6.709e+004
1.213e+005
1.560e+005
774.6
42
HHV Mass Basis (Std)
43
CO2 Loading
44
CO2 App ML Con
45
CO2 App WT Con
46
LHV Mass Basis (Std)
4.469e+004
5459
17.62
47
Phase Fraction [Vol. Basis]
2.380e-002
2.380e-002
0.3325
0.6437
48
Phase Fraction [Mass Basis]
2.489e-003
2.489e-003
49
Phase Fraction [Act. Vol. Basis]
50
Mass Exergy
51
Partial Pressure of CO2
52
Cost Based on Flow
53
Act. Gas Flow
54
Avg. Liq. Density
55 56 57
Std. Ideal Liq. Mass Density
58
Act. Liq. Flow
59
Z Factor
60
Watson K
61
User Property
62
Partial Pressure of H2S
63
Cp/(Cp - R)
64
Cp/Cv
65
Heat of Vap.
66
Kinematic Viscosity
67
Liq. Mass Density (Std. Cond)
68
Liq. Vol. Flow (Std. Cond)
69
Aspen Technology Inc.
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
7.590e-002 15.59
7.310
13.02
17.96
0.4354
3.146
0.4724
0.4092
1874
5.219e+004
5662
---
---
2.463e+039
(lbmole/ft3)
---
---
5.194e-003
(lbmol/lb)
---
---
9.929e-005
(Btu/lb)
(Btu/lb) (psia)
-4129 -6.433e-002
1793
17.64 1.071e+028 2.218 2.262e-002
0.3058
0.6917
0.3670
0.3670
0.2869
0.3461
314.0
---
---
---
---
---
---
0.0000
0.0000
1.189e-009
(Cost/s)
0.0000
0.0000
(ACFM)
0.8849
0.8849
---
---
(lbmole/ft3)
1.339
2.158
1.600
1.173
Specific Heat
(Btu/lbmole-F)
15.59
13.02
17.96
Std. Gas Flow
(MMSCFD)
1.802
0.7162
1.017
Licensed to: LEGENDS
7.310 6.914e-002
(lb/ft3)
47.94
5.014
(USGPS)
0.1903
---
8.624e-002 7.046e-002
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
44.09
51.52 0.1041
---
0.9337
8.360
41.81
7.782
5.989e-002 8.514
---
---
---
---
0.0000
---
---
---
1.146
1.373
1.180
1.124
1.008
1.525
1.629
1.000
9149
---
---
---
---
0.5273
0.4493
54.44
9.486e-002
6.133e-003
7.282e-002
2.948
3.199e+005
1.232e+004
1.274e+005
7119
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 309 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: gas Acido (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Liquid Fraction
13
Molar Volume
14
Mass Heat of Vap.
15
Phase Fraction [Molar Basis]
16
Surface Tension
17
Thermal Conductivity
18
Viscosity
19
Cv (Semi-Ideal)
20
Mass Cv (Semi-Ideal)
21
Cv
22
Mass Cv
23
Cv (Ent. Method)
24
Mass Cv (Ent. Method)
25
Cp/Cv (Ent. Method)
26
Reid VP at 37.8 C
27
True VP at 37.8 C
28
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
29
Viscosity Index
(ft3/lbmole) (Btu/lb)
Vapour Phase
Liquid Phase
Liquid Phase
0.9616
0.0000
1.000
1.000
0.7297
6.980
0.5267
0.4477
255.5
---
---
---
0.0384
0.0384
0.3974
0.5642
(dyne/cm)
---
14.31
58.41
(Btu/hr-ft-F)
---
3.033e-002
0.1377
0.1467
---
2.812e-003
(cP)
---
0.3765
85.51
13.60
5.324
11.03
---
0.3799
2.291
0.4004
---
15.46
4.794
7.992
---
0.4318
2.063
0.2901
---
---
---
9.018
---
---
---
0.3273
---
---
---
1.444
---
(psia)
---
---
---
---
(psia)
---
---
---
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
1.397e+005 19.01
30
1.232e+004 ---
1.274e+005 ---
--0.0000 ---
COMPOSITION
31 32
Overall Phase
33 34
COMPONENTS
35
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
0.0384
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
36
CO
58.6846
0.2960
1643.8092
0.2316
140.8030
0.2224
37
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Oxygen
4.1926
0.0211
134.1640
0.0189
8.0748
0.0128
39
Methane
3.6586
0.0185
58.6943
0.0083
13.4237
0.0212
40
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Hydrogen
8.4386
0.0426
17.0122
0.0024
16.6746
0.0263
42
Ethane
5.6111
0.0283
168.7244
0.0238
32.4813
0.0513
43
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
CO2
111.3102
0.5615
4898.7266
0.6901
406.4164
0.6421
45
Nitrogen
6.3500
0.0320
177.8812
0.0251
15.1047
0.0239
46
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Total
198.2456
1.0000
7099.0117
1.0000
632.9785
1.0000
51
Vapour Phase
52 53
COMPONENTS
54
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
3.837e-002 LIQUID VOLUME FRACTION
55
CO
0.0655
0.0086
1.8346
0.1038
0.1571
0.0104
56
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Oxygen
0.0017
0.0002
0.0551
0.0031
0.0033
0.0002
58
Methane
0.0001
0.0000
0.0017
0.0001
0.0004
0.0000
59
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Hydrogen
7.5159
0.9882
15.1521
0.8574
14.8514
0.9858
61
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Nitrogen
0.0225
0.0030
0.6293
0.0356
0.0534
0.0035
65
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 310 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: gas Acido (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
Fluid Package:
Total
7.6057
1.0000
14
17.6726
Phase Fraction 1.0000
15.0657
Liquid Phase
15 16
COMPONENTS
17
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
3.837e-002 1.0000
Phase Fraction MASS FRACTION
0.3974
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
18
CO
57.9190
0.7351
1622.3628
0.7473
138.9660
0.6603
19
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Oxygen
4.1729
0.0530
133.5337
0.0615
8.0369
0.0382
21
Methane
3.6555
0.0464
58.6448
0.0270
13.4123
0.0637
22
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Hydrogen
0.9226
0.0117
1.8599
0.0009
1.8230
0.0087
24
Ethane
5.6106
0.0712
168.7105
0.0777
32.4786
0.1543
25
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
CO2
0.2156
0.0027
9.4864
0.0044
0.7870
0.0037
27
Nitrogen
6.2916
0.0799
176.2452
0.0812
14.9658
0.0711
28
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Total
78.7877
1.0000
2170.8433
1.0000
210.4697
1.0000
33
Liquid Phase
34 35
COMPONENTS
36
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.5642 LIQUID VOLUME FRACTION
37
CO
0.7001
0.0063
19.6118
0.0040
1.6799
0.0041
38
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Oxygen
0.0180
0.0002
0.5752
0.0001
0.0346
0.0001
40
Methane
0.0030
0.0000
0.0478
0.0000
0.0109
0.0000
41
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Hydrogen
0.0001
0.0000
0.0002
0.0000
0.0002
0.0000
43
Ethane
0.0005
0.0000
0.0138
0.0000
0.0027
0.0000
44
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
CO2
111.0946
0.9932
4889.2402
0.9957
405.6294
0.9955
46
Nitrogen
0.0359
0.0003
1.0067
0.0002
0.0855
0.0002
47
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Total
111.8522
1.0000
4910.4957
1.0000
407.4431
1.0000
52
K VALUE
53 54
COMPONENTS
MIXED
LIGHT
HEAVY
55
CO
2.801e-002
56
H2O
2.612e-042
57
Oxygen
1.029e-002
4.271e-003
1.407
58
Methane
7.205e-004
2.980e-004
0.5190
59
H2S
60
Hydrogen
1.171e-002 ---
---
---
204.2
84.39
61
Ethane
62
Propane
63
CO2
1.198e-011
2.556e-009
64
Nitrogen
8.898e-002
3.699e-002
65
Air
66
Mercury
67
MEAmine
68 69
Ammonia
Aspen Technology Inc. Licensed to: LEGENDS
1.218e-008 ---
5.034e-009 ---
---
---
---
---
2.084e-053 ---
Aspen HYSYS Version 8.8 (34.0.0.8909)
-----
1.376 1.533e-042
--1.229e+006 8.711e-005 --7.040e-012 9.192 ----1.223e-053 ---
Page 311 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: gas Acido (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Distillation:
LOGICAL CONNECTION T-102
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
170.0 psia 198.2 lbmole/hrMass:
23
7099 lb/hr Std Ideal Liq Volume:
633.0 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: GAS COMBUSTIBLE
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
60.00
60.00
(psia)
414.7
414.7
351.6
351.6
6097
6097
(lbmole/hr) (lb/hr)
1337 -3.254e+004 37.34
1337 -3.254e+004 37.34
(Btu/hr)
-1.144e+007
-1.144e+007
(barrel/day)
* 5.676e+005
5.676e+005
47
PROPERTIES
48 49
Overall
Vapour Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-1876
-1876
55
Mass Entropy
(Btu/lb-F)
2.153
2.153
56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
60
HHV Mass Basis (Std)
2.274e+004
2.274e+004
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
Phase Fraction [Vol. Basis]
1.000
1.000
66
Phase Fraction [Mass Basis]
1.000
1.000
67
Phase Fraction [Act. Vol. Basis]
1.000
1.000
68
Mass Exergy
201.3
---
69
Aspen Technology Inc. Licensed to: LEGENDS
17.34 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
8.051e-002 1.396 1.867e+004
17.34 8.051e-002 1.396 1.867e+004
9.668
9.668
0.5575
0.5575
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
(Btu/lb)
---
2.067e+004
2.067e+004
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 312 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: GAS COMBUSTIBLE (continued) Property Package:
7 8 9
Basis-1 Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Vapour Phase
(psia)
0.5811
---
(Cost/s)
0.0000
0.0000
(ACFM)
72.78
72.78
(lbmole/ft3)
1.124
1.124
Specific Heat
(Btu/lbmole-F)
9.668
9.668
17
Std. Gas Flow
(MMSCFD)
3.196
3.196
18
Std. Ideal Liq. Mass Density
(lb/ft3)
19.49
19.49
19
Act. Liq. Flow
(USGPS)
---
---
20
Z Factor
0.9237
0.9237
21
Watson K
19.04
19.04
22
User Property
---
---
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.258
1.258
1.406
1.406
2673
---
0.5163
0.5163
4.592e-002
4.592e-002
5.676e+005
5.676e+005
0.0000
0.0000
(ft3/lbmole)
12.42
12.42
(Btu/lb)
154.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.944e-002
1.944e-002
1.155e-002
1.155e-002
7.682
7.682
0.4430
0.4430
6.876
6.876
0.3965
0.3965
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
5.676e+005 -38.94
48
5.676e+005 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Methane
318.5575
0.9061
5110.5864
0.8382
1168.8153
0.8741
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Ethane
26.1799
0.0745
787.2275
0.1291
151.5498
0.1133
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.4926
0.0014
21.6806
0.0036
1.7987
0.0013
63
Nitrogen
6.3339
0.0180
177.4302
0.0291
15.0664
0.0113
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
351.5639
1.0000
6096.9247
1.0000
1337.2302
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 313 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: GAS COMBUSTIBLE (continued) Property Package:
7 8 9
Basis-1 Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
318.5575
0.9061
5110.5864
0.8382
1168.8153
0.8741
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
26.1799
0.0745
787.2275
0.1291
151.5498
0.1133
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.4926
0.0014
21.6806
0.0036
1.7987
0.0013
24
Nitrogen
6.3339
0.0180
177.4302
0.0291
15.0664
0.0113
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
351.5639
1.0000
6096.9247
1.0000
1337.2302
1.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49
FEED TO
PRODUCT FROM
50
Tee:
51
LOGICAL CONNECTION TEE-101
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Inactive) Molar:
61
414.7 psia 351.6 lbmole/hrMass:
6097 lb/hr Std Ideal Liq Volume:
1337 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 314 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
60.00*
60.00
(psia)
414.7*
414.7
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
0.0000 -3.254e+004
0.0000 -3.254e+004
37.34
37.34
(Btu/hr)
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29 30 31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
35
HHV Mass Basis (Std)
2.274e+004
2.274e+004
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
1.000
1.000
41
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
---
---
43
Mass Exergy
(Btu/lb)
201.3
---
44
Partial Pressure of CO2
(psia)
0.5811
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
0.0000
47
Avg. Liq. Density
48
17.34 (lbmole/ft3) (lb/ft3)
8.051e-002
17.34 8.051e-002
1.396
1.396
(barrel/day)
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-1876
-1876
Mass Entropy
(Btu/lb-F)
2.153
2.153
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
9.668
9.668
0.5575
0.5575
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
(ACFM)
0.0000
(lbmole/ft3)
---
---
Specific Heat
(Btu/lbmole-F)
9.668
9.668
49
Std. Gas Flow
(MMSCFD)
50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
0.0000
0.0000
(lb/ft3)
19.49
19.49
(USGPS)
---
---
0.9237
0.9237
19.04
19.04
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.258
1.258
1.406
1.406
2673
---
0.5163
0.5163
4.592e-002
4.592e-002
0.0000
0.0000
0.0000
0.0000
(ft3/lbmole)
12.42
12.42
(Btu/lb)
154.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
1.944e-002
1.944e-002
1.155e-002
1.155e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 315 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21 22
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 7.682
7.682
0.4430
0.4430
6.876
6.876
0.3965
0.3965
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
Viscosity Index
-38.94
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
0.0000
0.9061
0.0000
0.8382
0.0000
0.8741
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
0.0000
0.0745
0.0000
0.1291
0.0000
0.1133
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.0000
0.0014
0.0000
0.0036
0.0000
0.0013
38
Nitrogen
0.0000
0.0180
0.0000
0.0291
0.0000
0.0113
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Methane
0.0000
0.9061
0.0000
0.8382
0.0000
0.8741
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
0.0000
0.0745
0.0000
0.1291
0.0000
0.1133
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0014
0.0000
0.0036
0.0000
0.0013
57
Nitrogen
0.0000
0.0180
0.0000
0.0291
0.0000
0.0113
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
63
K VALUE
64 65
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 316 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25
FEED TO
PRODUCT FROM
26
Component Splitter:
27
LOGICAL CONNECTION D-4A
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Inactive) Molar:
* 414.7 psia
0.0000 lbmole/hrMass:
37
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: H2S-1
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
60.00*
60.00
(psia)
414.7*
414.7
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
0.0000 -3.254e+004
0.0000 -3.254e+004
37.34
37.34
(Btu/hr)
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.34
(lbmole/ft3) (lb/ft3)
8.051e-002
17.34 8.051e-002
1.396
1.396
(barrel/day)
0.0000
0.0000
(Btu/lb)
-1876
-1876
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 317 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S-1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
16
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
17
HHV Mass Basis (Std)
2.274e+004
2.274e+004
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
Phase Fraction [Vol. Basis]
1.000
1.000
23
Phase Fraction [Mass Basis]
1.000
1.000
24
Phase Fraction [Act. Vol. Basis]
---
---
25
Mass Exergy
(Btu/lb)
201.3
---
26
Partial Pressure of CO2
(psia)
0.5811
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
0.0000
29
Avg. Liq. Density
30
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.153
2.153
9.668
9.668
0.5575
0.5575
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
(ACFM)
0.0000
(lbmole/ft3)
---
---
Specific Heat
(Btu/lbmole-F)
9.668
9.668
31
Std. Gas Flow
(MMSCFD)
32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60 61
0.0000
0.0000
(lb/ft3)
19.49
19.49
(USGPS)
---
---
0.9237
0.9237
19.04
19.04
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
0.0000
---
1.258
1.258
1.406
1.406
2673
---
0.5163
0.5163
4.592e-002
(barrel/day)
4.592e-002
0.0000
0.0000
0.0000
0.0000
(ft3/lbmole)
12.42
12.42
(Btu/lb)
154.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.944e-002
1.944e-002
1.155e-002
1.155e-002
7.682
7.682
0.4430
0.4430
6.876
6.876
0.3965
0.3965
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
Viscosity Index
-38.94
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
1.0000
LIQUID VOLUME FRACTION 0.0000
Page 318 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S-1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
0.0000
0.9061
0.0000
0.8382
0.0000
0.8741
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
0.0000
0.0745
0.0000
0.1291
0.0000
0.1133
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.0000
0.0014
0.0000
0.0036
0.0000
0.0013
23
Nitrogen
0.0000
0.0180
0.0000
0.0291
0.0000
0.0113
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Methane
0.0000
0.9061
0.0000
0.8382
0.0000
0.8741
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
0.0000
0.0745
0.0000
0.1291
0.0000
0.1133
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0000
0.0014
0.0000
0.0036
0.0000
0.0013
42
Nitrogen
0.0000
0.0180
0.0000
0.0291
0.0000
0.0113
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
---
---
---
52
H2O
---
---
---
53
Oxygen
---
---
---
54
Methane
---
---
---
---
---
---
55
H2S
56
Hydrogen
---
---
---
57
Ethane
---
---
---
58
Propane
---
---
---
59
CO2
---
---
---
60
Nitrogen
---
---
---
---
---
---
61
Air
62
Mercury
---
---
---
63
MEAmine
---
---
---
64
Ammonia
---
---
---
65
UNIT OPERATIONS
66 67
FEED TO
68 69
PRODUCT FROM Component Splitter:
Aspen Technology Inc. Licensed to: LEGENDS
LOGICAL CONNECTION D-4B
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 319 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S-1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Active):
18
Flow Specification
(Inactive) Molar:
* 414.7 psia
0.0000 lbmole/hrMass:
19
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: MEA
28 29 30
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
Liquid Phase
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
* 1.995e+004
1.995e+004
39
Molar Enthalpy
(Btu/lbmole)
-1.128e+005
-1.128e+005
40
Molar Entropy
(Btu/lbmole-F)
41
Heat Flow
42
Liq Vol Flow @Std Cond
0.0000
1.0000
(F)
110.0*
110.0
(psia)
244.7*
244.7
(lbmole/hr) (lb/hr)
4851 2.963e+005
3.899
4851 2.963e+005
3.899
(Btu/hr)
-5.474e+008
-5.474e+008
(barrel/day)
* 1.994e+004
1.994e+004
43
PROPERTIES
44 45
Overall
Liquid Phase
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Mass Enthalpy
(Btu/lb)
51
Mass Entropy
(Btu/lb-F)
52
Heat Capacity
53
Mass Heat Capacity
54
LHV Molar Basis (Std)
(Btu/lbmole)
5.860e+005
5.860e+005
55
HHV Molar Basis (Std)
(Btu/lbmole)
6.477e+005
6.477e+005
56
HHV Mass Basis (Std)
1.060e+004
1.060e+004
57
CO2 Loading
58
CO2 App ML Con
59
CO2 App WT Con
60
LHV Mass Basis (Std)
61
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
61.08
61.08
1.006
1.006
61.47 2.061e+004 -1847 6.383e-002
61.47 2.061e+004 -1847 6.383e-002
43.26
43.26
0.7082
0.7082
0.0000
0.0000
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
9594
9594
Phase Fraction [Vol. Basis]
0.0000
1.000
62
Phase Fraction [Mass Basis]
0.0000
1.000
63
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
64
Mass Exergy
(Btu/lb)
1.774
---
65
Partial Pressure of CO2
(psia)
0.0000
---
66
Cost Based on Flow
(Cost/s)
0.0000
0.0000
67
Act. Gas Flow
68
Avg. Liq. Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(ACFM)
---
---
(lbmole/ft3)
1.039
1.039
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 320 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Liquid Phase
12
Specific Heat
(Btu/lbmole-F)
43.26
43.26
13
Std. Gas Flow
(MMSCFD)
44.10
44.10
14
Std. Ideal Liq. Mass Density
(lb/ft3)
63.49
63.49
15
Act. Liq. Flow
(USGPS)
10.02
16
Z Factor
17
Watson K
18
User Property
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
(psia)
41
True VP at 37.8 C
(psia)
42
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
43
Viscosity Index
3.977e-002
(psia)
(Btu/lbmole) (cSt)
9.103
9.103
---
---
0.0000
---
1.048
1.048
2.950
2.950
1.404e+004 11.05
(lb/ft3)
63.53
(barrel/day) (ft3/lbmole) (Btu/lb)
10.02 3.977e-002
1.994e+004
--11.05 63.53 1.994e+004
1.000
1.000
0.9937
0.9937
229.9
---
0.0000
1.0000
(dyne/cm)
46.52
46.52
(Btu/hr-ft-F)
0.1091
0.1091
10.88
10.88
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
41.28
41.28
0.6757
0.6757
14.67
14.67
0.2401
0.2401
---
---
---
---
---
---
2.125e-002
2.125e-002
2.125e-002
2.125e-002
1.994e+004
1.994e+004
24.13
44
---
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
50
CO
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
51
H2O
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
52
Oxygen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
53
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
54
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
55
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
56
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
57
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
58
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
59
Nitrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
60
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
61
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
62
MEAmine
63
Ammonia
64
Total
* 4851.3340 * 0.0000
4851.3340
* 1.0000 * 0.0000
1.0000
* 296338.4030 * 0.0000
296338.4030
* 1.0000 * 0.0000
1.0000
* 19952.5350 * 0.0000
19952.5350
* 1.0000 * 0.0000
1.0000
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 321 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
4851.3340
1.0000
28
Ammonia
0.0000
0.0000
29
Total
4851.3340
1.0000
296338.4030 0.0000 296338.4030
30
1.0000
19952.5350
0.0000
1.0000
0.0000
1.0000
0.0000
19952.5350
1.0000
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
0.0000
0.0000
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Absorber:
LOGICAL CONNECTION
T-100
51
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Active):
60
Flow Specification
(Active)
61
* 244.7 psia
Molar:
4851 lbmole/hrMass:
* 2.963e+005 lb/hrStd Ideal Liq Volume: 1.995e+004 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 322 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA RICA
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Liquid Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
2.043e+004
2.043e+004
18
Molar Enthalpy
(Btu/lbmole)
-1.133e+005
-1.133e+005
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
0.0000
1.0000
(F)
113.3
113.3
(psia)
229.7
229.7
(lbmole/hr) (lb/hr)
4995 3.015e+005
5.022
4995 3.015e+005
5.022
(Btu/hr)
-5.657e+008
-5.657e+008
(barrel/day)
* 2.036e+004
2.036e+004
22
PROPERTIES
23 24
Overall
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
30
Mass Entropy
(Btu/lb-F)
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
5.707e+005
5.707e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
6.309e+005
6.309e+005
35
HHV Mass Basis (Std)
1.045e+004
1.045e+004
36
CO2 Loading
1.992e-002
1.992e-002
37
CO2 App ML Con
(lbmole/ft3)
1.958e-002
1.958e-002
38
CO2 App WT Con
(lbmol/lb)
3.205e-004
3.205e-004
39
LHV Mass Basis (Std)
40
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
60.37
60.37
1.012
1.012
61.10 2.110e+004 -1876 8.319e-002
61.10 2.110e+004 -1876 8.319e-002
42.61
42.61
0.7058
0.7058
9455
9455
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
2.134
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
1.045
1.045
Specific Heat
(Btu/lbmole-F)
42.61
42.61
Std. Gas Flow
(MMSCFD)
45.40
45.40
(lb/ft3)
63.08
63.08
(USGPS)
10.25
Licensed to: LEGENDS
3.691e-002
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb)
10.25 3.691e-002
9.109
9.109
---
---
0.0000
---
1.049
1.049
2.803
2.803
2.061e+004 9.896 63.32 2.036e+004
--9.896 63.32 2.036e+004
1.000
1.000
0.9880
0.9880
341.4
---
0.0000
1.0000
(dyne/cm)
45.05
45.05
(Btu/hr-ft-F)
0.1060
0.1060
9.685
9.685
(cP)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 323 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA RICA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Liquid Phase
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
236.3
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
40.62
40.62
0.6729
0.6729
15.20
15.20
0.2518
0.2518
18.88
18.88
0.3128
0.3128
2.256
2.256
21.56
21.56 236.3
2.036e+004
2.036e+004
23.52
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.6790
0.0001
19.0190
0.0001
1.6291
0.0001
30
H2O
14.4510
0.0029
260.3363
0.0009
17.8619
0.0009
31
Oxygen
4.1931
0.0008
134.1791
0.0004
8.0757
0.0004
32
Methane
3.6632
0.0007
58.7686
0.0002
13.4407
0.0007
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
8.4386
0.0017
17.0122
0.0001
16.6746
0.0008
35
Ethane
9.4564
0.0019
284.3530
0.0009
54.7410
0.0027
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
96.6394
0.0193
4253.0720
0.0141
352.8505
0.0173
38
Nitrogen
6.3500
0.0013
177.8814
0.0006
15.1047
0.0007
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
4850.9181
0.9712
42
Ammonia
0.0000
0.0000
43
Total
4994.7887
1.0000
44
296312.9955 0.0000 301517.6171
0.9827
19950.8243
0.0000 1.0000
46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
0.0000
20431.2026
Liquid Phase
45
0.9765
0.0000
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.6790
0.0001
19.0190
0.0001
1.6291
0.0001
49
H2O
14.4510
0.0029
260.3363
0.0009
17.8619
0.0009
50
Oxygen
4.1931
0.0008
134.1791
0.0004
8.0757
0.0004
51
Methane
3.6632
0.0007
58.7686
0.0002
13.4407
0.0007
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
8.4386
0.0017
17.0122
0.0001
16.6746
0.0008
54
Ethane
9.4564
0.0019
284.3530
0.0009
54.7410
0.0027
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
96.6394
0.0193
4253.0720
0.0141
352.8505
0.0173
57
Nitrogen
6.3500
0.0013
177.8814
0.0006
15.1047
0.0007
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
4850.9181
0.9712
61
Ammonia
0.0000
0.0000
62
Total
4994.7887
1.0000
63
0.0000 301517.6171
0.9827
19950.8243
0.0000
0.9765
0.0000
1.0000
0.0000
20431.2026
1.0000
K VALUE
64 65
296312.9955
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
0.0000
0.0000
---
67
H2O
0.0000
0.0000
---
68
Oxygen
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 324 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA RICA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
0.0000
0.0000
---
---
---
---
14
Hydrogen
0.0000
0.0000
---
15
Ethane
0.0000
0.0000
---
16
Propane
---
---
---
17
CO2
0.0000
0.0000
---
18
Nitrogen
0.0000
0.0000
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
0.0000
0.0000
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Mixer:
MIX-101 Absorber:
27
LOGICAL CONNECTION T-100
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
229.7 psia 4995 lbmole/hrMass:
37
3.015e+005 lb/hrStd Ideal Liq Volume: 2.043e+004 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: MEA.
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
Vapour Phase
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
2.054e+004
57
Molar Enthalpy
(Btu/lbmole)
-1.007e+005
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Liquid Phase
0.2258
0.2258
0.7742
(F)
322.8
322.8
322.8
(psia)
15.00*
15.00
15.00
5020
1134
(lbmole/hr) (lb/hr)
3.033e+005
24.98
(Btu/hr)
-5.054e+008
(barrel/day)
* 2.041e+004
61
6.608e+004 4566 -9.243e+004 46.97 -1.048e+008 4441
3886 2.372e+005 1.597e+004 -1.031e+005 18.57 -4.006e+008 1.596e+004
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 60.42
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
8.043e-003 0.4860 2.668e+006 -1666
58.30 1.830e-003 0.1067 2.648e+006 -1586
Liquid Phase 61.04 0.8532 52.08 1.947e+004 -1689
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 325 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
5.668e+005
5.033e+005
5.853e+005
16
HHV Molar Basis (Std)
(Btu/lbmole)
6.265e+005
5.564e+005
6.469e+005
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.4134
0.8057
43.96
24.14
49.75
0.7276
0.4141
0.8149
1.037e+004
0.3041
9544
1.060e+004
---
---
5.268e-004
(lbmole/ft3)
---
---
4.489e-004
(lbmol/lb)
---
---
8.619e-006
(Btu/lb)
9380
8633
9588
Phase Fraction [Vol. Basis]
0.2223
0.2223
0.7777
23
Phase Fraction [Mass Basis]
0.2179
0.2179
24
Phase Fraction [Act. Vol. Basis]
0.9927
0.9927
25
Mass Exergy
(Btu/lb)
54.07
---
26
Partial Pressure of CO2
(psia)
1.965
---
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
(psia)
59
True VP at 37.8 C
(psia)
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(ACFM)
1.033e+004
1.033e+004
0.7821 7.298e-003 ---
---
(lbmole/ft3)
1.045
1.061
1.040
Specific Heat
(Btu/lbmole-F)
43.96
24.14
49.75
Std. Gas Flow
(MMSCFD)
45.63
10.30
35.33
(lb/ft3)
63.12
61.86
63.48
(USGPS)
9.464
---
---
0.9762
9.099
9.081
9.103
---
---
---
0.0000
---
---
1.047
1.090
1.042
1.012
1.101
1.042
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
3.497e+004
9.464 2.094e-003
---
---
---
4.347
1.665
63.54
63.61
2.041e+004
4441
63.52 1.596e+004
0.7742
0.0000
1.000
(ft3/lbmole)
124.3
546.5
1.172
(Btu/lb)
578.8
---
---
0.2258
0.2258
0.7742
(dyne/cm)
25.58
(Btu/hr-ft-F)
---
1.246e-002
---
7.427e-003
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
25.58 8.386e-002 1.389
41.98
22.15
47.76
0.6947
0.3800
0.7824
43.46
21.93
47.76
0.7193
0.3762
0.7824
---
---
---
---
---
---
---
---
---
21.16
98.38
0.3874
37.71
170.0
2.040e+004 8.787
62
4441 ---
0.6833 1.596e+004 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0011
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0001
0.2258
LIQUID VOLUME FRACTION 0.0000
Page 326 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2258
LIQUID VOLUME FRACTION
15
H2O
14.4510
0.0029
260.3363
0.0009
17.8619
0.0009
16
Oxygen
0.0005
0.0000
0.0151
0.0000
0.0009
0.0000
17
Methane
0.0046
0.0000
0.0743
0.0000
0.0170
0.0000
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
3.8453
0.0008
115.6287
0.0004
22.2598
0.0011
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
150.5434
0.0300
6625.3710
0.0218
549.6652
0.0268
23
Nitrogen
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
4850.9181
0.9664
27
Ammonia
0.0000
0.0000
28
Total
5019.7630
1.0000
29
296312.9955 0.0000 303314.4222
0.9769 0.0000 1.0000
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
MASS FRACTION
19950.8243 0.0000
0.9713 0.0000
20540.6292
1.0000
Phase Fraction
0.2258
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
34
H2O
11.7701
0.0104
212.0396
0.0032
14.5482
0.0032
35
Oxygen
0.0005
0.0000
0.0150
0.0000
0.0009
0.0000
36
Methane
0.0046
0.0000
0.0739
0.0000
0.0169
0.0000
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
3.7836
0.0033
113.7731
0.0017
21.9026
0.0048
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
148.4988
0.1310
6535.3880
0.0989
542.1998
0.1187
42
Nitrogen
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
969.5452
0.8553
0.8962
3987.5394
0.8733
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
1133.6029
1.0000
1.0000
4566.2079
1.0000
48
59223.6049 0.0000 66084.8957
Liquid Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7742 LIQUID VOLUME FRACTION
52
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
H2O
2.6809
0.0007
48.2968
0.0002
3.3137
0.0002
54
Oxygen
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
55
Methane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Ethane
0.0617
0.0000
1.8556
0.0000
0.3572
0.0000
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
2.0446
0.0005
89.9830
0.0004
7.4653
0.0005
61
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
3881.3728
0.9988
65
Ammonia
0.0000
0.0000
66
Total
3886.1601
1.0000
237089.3906 0.0000 237229.5265
0.9994 0.0000 1.0000
15963.2850 0.0000 15974.4213
0.9993 0.0000 1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 327 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
1620
1620
---
13
H2O
15.05
15.05
---
14
Oxygen
874.3
874.3
---
15
Methane
625.2
625.2
---
---
---
---
16
H2S
17
Hydrogen
1984
1984
---
18
Ethane
210.2
210.2
---
19
Propane
---
---
---
20
CO2
249.0
249.0
---
21
Nitrogen
1484
1484
---
---
---
---
22
Air
23
Mercury
---
---
---
24
MEAmine
0.8563
0.8563
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Recycle:
RCY-5
Valve:
LOGICAL CONNECTION VLV-104
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 15.00 psia
5020 lbmole/hrMass:
40
3.033e+005 lb/hrStd Ideal Liq Volume: 2.054e+004 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: MEA..
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
2.054e+004
60
Molar Enthalpy
(Btu/lbmole)
-1.007e+005
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Liquid Phase
0.2258
0.2258
0.7742
(F)
322.8*
322.8
322.8
(psia)
15.00*
15.00
15.00
5020*
1134
(lbmole/hr) (lb/hr)
3.033e+005
24.98
(Btu/hr)
-5.054e+008
(barrel/day)
* 2.041e+004
64
6.608e+004 4566 -9.243e+004 46.97 -1.048e+008 4441
3886 2.372e+005 1.597e+004 -1.031e+005 18.57 -4.006e+008 1.596e+004
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 60.42
(lbmole/ft3)
8.043e-003
58.30 1.830e-003
Liquid Phase 61.04 0.8532
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 328 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA.. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-1666
-1586
-1689
15
Mass Entropy
(Btu/lb-F)
0.4134
0.8057
0.3041
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
5.668e+005
5.033e+005
5.853e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
6.265e+005
5.564e+005
6.469e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.4860 2.668e+006
0.1067 2.648e+006
52.08 1.947e+004
43.96
24.14
49.75
0.7276
0.4141
0.8149
9544
1.060e+004
---
---
5.268e-004
(lbmole/ft3)
---
---
4.489e-004
(lbmol/lb)
---
---
8.619e-006
(Btu/lb)
9380
8633
9588
Phase Fraction [Vol. Basis]
0.2223
0.2223
0.7777
26
Phase Fraction [Mass Basis]
0.2179
0.2179
27
Phase Fraction [Act. Vol. Basis]
0.9927
0.9927
28
Mass Exergy
(Btu/lb)
54.07
---
29
Partial Pressure of CO2
(psia)
1.965
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(ACFM)
1.037e+004
1.033e+004
1.033e+004
0.7821 7.298e-003 ---
---
(lbmole/ft3)
1.045
1.061
1.040
Specific Heat
(Btu/lbmole-F)
43.96
24.14
49.75
Std. Gas Flow
(MMSCFD)
45.63
10.30
35.33
(lb/ft3)
63.12
61.86
63.48
(USGPS)
9.464
---
---
0.9762
9.099
9.081
9.103
---
---
---
0.0000
---
---
1.047
1.090
1.042
1.012
1.101
1.042
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
3.497e+004
9.464 2.094e-003
---
---
---
4.347
1.665
63.54
63.61
2.041e+004
4441
63.52 1.596e+004
0.7742
0.0000
1.000
(ft3/lbmole)
124.3
546.5
1.172
(Btu/lb)
578.8
---
---
0.2258
0.2258
0.7742
(dyne/cm)
25.58
(Btu/hr-ft-F)
---
1.246e-002
---
7.427e-003
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
25.58 8.386e-002 1.389
41.98
22.15
47.76
0.6947
0.3800
0.7824
43.46
21.93
47.76
0.7193
0.3762
0.7824
---
---
---
---
---
---
---
---
---
21.16
98.38
0.3874
37.71
170.0
2.040e+004 8.787
4441 ---
0.6833 1.596e+004 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 329 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA.. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14 15
CO
16
H2O
17
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2258
LIQUID VOLUME FRACTION
* 0.0000
* 0.0000
* 0.0011
* 0.0000
* 0.0001
* 0.0000
* 14.4510
* 0.0029
* 260.3363
* 0.0009
* 17.8619
* 0.0009
Oxygen
* 0.0005
* 0.0000
* 0.0151
* 0.0000
* 0.0009
* 0.0000
18
Methane
* 0.0046
* 0.0000
* 0.0743
* 0.0000
* 0.0170
* 0.0000
19
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
20
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
21
Ethane
* 3.8453
* 0.0008
* 115.6287
* 0.0004
* 22.2598
* 0.0011
22
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
23
CO2
* 150.5434
* 0.0300
* 0.0218
* 549.6652
* 0.0268
24
Nitrogen
* 0.0000
* 0.0000
* 0.0002
* 0.0000
* 0.0000
* 0.0000
25
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
26
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
27
MEAmine
28
Ammonia
29
Total
* 4850.9181 * 0.0000
5019.7630
* 0.9664 * 0.0000
1.0000
30
* 6625.3710
* 296312.9955 * 0.0000
303314.4222
* 0.9769 * 0.0000
1.0000
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
MASS FRACTION
* 19950.8243 * 0.0000
* 0.9713 * 0.0000
20540.6292
1.0000
Phase Fraction
0.2258
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
35
H2O
11.7701
0.0104
212.0395
0.0032
14.5482
0.0032
36
Oxygen
0.0005
0.0000
0.0150
0.0000
0.0009
0.0000
37
Methane
0.0046
0.0000
0.0739
0.0000
0.0169
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
3.7836
0.0033
113.7731
0.0017
21.9026
0.0048
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
148.4988
0.1310
6535.3879
0.0989
542.1998
0.1187
43
Nitrogen
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
969.5446
0.8553
0.8962
3987.5367
0.8733
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
1133.6022
1.0000
1.0000
4566.2052
1.0000
49
59223.5645 0.0000 66084.8553
Liquid Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7742 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
2.6809
0.0007
48.2968
0.0002
3.3137
0.0002
55
Oxygen
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0617
0.0000
1.8556
0.0000
0.3572
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
2.0446
0.0005
89.9831
0.0004
7.4653
0.0005
62
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
3881.3735
0.9988
66
Ammonia
0.0000
0.0000
67
Total
3886.1607
1.0000
237089.4310 0.0000 237229.5669
0.9994 0.0000 1.0000
15963.2877 0.0000 15974.4240
0.9993 0.0000 1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 330 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA.. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
1620
1620
---
13
H2O
15.05
15.05
---
14
Oxygen
874.3
874.3
---
15
Methane
625.2
625.2
---
---
---
---
16
H2S
17
Hydrogen
1984
1984
---
18
Ethane
210.2
210.2
---
19
Propane
---
---
---
20
CO2
249.0
249.0
---
21
Nitrogen
1484
1484
---
---
---
---
22
Air
23
Mercury
---
---
---
24
MEAmine
0.8563
0.8563
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Recycle:
LOGICAL CONNECTION RCY-5
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
* 15.00 psia * Mass: 5020 lbmole/hr
40
3.033e+005 lb/hrStd Ideal Liq Volume: 2.054e+004 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: NH3
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
79.29
79.29
(psia)
229.7
229.7
250.4
250.4
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
4339
4339
483.2
483.2
-3.038e+004 19.86 -7.606e+006 482.5*
(barrel/day)
64
-3.038e+004 19.86 -7.606e+006 482.5
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Liquid Phase 17.33
17.33
2.161
2.161
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 331 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: NH3 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Density
13
Act. Volume Flow
14
(lb/ft3)
Liquid Phase 37.47
37.47
(barrel/day)
495.1
495.1
Mass Enthalpy
(Btu/lb)
-1753
-1753
15
Mass Entropy
(Btu/lb-F)
1.146
1.146
16
Heat Capacity
20.45
20.45
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
1.380e+005
1.380e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
1.644e+005
1.644e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
1.336e-002
1.336e-002
23
CO2 App WT Con
(lbmol/lb)
3.567e-004
3.567e-004
24
LHV Mass Basis (Std)
25
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.180
1.180
9487
9487
14.19
14.19
7964
7964
Phase Fraction [Vol. Basis]
0.0000
1.000
26
Phase Fraction [Mass Basis]
0.0000
1.000
27
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
28
Mass Exergy
(Btu/lb)
135.7
---
29
Partial Pressure of CO2
(psia)
0.0000
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
2.215
2.215
Specific Heat
(Btu/lbmole-F)
20.45
20.45
Std. Gas Flow
(MMSCFD)
2.276
2.276
(lb/ft3)
38.39
38.39
(USGPS)
0.2407
0.2407
1.837e-002
(psia)
(Btu/lbmole)
1.837e-002
12.27
12.27
---
---
0.0000
---
1.108
1.108
2.319
2.319
9450
---
(cSt)
0.2063
0.2063
(lb/ft3)
38.45
38.45
482.5
482.5
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4626
0.4626
545.2
---
0.0000
1.0000
(dyne/cm)
25.66
25.66
(Btu/hr-ft-F)
0.2688
0.2688
0.1238
0.1238
18.47
18.47
1.065
1.065
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
8.820
8.820
0.5088
0.5088
5.954
---
0.3435
---
3.435
---
(psia)
234.0
234.0
(psia)
287.9
287.9
482.5
482.5
-62.73
---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 332 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: NH3 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
16
H2O
1.8304
0.0073
32.9751
0.0076
2.2625
0.0047
17
Oxygen
0.3767
0.0015
12.0553
0.0028
0.7256
0.0015
18
Methane
0.4555
0.0018
7.3074
0.0017
1.6712
0.0035
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0215
0.0001
0.0433
0.0000
0.0425
0.0001
21
Ethane
1.7337
0.0069
52.1314
0.0120
10.0359
0.0208
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
1.5480
0.0062
68.1279
0.0157
5.6521
0.0117
24
Nitrogen
0.0074
0.0000
0.2077
0.0000
0.0176
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1091
0.0004
6.6643
0.0015
0.4487
0.0009
28
Ammonia
244.2724
0.9757
4159.9584
0.9586
462.3567
0.9568
29
Total
250.3547
1.0000
4339.4720
1.0000
483.2129
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
35
H2O
1.8304
0.0073
32.9751
0.0076
2.2625
0.0047
36
Oxygen
0.3767
0.0015
12.0553
0.0028
0.7256
0.0015
37
Methane
0.4555
0.0018
7.3074
0.0017
1.6712
0.0035
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0215
0.0001
0.0433
0.0000
0.0425
0.0001
40
Ethane
1.7337
0.0069
52.1314
0.0120
10.0359
0.0208
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
1.5480
0.0062
68.1279
0.0157
5.6521
0.0117
43
Nitrogen
0.0074
0.0000
0.2077
0.0000
0.0176
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.1091
0.0004
6.6643
0.0015
0.4487
0.0009
47
Ammonia
244.2724
0.9757
4159.9584
0.9586
462.3567
0.9568
48
Total
250.3547
1.0000
4339.4720
1.0000
483.2129
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
0.0000
0.0000
---
53
H2O
0.0000
0.0000
---
54
Oxygen
0.0000
0.0000
---
55
Methane
0.0000
0.0000
---
---
---
---
56
H2S
57
Hydrogen
0.0000
0.0000
---
58
Ethane
0.0000
0.0000
---
59
Propane
---
---
---
60
CO2
0.0000
0.0000
---
61
Nitrogen
0.0000
0.0000
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
0.0000
0.0000
---
65
Ammonia
0.0000
0.0000
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 333 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: NH3 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Mixer:
LOGICAL CONNECTION MIX-108
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
229.7 psia 250.4 lbmole/hrMass:
23
4339 lb/hr Std Ideal Liq Volume:
483.2 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: Vapor de agua
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
3041
3041
44
Molar Entropy
(Btu/lbmole-F)
32.72
32.72
45
Heat Flow
(Btu/hr)
0.0000
0.0000
46
Liq Vol Flow @Std Cond
(barrel/day)
* 0.0000
0.0000
1.0000
1.0000
(F)
500.0*
500.0
(psia)
314.7*
314.7
* 0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
47
PROPERTIES
48 49
Overall
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Vapour Phase 32.00
(lbmole/ft3) (lb/ft3)
3.047e-002
32.00 3.047e-002
0.9751
0.9751
(barrel/day)
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
95.04
95.04
55
Mass Entropy
(Btu/lb-F)
1.022
1.022
56
Heat Capacity
57
Mass Heat Capacity
58 59 60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66 67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
7.588
7.588
(Btu/lb-F)
0.2371
0.2371
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
HHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
0.0000
0.0000
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
---
---
Licensed to: LEGENDS
(Btu/lbmole-F)
(Btu/lb)
(Btu/lb)
127.3
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 334 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Vapor de agua (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Vapour Phase
(psia)
0.0000
---
(Cost/s)
0.0000
0.0000 0.0000
(ACFM)
0.0000
(lbmole/ft3)
---
---
Specific Heat
(Btu/lbmole-F)
7.588
7.588
17
Std. Gas Flow
(MMSCFD)
18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
0.0000
0.0000
(lb/ft3)
71.02
71.02
(USGPS)
---
---
Z Factor
1.003
1.003
21
Watson K
4.786
4.786
22
User Property
---
---
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46 47
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
0.0000
---
1.354
1.354
1.369
1.369
1935
---
2.075
2.075
8.458e-002
(barrel/day)
8.458e-002
0.0000
0.0000
0.0000
0.0000
(ft3/lbmole)
32.82
32.82
(Btu/lb)
60.48
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
2.537e-002
2.537e-002
3.241e-002
3.241e-002
5.602
5.602
0.1751
0.1751
5.543
5.543
0.1732
0.1732
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
Viscosity Index
-20.27
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
54
CO
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
55
H2O
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
56
Oxygen
* 0.0000
* 1.0000
* 0.0000
* 1.0000
* 0.0000
* 1.0000
57
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
58
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
59
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
60
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
61
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
62
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
63
Nitrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
64
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
65
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
66
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
67
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
68
Total
0.0000
1.0000
0.0000
1.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 335 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Vapor de agua (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Distillation:
LOGICAL CONNECTION
T-7
51
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Active):
60
Flow Specification
(Active)
61
* 314.7 psia
Molar:
* Mass: 0.0000 lbmole/hr
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 336 of 336 * Specified by user.
REEMPLAZA A:
REV.
REEMPLAZADO POR:
REV.
ESTE DOCUMENTO ES PROPIEDAD DE STARK INDUSTRIES
TITULO: BALANCE DE MATERIA Y ENERGIA OBRA: MEMORIA DE CÁLCULO
IDENTIFICACIÓN:
ESCALA:
REVISION: 1
N/A CND-FEND-MEXXX
A
MEMORIA DE CÁLCULO
ELABORO
Ing. Jose Maria Ayaa
REVISO
Ing. Jose Maria Ayala
APROBÓ A REV.
PARA APROBACIÓN
29.12.18
DESCRIPCIÓN
FECHA
MPR ELABORO
ACS
HDL
REVISO
APROBÓ
LISTA DE REVISIONES
2
Memoria de Cálculo BALANCE DE MASA Y ENERGIA
Identificación CND-FENDMEXXX
Revisión
Pág. 1
De 22
A
1
OBJETIVO .................................................................................................................... 4
2
ALCANCE ..................................................................................................................... 4
3
DATOS Y CÁLCULOS..................................................................................................... 4
4
CONCLUSIONES ......................................................................................................... 57
3
Memoria de Cálculo BALANCE DE MATERIA Y ENERGÍA
Identificación CND-FENDMEXXX
Revisión A
1
OBJETIVO
Mediante el presente trabajo se pretende simular y validar la planta de amoniaco y urea 2
ALCANCE
El balance de masa y energía adjunto en el presente documento es el resultado de una simulación de una planta de Amoniaco y Urea. Se utilizó el programa Aspen Hysys v8.8. 3. Datos y cálculos Parámetros de las especificaciones técnicas .
Compositions Comp Mole Frac (CO) Comp Mole Frac (H2O) Comp Mole Frac (Oxygen) Comp Mole Frac (Methane) Comp Mole Frac (H2S) Comp Mole Frac (Hydrogen) Comp Mole Frac (Ethane) Comp Mole Frac (Propane) Comp Mole Frac (CO2) Comp Mole Frac (Nitrogen) Comp Mole Frac (Air) Comp Mole Frac (Mercury) Comp Mole Frac (MEAmine) Comp Mole Frac (Ammonia)
Gas de Alimentacion 0 0 0 0.906 10 0 0.074 50 0.001 0.018 4 0 0 0 0
Gas Combustible 0 0 0 0.906 10 0 0.074 50 0.001 0.018 4 0 0 0 0
Vapor 0 1 0 0 0 0 0 0 0 0 0 0 0 0
H2S-1 0 0 0 0.906 10 0 0.074 50 0.001 0.018 4 0 0 0 0
4
Memoria de Cálculo BALANCE DE MATERIA Y ENERGÍA
Identificación CND-FENDMEXXX
Revisión A
Compositions Comp Mole Frac (CO) Comp Mole Frac (H2O) Comp Mole Frac (Oxygen) Comp Mole Frac (Methane) Comp Mole Frac (H2S) Comp Mole Frac (Hydrogen) Comp Mole Frac (Ethane) Comp Mole Frac (Propane) Comp Mole Frac (CO2) Comp Mole Frac (Nitrogen) Comp Mole Frac (Air) Comp Mole Frac (Mercury) Comp Mole Frac (MEAmine) Comp Mole Frac (Ammonia)
H2S-Stand By 0 0 0 0.90 61 0 0 0.07 45 0 0.00 0.01 14 8 0 0 0 0
Gas de Alimentacion
Conditions
gasc 0.43 72 0 0.03 0.02 12 69 0 0.00 0.03 05 09 0 0.42 0.04 65 69 0 0 0 0
Gas Combustible
Temperature (F)
60
60
Pressure (psia)
414. 7 792. 2
414. 7 351. 6
Molar Flow (lbmol/hr)
Compositions Temperature (F) Pressure (psia) Molar Flow (lbmol/hr)
Corrientes de Amoniaco 84 y 85 0 0 0.00 0.00 0.00 73 0.00 73 0.00 15 0.00 15 18 0 18 0 0.00 0.00 0.00 01 0.00 01 69 0 69 0 0.00 0.00 62 0 62 0 0 0 0 0 0.00 0.00 0.97 04 0.97 04 57 57
Vap or
gasc
274. 9 364. 7 191 8
335. 170 3 133. 8
Corrientes de Amoniaco 84 y 85 79.29 79.29 229.7 229.7 203 250.4
5
Memoria de Cálculo BALANCE DE MATERIA Y ENERGÍA
Identificación CND-FENDMEXXX
Revisión A
4. CONCUSIONES
El sistema de producción de amoniaco tiene una producción nominal de 200 toneladas día. Los flujos, composiciones, presiones y temperaturas están presentes en el work book. El presente documento tiene relación con el documento de l
6
Memoria de Cálculo BALANCE DE MATERIA Y ENERGÍA
Identificación CND-FENDMEXXX
Revisión A
WORK BOOK CORRIENTES
7
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 000
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Vapour Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
1983
1983
18
Molar Enthalpy
(Btu/lbmole)
-8118
-8118
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Liquid Phase
1.0000
1.0000
0.0000
(F)
87.00
87.00
87.00
(psia)
4565
4565
4565
865.2
865.2
0.0000
(lbmole/hr) (lb/hr)
1.450e+004
25.54
1.450e+004
25.54
0.0000 0.0000 -2.941e+004 21.07
(Btu/hr)
-7.024e+006
-7.024e+006
0.0000
(barrel/day)
* 1.399e+006
1.399e+006
0.0000
22
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29 30 31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
9.722e+004
9.722e+004
1.394e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.112e+005
1.112e+005
1.649e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41 42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
16.75
16.75
17.77
0.7725
0.7725
2.039
12.94
12.94
36.24
(barrel/day)
4788
4788
0.0000
Mass Enthalpy
(Btu/lb)
-484.6
-484.6
-1655
Mass Entropy
(Btu/lb-F)
1.525
1.525
1.186
9.827
9.827
18.65
0.5866
0.5866
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.049
6635
6635
9277
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
5803
5803
7845
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
358.1
---
---
(psia)
40.73
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
18.67
18.67
---
(lbmole/ft3)
1.865
1.865
2.120
Specific Heat
(Btu/lbmole-F)
9.827
9.827
18.65
Std. Gas Flow
(MMSCFD)
7.864
7.864
0.0000
(lb/ft3)
31.25
31.25
37.68
(USGPS)
---
---
---
---
1.007
0.3816
10.42
10.42
12.17
---
---
---
0.0000
---
---
1.253
1.253
1.119
1.673
1.673
1.907
6063
---
Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP)
9.675e-002
9.675e-002
--0.1651
4.428e-002
4.428e-002
36.15
1.399e+006
1.399e+006
0.0000
0.0000
0.0000
1.000
1.295
1.295
0.4904
361.9
---
---
1.0000
1.0000
0.0000
---
---
4.891e-002
4.891e-002
2.006e-002
2.006e-002
22.44 0.2277 9.584e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 1 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 000 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
7.841
7.841
16.66
0.4680
0.4680
0.9377
5.874
5.874
9.781
0.3506
0.3506
0.5504
5.850
5.850
9.126
0.3492
0.3492
0.5135
1.680
1.680
2.044
---
---
511.5
---
---
1.399e+006 ---
1.399e+006 ---
23
4059 0.0000 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.1829
0.0002
5.1221
0.0004
0.4387
0.0002
30
H2O
0.0111
0.0000
0.1998
0.0000
0.0137
0.0000
31
Oxygen
121.3251
0.1402
3882.4021
0.2678
233.6677
0.1179
32
Methane
71.9227
0.0831
1153.8485
0.0796
263.8906
0.1331
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
318.8737
0.3686
642.8494
0.0443
630.0928
0.3178
35
Ethane
17.5827
0.0203
528.7093
0.0365
101.7823
0.0513
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
7.7207
0.0089
339.7837
0.0234
28.1897
0.0142
38
Nitrogen
215.2337
0.2488
6029.3408
0.4160
511.9783
0.2582
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0003
0.0000
0.0160
0.0000
0.0011
0.0000
42
Ammonia
112.3241
0.1298
1912.8795
0.1320
212.6061
0.1072
43
Total
865.1768
1.0000
14495.1511
1.0000
1982.6611
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.1829
0.0002
5.1221
0.0004
0.4387
0.0002
49
H2O
0.0111
0.0000
0.1998
0.0000
0.0137
0.0000
50
Oxygen
121.3251
0.1402
3882.4021
0.2678
233.6677
0.1179
51
Methane
71.9227
0.0831
1153.8485
0.0796
263.8906
0.1331
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
318.8737
0.3686
642.8494
0.0443
630.0928
0.3178
54
Ethane
17.5827
0.0203
528.7093
0.0365
101.7823
0.0513
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
7.7207
0.0089
339.7837
0.0234
28.1897
0.0142
57
Nitrogen
215.2337
0.2488
6029.3408
0.4160
511.9783
0.2582
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0003
0.0000
0.0160
0.0000
0.0011
0.0000
61
Ammonia
112.3241
0.1298
1912.8795
0.1320
212.6061
0.1072
62
Total
865.1768
1.0000
14495.1511
1.0000
1982.6611
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
0.0000
0.0097
0.0000
0.0098
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000 LIQUID VOLUME FRACTION 0.0000 0.0059
Page 2 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 000 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
Oxygen
0.0000
0.0278
0.0000
0.0501
0.0000
0.0266
16
Methane
0.0000
0.0203
0.0000
0.0183
0.0000
0.0369
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0000
0.0232
0.0000
0.0026
0.0000
0.0228
19
Ethane
0.0000
0.0162
0.0000
0.0274
0.0000
0.0465
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0000
0.0121
0.0000
0.0299
0.0000
0.0218
22
Nitrogen
0.0000
0.0112
0.0000
0.0176
0.0000
0.0132
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0000
0.0006
0.0000
0.0020
0.0000
0.0012
26
Ammonia
0.0000
0.8790
0.0000
0.8423
0.0000
0.8251
27
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
5.037
5.037
---
34
Methane
4.099
4.099
---
---
---
---
35
H2S
12.33
12.33
1.328e-003
---
1.328e-003
---
36
Hydrogen
15.86
15.86
---
37
Ethane
1.255
1.255
---
38
Propane
---
---
---
39
CO2
0.7400
0.7400
---
40
Nitrogen
22.30
22.30
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
45
5.275e-004
0.1477
---
0.1477
---
UNIT OPERATIONS
46 47 48
5.275e-004
FEED TO
PRODUCT FROM
Mixer:
MIX-104 Tee:
49
LOGICAL CONNECTION TEE-104
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
4565 psia 865.2 lbmole/hrMass:
1.450e+004 lb/hrStd Ideal Liq Volume:
1983 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 3 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
60.00
60.00
(psia)
414.7
414.7
440.7*
440.7
7642
7642
(lbmole/hr) (lb/hr)
1676 -3.254e+004 37.34
1676 -3.254e+004 37.34
(Btu/hr)
-1.434e+007
-1.434e+007
(barrel/day)
* 7.114e+005
7.114e+005
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-1876
-1876
30
Mass Entropy
(Btu/lb-F)
2.153
2.153
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
35
HHV Mass Basis (Std)
2.274e+004
2.274e+004
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
1.000
1.000
41
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
(Btu/lb)
201.3
---
44
Partial Pressure of CO2
(psia)
0.5811
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48
17.34 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
8.051e-002 1.396 2.340e+004
17.34 8.051e-002 1.396 2.340e+004
9.668
9.668
0.5575
0.5575
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
(ACFM)
91.23
91.23
(lbmole/ft3)
1.124
1.124
Specific Heat
(Btu/lbmole-F)
9.668
9.668
49
Std. Gas Flow
(MMSCFD)
4.006
4.006
50
Std. Ideal Liq. Mass Density
(lb/ft3)
19.49
19.49
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
0.9237
0.9237
53
Watson K
19.04
19.04
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.258
1.258
1.406
1.406
2673
---
0.5163
0.5163
4.592e-002
4.592e-002
7.114e+005
7.114e+005
0.0000
0.0000
(ft3/lbmole)
12.42
12.42
(Btu/lb)
154.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
1.944e-002
1.944e-002
1.155e-002
1.155e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 4 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 7.682
7.682
0.4430
0.4430
6.876
6.876
0.3965
0.3965
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
7.114e+005
7.114e+005
-38.94
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
399.3043
0.9061
6405.9987
0.8382
1465.0823
0.8741
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
32.8159
0.0745
986.7710
0.1291
189.9641
0.1133
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.6175
0.0014
27.1761
0.0036
2.2546
0.0013
38
Nitrogen
7.9393
0.0180
222.4045
0.0291
18.8854
0.0113
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
440.6770
1.0000
7642.3504
1.0000
1676.1864
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Methane
399.3043
0.9061
6405.9987
0.8382
1465.0823
0.8741
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
32.8159
0.0745
986.7710
0.1291
189.9641
0.1133
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6175
0.0014
27.1761
0.0036
2.2546
0.0013
57
Nitrogen
7.9393
0.0180
222.4045
0.0291
18.8854
0.0113
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
440.6770
1.0000
7642.3504
1.0000
1676.1864
1.0000
63
K VALUE
64 65
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 5 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Valve:
PIC-1
Tee:
LOGICAL CONNECTION TEE-101
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Active)
414.7 psia * Mass: 440.7 lbmole/hr
Molar:
37
7642 lb/hr Std Ideal Liq Volume:
1676 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 2
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
52.59
52.59
(psia)
306.7*
306.7
440.7
440.7
7642
7642
(lbmole/hr) (lb/hr)
1676 -3.254e+004 37.90
1676 -3.254e+004 37.90
(Btu/hr)
-1.434e+007
-1.434e+007
(barrel/day)
* 7.114e+005
7.114e+005
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.34
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
5.934e-002 1.029 3.174e+004 -1876
17.34 5.934e-002 1.029 3.174e+004 -1876
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 6 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 2 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
16
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
17
HHV Mass Basis (Std)
2.274e+004
2.274e+004
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
Phase Fraction [Vol. Basis]
1.000
1.000
23
Phase Fraction [Mass Basis]
1.000
1.000
24
Phase Fraction [Act. Vol. Basis]
1.000
1.000
25
Mass Exergy
(Btu/lb)
184.0
---
26
Partial Pressure of CO2
(psia)
0.4298
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.185
2.185
9.393
9.393
0.5416
0.5416
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
(ACFM)
123.8
123.8
(lbmole/ft3)
1.124
1.124
Specific Heat
(Btu/lbmole-F)
9.393
9.393
31
Std. Gas Flow
(MMSCFD)
4.006
4.006
32
Std. Ideal Liq. Mass Density
(lb/ft3)
19.49
19.49
33
Act. Liq. Flow
(USGPS)
---
---
34
Z Factor
0.9402
0.9402
35
Watson K
19.04
19.04
36
User Property
---
---
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.268
1.268
1.379
1.379
3065
---
0.6811
0.6811
4.592e-002
4.592e-002
7.114e+005
7.114e+005
0.0000
0.0000
(ft3/lbmole)
16.85
16.85
(Btu/lb)
176.7
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.869e-002
1.869e-002
1.123e-002
1.123e-002
7.407
7.407
0.4271
0.4271
6.813
6.813
0.3928
0.3928
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
7.114e+005 -31.43
62
7.114e+005 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
1.0000
LIQUID VOLUME FRACTION 0.0000
Page 7 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 2 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
399.3043
0.9061
6405.9987
0.8382
1465.0823
0.8741
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
32.8159
0.0745
986.7710
0.1291
189.9641
0.1133
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.6175
0.0014
27.1761
0.0036
2.2546
0.0013
23
Nitrogen
7.9393
0.0180
222.4045
0.0291
18.8854
0.0113
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
440.6770
1.0000
7642.3504
1.0000
1676.1864
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Methane
399.3043
0.9061
6405.9987
0.8382
1465.0823
0.8741
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
32.8159
0.0745
986.7710
0.1291
189.9641
0.1133
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.6175
0.0014
27.1761
0.0036
2.2546
0.0013
42
Nitrogen
7.9393
0.0180
222.4045
0.0291
18.8854
0.0113
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
440.6770
1.0000
7642.3504
1.0000
1676.1864
1.0000
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
---
---
---
52
H2O
---
---
---
53
Oxygen
---
---
---
54
Methane
---
---
---
---
---
---
55
H2S
56
Hydrogen
---
---
---
57
Ethane
---
---
---
58
Propane
---
---
---
59
CO2
---
---
---
60
Nitrogen
---
---
---
---
---
---
61
Air
62
Mercury
---
---
---
63
MEAmine
---
---
---
64
Ammonia
---
---
---
65
UNIT OPERATIONS
66 67 68 69
FEED TO Tee:
Aspen Technology Inc. Licensed to: LEGENDS
PRODUCT FROM TEE-102 Valve:
LOGICAL CONNECTION PIC-1
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 8 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 2 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Active):
18
Flow Specification
(Inactive) Molar:
* 306.7 psia
440.7 lbmole/hrMass:
19
7642 lb/hr Std Ideal Liq Volume:
1676 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: 3
28 29 30
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
39
Molar Enthalpy
(Btu/lbmole)
40
Molar Entropy
(Btu/lbmole-F)
41
Heat Flow
42
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
52.59
52.59
(psia)
306.7
306.7
2.635*
2.635
45.70
45.70
(lbmole/hr) (lb/hr)
(Btu/hr)
10.02 -3.254e+004 37.90 -8.576e+004 4255*
(barrel/day)
43
10.02 -3.254e+004 37.90 -8.576e+004 4255
PROPERTIES
44 45
Overall
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Vapour Phase 17.34
(lbmole/ft3)
17.34 5.934e-002
1.029
1.029
(barrel/day)
189.8
189.8
Mass Enthalpy
(Btu/lb)
-1876
-1876
51
Mass Entropy
(Btu/lb-F)
2.185
2.185
52
Heat Capacity
53
Mass Heat Capacity
54
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
55
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
56
HHV Mass Basis (Std)
2.274e+004
2.274e+004
57
CO2 Loading
58
CO2 App ML Con
59
CO2 App WT Con
60
LHV Mass Basis (Std)
61
Phase Fraction [Vol. Basis]
1.000
1.000
62
Phase Fraction [Mass Basis]
1.000
1.000
63
Phase Fraction [Act. Vol. Basis]
1.000
1.000
64
Mass Exergy
(Btu/lb)
184.0
---
65
Partial Pressure of CO2
(psia)
0.4298
---
66
Cost Based on Flow
(Cost/s)
0.0000
0.0000
67
Act. Gas Flow
(ACFM)
0.7402
0.7402
68
Avg. Liq. Density
(lbmole/ft3)
1.124
1.124
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
5.934e-002
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
9.393
9.393
0.5416
0.5416
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 9 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 3 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Specific Heat
(Btu/lbmole-F)
13
Std. Gas Flow
(MMSCFD)
14
Std. Ideal Liq. Mass Density
15
Act. Liq. Flow
16
Z Factor
17
Watson K
18
User Property
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
41
True VP at 37.8 C
42
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
43
Viscosity Index
Vapour Phase 9.393
2.396e-002
9.393 2.396e-002
(lb/ft3)
19.49
(USGPS)
---
---
0.9402
0.9402
19.04
19.04
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
0.0000
---
1.268
1.268
1.379
1.379
3065
---
0.6811
0.6811
4.592e-002
(barrel/day)
19.49
4.592e-002
4255
4255
0.0000
0.0000
(ft3/lbmole)
16.85
16.85
(Btu/lb)
176.7
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.869e-002
1.869e-002
1.123e-002
1.123e-002
7.407
7.407
0.4271
0.4271
6.813
6.813
0.3928
0.3928
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
4255
4255
-31.43
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
44
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
50
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Methane
2.3879
0.9061
38.3088
0.8382
8.7614
0.8741
54
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Ethane
0.1962
0.0745
5.9010
0.1291
1.1360
0.1133
57
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
CO2
0.0037
0.0014
0.1625
0.0036
0.0135
0.0013
59
Nitrogen
0.0475
0.0180
1.3300
0.0291
0.1129
0.0113
60
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Total
2.6353
1.0000
45.7024
1.0000
10.0238
1.0000
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 10 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 3 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
2.3879
0.9061
38.3088
0.8382
8.7614
0.8741
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.1962
0.0745
5.9010
0.1291
1.1360
0.1133
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0037
0.0014
0.1625
0.0036
0.0135
0.0013
24
Nitrogen
0.0475
0.0180
1.3300
0.0291
0.1129
0.0113
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2.6353
1.0000
45.7024
1.0000
10.0238
1.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Component Splitter:
D-4A
51
Tee:
LOGICAL CONNECTION TEE-102
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Active)
61
306.7 psia Molar:
* Mass: 2.635 lbmole/hr
45.70 lb/hr Std Ideal Liq Volume:
10.02 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 11 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 4
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
52.59
52.59
(psia)
306.7
306.7
438.0
438.0
7597
7597
(lbmole/hr) (lb/hr)
1666 -3.254e+004 37.90
1666 -3.254e+004 37.90
(Btu/hr)
-1.425e+007
-1.425e+007
(barrel/day)
* 7.072e+005
7.072e+005
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-1876
-1876
30
Mass Entropy
(Btu/lb-F)
2.185
2.185
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
35
HHV Mass Basis (Std)
2.274e+004
2.274e+004
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
1.000
1.000
41
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
(Btu/lb)
184.0
---
44
Partial Pressure of CO2
(psia)
0.4298
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48
17.34 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
5.934e-002 1.029 3.155e+004
17.34 5.934e-002 1.029 3.155e+004
9.393
9.393
0.5416
0.5416
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
(ACFM)
123.0
123.0
(lbmole/ft3)
1.124
1.124
Specific Heat
(Btu/lbmole-F)
9.393
9.393
49
Std. Gas Flow
(MMSCFD)
3.982
3.982
50
Std. Ideal Liq. Mass Density
(lb/ft3)
19.49
19.49
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
0.9402
0.9402
53
Watson K
19.04
19.04
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.268
1.268
1.379
1.379
3065
---
0.6811
0.6811
4.592e-002
4.592e-002
7.072e+005
7.072e+005
0.0000
0.0000
(ft3/lbmole)
16.85
16.85
(Btu/lb)
176.7
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
1.869e-002
1.869e-002
1.123e-002
1.123e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 12 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 4 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 7.407
7.407
0.4271
0.4271
6.813
6.813
0.3928
0.3928
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
7.072e+005
7.072e+005
-31.43
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
396.9164
0.9061
6367.6899
0.8382
1456.3209
0.8741
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
32.6197
0.0745
980.8700
0.1291
188.8281
0.1133
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.6138
0.0014
27.0136
0.0036
2.2412
0.0013
38
Nitrogen
7.8919
0.0180
221.0745
0.0291
18.7724
0.0113
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
438.0417
1.0000
7596.6480
1.0000
1666.1625
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Methane
396.9164
0.9061
6367.6899
0.8382
1456.3209
0.8741
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
32.6197
0.0745
980.8700
0.1291
188.8281
0.1133
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6138
0.0014
27.0136
0.0036
2.2412
0.0013
57
Nitrogen
7.8919
0.0180
221.0745
0.0291
18.7724
0.0113
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
438.0417
1.0000
7596.6480
1.0000
1666.1625
1.0000
63
K VALUE
64 65
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 13 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 4 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Component Splitter:
D-4B
LOGICAL CONNECTION
Tee:
TEE-102
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
306.7 psia 438.0 lbmole/hrMass:
37
7597 lb/hr Std Ideal Liq Volume:
1666 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 5
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.0067
0.0067
0.9933
(F)
308.1
308.1
308.1
(psia)
414.7*
414.7
414.7
482.2
3.250
479.0
8686
56.74
8629
602.8
10.75
592.1
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-1.182e+005 19.72 -5.698e+007 590.4*
(barrel/day)
61
-4.404e+004 41.52 -1.431e+005 5243
-1.187e+005 19.58 -5.684e+007 582.2
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 18.01
(lbmole/ft3) (lb/ft3)
2.230
17.46 5.158e-002
Aqueous Phase 18.02 3.126
40.17
0.9005
56.31
(barrel/day)
924.4
269.4
655.0
(Btu/lb)
-6560
-2523
-6587
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 14 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 5 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
(Btu/lb-F)
Vapour Phase
Aqueous Phase
1.095
2.378
1.087
19.63
10.41
19.69
(Btu/lb-F)
1.090
0.5965
1.093
LHV Molar Basis (Std)
(Btu/lbmole)
1959
16
HHV Molar Basis (Std)
(Btu/lbmole)
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
(lbmole/ft3)
1.708e-005
20
CO2 App WT Con
(lbmol/lb)
4.252e-007
21
LHV Mass Basis (Std)
22
Phase Fraction [Vol. Basis]
23
Phase Fraction [Mass Basis]
24
Phase Fraction [Act. Vol. Basis]
25
Mass Exergy
26
Partial Pressure of CO2
27
Cost Based on Flow
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
(psia)
59
True VP at 37.8 C
(psia)
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(Btu/lbmole-F)
(Btu/lb)
1.969e+004 1093 ---
(Btu/lb)
2.892e+005 3.216e+005 1.842e+004 ---
108.8
9.484 1.764e+004 979.2 ---
---
8.726e-006
---
1.550e-007
1.657e+004
0.5265
1.783e-002
1.783e-002
0.9822
6.533e-003
6.533e-003
0.9935
0.2914
0.2914
0.7086
(Btu/lb)
43.83
---
---
(psia)
0.3006
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1.050
1.050
---
(lbmole/ft3)
3.420
1.293
3.458
Specific Heat
(Btu/lbmole-F)
19.63
10.41
19.69
Std. Gas Flow
(MMSCFD)
4.384
2.954e-002
4.354
(lb/ft3)
61.59
22.57
62.30
(USGPS)
0.3184
---
0.3184
(psia)
(Btu/lbmole)
---
0.9759
19.04
19.07
15.22
---
---
---
0.0000
---
---
1.113
1.236
1.112
1.003
1.285
1.187
2.549e+004
(cSt)
---
(lb/ft3)
62.88
(barrel/day) (ft3/lbmole) (Btu/lb)
1.610e-002
---
---
1.048
0.1960
4.626e-002
63.35
590.4
5243
0.9933
0.0000
582.2 1.000
0.4484
19.39
0.3199
1415
---
---
0.0067
0.0067
0.9933
(dyne/cm)
47.97
(Btu/hr-ft-F)
---
2.865e-002
0.3964
---
1.512e-002
0.1768
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
47.97
17.64
8.429
17.71
0.9796
0.4828
0.9828
19.57
8.104
16.59
1.086
0.4642
0.9207
20.83
---
16.30
1.156
---
0.9048
0.9425
---
1.208
---
---
---
---
---
---
5826
5243
582.2
---
---
---
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
0.0067
LIQUID VOLUME FRACTION 0.0000
Page 15 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 5 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
0.0067
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
H2O
479.5977
0.9945
8640.0000
0.9947
592.7991
0.9834
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
2.3879
0.0050
38.3088
0.0044
8.7614
0.0145
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
0.1962
0.0004
5.9010
0.0007
1.1360
0.0019
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.0037
0.0000
0.1625
0.0000
0.0135
0.0000
23
Nitrogen
0.0475
0.0001
1.3300
0.0002
0.1129
0.0002
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
482.2330
1.0000
8685.7024
1.0000
602.8230
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
6.740e-003 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
H2O
0.6311
0.1942
11.3702
0.2004
0.7801
0.0726
35
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Methane
2.3750
0.7308
38.1025
0.6715
8.7142
0.8109
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
0.1961
0.0603
5.8959
0.1039
1.1350
0.1056
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0024
0.0007
0.1037
0.0018
0.0086
0.0008
42
Nitrogen
0.0454
0.0140
1.2719
0.0224
0.1080
0.0101
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
3.2500
1.0000
56.7441
1.0000
10.7460
1.0000
48
Aqueous Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9933 LIQUID VOLUME FRACTION
52
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
H2O
478.9665
1.0000
8628.6298
1.0000
592.0190
0.9999
54
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Methane
0.0129
0.0000
0.2063
0.0000
0.0472
0.0001
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Ethane
0.0002
0.0000
0.0051
0.0000
0.0010
0.0000
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
0.0013
0.0000
0.0588
0.0000
0.0049
0.0000
61
Nitrogen
0.0021
0.0000
0.0581
0.0000
0.0049
0.0000
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Total
478.9830
1.0000
8628.9582
1.0000
592.0770
1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 16 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 5 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.1942
---
0.1942
---
---
14
Oxygen
15
Methane
16
2.722e+004
H2S
---
---
---
---
---
---
2.722e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
259.7
---
259.7
21
Nitrogen
3224
---
3224
---
---
---
22
1.689e+005
Air
---
---
1.689e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Mixer:
LOGICAL CONNECTION
MIX-105 Component Splitter:
30
D-4A
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 414.7 psia
482.2 lbmole/hrMass:
40
8686 lb/hr Std Ideal Liq Volume:
602.8 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 6
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.4952
0.4952
0.5048
(F)
209.1
209.1
209.1
(psia)
414.7*
414.7
414.7
917.6
454.5
463.2
(lbmole/hr) (lb/hr)
1.624e+004
(barrel/day)
(Btu/hr)
2259 -7.753e+004 28.36 -7.115e+007 2196*
(barrel/day)
64
7892
8344
1686
572.5
-3.367e+004 40.01 -1.530e+007 7.337e+005
-1.206e+005 16.92 -5.585e+007 563.0
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.69
(lbmole/ft3)
0.1182
17.37 5.963e-002
Aqueous Phase 18.02 3.294
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 17 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 6 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-4382
-1939
-6693
15
Mass Entropy
(Btu/lb-F)
1.603
2.304
0.9393
16
Heat Capacity
14.54
10.12
18.88
17
Mass Heat Capacity
0.8219
0.5829
1.048
18
LHV Molar Basis (Std)
(Btu/lbmole)
1.711e+005
3.455e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
1.974e+005
3.807e+005
20
HHV Mass Basis (Std)
1.116e+004
2.192e+004
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
---
24
LHV Mass Basis (Std)
(Btu/lb)
9670
25
Phase Fraction [Vol. Basis]
0.7466
0.7466
26
Phase Fraction [Mass Basis]
0.4861
0.4861
27
Phase Fraction [Act. Vol. Basis]
0.9819
0.9819
28
Mass Exergy
(Btu/lb)
109.7
---
29
Partial Pressure of CO2
(psia)
0.5576
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.092 3.318e+004
1.036 3.258e+004
59.34 601.1
1.617 1.763e+004 978.8
---
---
---
---
1.994e-005
---
3.361e-007
1.989e+004
---
8.975e-002 0.2534 0.5139 1.812e-002 ---
(ACFM)
127.0
127.0
---
(lbmole/ft3)
1.736
1.152
3.458
Specific Heat
(Btu/lbmole-F)
14.54
10.12
18.88
Std. Gas Flow
(MMSCFD)
8.341
4.131
4.210
(lb/ft3)
30.72
20.00
62.30
(USGPS)
0.2922
---
0.2922
(psia)
(Btu/lbmole)
---
0.9690
19.04
19.04
9.822
---
---
---
0.0000
---
---
1.158
1.244
1.118
1.090
1.309
1.173
1.689e+004
1.754e-002
---
---
0.8425
0.2986
(cSt)
---
(lb/ft3)
31.61
4.598e-002
63.35
2196
7.337e+005
563.0
(barrel/day) (ft3/lbmole) (Btu/lb)
0.5048
0.0000
1.000
8.458
16.77
0.3036
954.4
---
---
0.4952
0.4952
0.5048
(dyne/cm)
58.91
(Btu/hr-ft-F)
---
2.577e-002
0.3929
---
1.398e-002
0.2838
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
58.91
12.56
8.137
16.89
0.7096
0.4686
0.9376
13.35
7.735
16.09
0.7543
0.4454
0.8930
---
---
15.48
---
---
0.8595
---
---
1.219
---
---
---
---
---
7.342e+005 -23.56
7.337e+005 ---
--563.0 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 18 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 6 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.4952
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
479.5977
0.5226
8640.0000
0.5321
592.7991
0.2624
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
396.9164
0.4325
6367.6899
0.3922
1456.3209
0.6447
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
32.6197
0.0355
980.8700
0.0604
188.8281
0.0836
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6138
0.0007
27.0136
0.0017
2.2412
0.0010
24
Nitrogen
7.8919
0.0086
221.0745
0.0136
18.7724
0.0083
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
917.6394
1.0000
1.0000
2258.9617
1.0000
16236.6480
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.4952 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
16.4179
0.0361
295.7705
0.0375
20.2931
0.0120
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
396.9142
0.8734
6367.6555
0.8068
1456.3130
0.8635
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
32.6196
0.0718
980.8696
0.1243
188.8280
0.1120
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6110
0.0013
26.8902
0.0034
2.2309
0.0013
43
Nitrogen
7.8900
0.0174
221.0226
0.0280
18.7680
0.0111
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
454.4528
1.0000
7892.2084
1.0000
1686.4330
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.5048 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
463.1797
1.0000
8344.2295
1.0000
572.5060
1.0000
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0021
0.0000
0.0344
0.0000
0.0079
0.0000
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0028
0.0000
0.1234
0.0000
0.0102
0.0000
62
Nitrogen
0.0019
0.0000
0.0519
0.0000
0.0044
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
463.1866
1.0000
8344.4396
1.0000
572.5286
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 19 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 6 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
CO
13
H2O
HEAVY ---
3.613e-002
14
Oxygen
15
Methane
16
LIGHT -----
3.613e-002
---
1.885e+005
H2S
---
---
---
---
---
---
---
---
1.885e+005 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
222.1
---
222.1
21
Nitrogen
4338
---
4338
---
---
---
22
2.473e+006
Air
---
---
2.473e+006
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Mixer:
LOGICAL CONNECTION
MIX-105 Component Splitter:
30
D-4B
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 414.7 psia
917.6 lbmole/hrMass:
40
1.624e+004 lb/hrStd Ideal Liq Volume:
2259 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 7
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.3364
0.3364
0.6636
(F)
239.7
239.7
239.7
(psia)
414.7
414.7
414.7
1400
471.0
(lbmole/hr) (lb/hr)
(Btu/hr)
2.492e+004 2862 -9.153e+004 25.43 -1.281e+008 2587*
(barrel/day)
64
8188 1714 -3.540e+004 40.53 -1.667e+007 7.603e+005
928.9 1.673e+004 1148 -1.200e+005 17.77 -1.115e+008 1129
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.80
(lbmole/ft3)
0.1631
17.39 5.678e-002
Aqueous Phase 18.02 3.244
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 20 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 7 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
1.128e+005
3.354e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
1.362e+005
3.701e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
---
24
LHV Mass Basis (Std)
(Btu/lb)
6338
25
Phase Fraction [Vol. Basis]
0.5988
0.5988
26
Phase Fraction [Mass Basis]
0.3285
0.3285
27
Phase Fraction [Act. Vol. Basis]
0.9666
0.9666
28
Mass Exergy
(Btu/lb)
85.37
---
29
Partial Pressure of CO2
(psia)
0.5393
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
2.904 3.668e+004
0.9871 3.546e+004
58.44 1224
(Btu/lb)
-5141
-2036
-6660
(Btu/lb-F)
1.428
2.331
0.9863
16.10
10.25
19.07
0.9043
0.5893
1.058
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
7651
2.129e+004
3.015 1.763e+004 978.8
---
---
---
---
1.743e-005
---
2.983e-007
1.929e+004
---
0.1674 0.4012 0.6715 3.337e-002 ---
(ACFM)
138.3
138.3
---
(lbmole/ft3)
2.091
1.175
3.458
Specific Heat
(Btu/lbmole-F)
16.10
10.25
19.07
Std. Gas Flow
(MMSCFD)
12.72
4.281
8.444
(lb/ft3)
37.23
20.43
62.30
(USGPS)
0.5950
---
0.5950
(psia)
(Btu/lbmole)
---
0.9732
19.04
19.04
11.17
---
---
---
0.0000
---
---
1.141
1.240
1.116
1.053
1.297
1.177
1.993e+004
---
---
0.9107
0.2562
(cSt)
---
(lb/ft3)
41.18
4.604e-002
2587
7.603e+005
(barrel/day)
1.703e-002
63.36 1129
0.6636
0.0000
1.000
(ft3/lbmole)
6.130
17.61
0.3083
(Btu/lb)
1119
---
---
0.3364
0.3364
0.6636
(dyne/cm)
55.65
(Btu/hr-ft-F)
---
2.692e-002
0.3962
---
1.440e-002
0.2398
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
55.65
14.11
8.260
17.08
0.7928
0.4751
0.9482
15.29
7.897
16.20
0.8589
0.4542
0.8991
---
---
15.39
---
---
0.8544
---
---
1.239
---
---
---
---
---
7.614e+005 ---
7.603e+005 ---
--1129 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 21 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 7 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
959.1953
0.6852
17
Oxygen
0.0000
0.0000
18
Methane
399.3043
19
H2S
20
Hydrogen
21
Ethane
22
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.3364
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.6934
1185.5983
0.4143
0.0000
0.0000
0.0000
0.0000
0.2852
6405.9987
0.2570
1465.0823
0.5119
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0234
986.7710
0.0396
189.9641
0.0664
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6175
0.0004
27.1761
0.0011
2.2546
0.0008
24
Nitrogen
7.9393
0.0057
222.4045
0.0089
18.8854
0.0066
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1399.8723
1.0000
1.0000
2861.7846
1.0000
17280.0000
24922.3504
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.3364 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
30.3074
0.0644
545.9916
0.0667
37.4610
0.0219
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
399.2963
0.8478
6405.8704
0.7824
1465.0529
0.8550
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
32.8158
0.0697
986.7690
0.1205
189.9637
0.1109
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6125
0.0013
26.9565
0.0033
2.2364
0.0013
43
Nitrogen
7.9355
0.0168
222.2980
0.0271
18.8763
0.0110
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
470.9676
1.0000
8187.8855
1.0000
1713.5904
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
53
CO
0.0000
0.0000
54
H2O
928.8879
1.0000
55
Oxygen
0.0000
0.0000
56
Methane
0.0080
57
H2S
58
MASS FLOW (lb/hr) 0.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.6636 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1148.1372
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.1284
0.0000
0.0294
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0001
0.0000
0.0019
0.0000
0.0004
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0050
0.0000
0.2197
0.0000
0.0182
0.0000
62
Nitrogen
0.0038
0.0000
0.1065
0.0000
0.0090
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
928.9047
1.0000
1.0000
1148.1942
1.0000
16734.0084
16734.4649
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 22 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 7 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
CO
13
H2O Oxygen
15
Methane
---
---
---
6.435e-002
---
9.843e+004
H2S
HEAVY ---
6.435e-002
14
16
LIGHT ---
---
---
---
---
---
---
9.843e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
242.0
---
242.0
21
Nitrogen
4116
---
4116
---
---
---
22
9.999e+005
Air
---
---
9.999e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Mixer:
MIX-106 Mixer:
LOGICAL CONNECTION MIX-105
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
414.7 psia 1400 lbmole/hrMass:
40
2.492e+004 lb/hrStd Ideal Liq Volume:
2862 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 8
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
310.0*
310.0
(psia)
364.7
364.7
(lbmole/hr) (lb/hr)
(Btu/hr)
1918 3.456e+004 2371 -1.186e+005 19.63 -2.276e+008 2332*
(barrel/day)
64
1918 3.456e+004 2371 -1.186e+005 19.63 -2.276e+008 2332
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Aqueous Phase 18.02
18.02
3.122
3.122
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 23 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 8 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
(lb/ft3)
Aqueous Phase 56.24
56.24
(barrel/day)
2627
2627
(Btu/lb)
-6585
-6585
(Btu/lb-F)
1.089
1.089
19.72
19.72
(Btu/lbmole-F) (Btu/lb-F)
1.095
1.095
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
19
HHV Molar Basis (Std)
(Btu/lbmole)
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
26
Phase Fraction [Mass Basis]
0.0000
1.000
27
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
28
Mass Exergy
(Btu/lb)
43.03
---
29
Partial Pressure of CO2
(psia)
0.0000
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
---
---
39
User Property
---
---
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.72
19.72
Std. Gas Flow
(MMSCFD)
17.44
17.44
(lb/ft3)
62.30
62.30
(USGPS)
1.277 1.414e-002
(psia)
(Btu/lbmole)
1.277 1.414e-002
0.0000
---
1.112
1.112
1.188
1.188
1.445e+004
---
(cSt)
0.1949
0.1949
(lb/ft3)
63.35
63.35
(barrel/day)
2332
2332
1.000
1.000
(ft3/lbmole)
0.3203
0.3203
(Btu/lb)
802.3
---
0.0000
1.0000
(dyne/cm)
47.75
47.75
(Btu/hr-ft-F)
0.3962
0.3962
0.1755
0.1755
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
17.73
17.73
0.9844
0.9844
16.60
16.60
0.9216
0.9216
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
2332
2332
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 24 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 8 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
1918.3906
1.0000
17
Oxygen
0.0000
0.0000
18
Methane
0.0000
19
H2S
20
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2371.1965
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1918.3906
1.0000
1.0000
2371.1965
1.0000
30
0.0000
Vapour Fraction
34560.0000
34560.0000
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
34
CO
0.0000
0.0000
35
H2O
1918.3906
1.0000
36
Oxygen
0.0000
0.0000
37
Methane
0.0000
38
H2S
39
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2371.1965
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
1918.3906
1.0000
1.0000
2371.1965
1.0000
49
34560.0000
34560.0000
K VALUE
50 51
0.0000
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
0.0000
---
0.0000
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 25 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 8 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Tee:
TEE-103 LNG:
LOGICAL CONNECTION LNG-101
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
364.7 psia 1918 lbmole/hrMass:
23
3.456e+004 lb/hrStd Ideal Liq Volume:
2371 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 9
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
310.0
310.0
(psia)
364.7
364.7
(lbmole/hr) (lb/hr)
(Btu/hr)
959.2 * 1.728e+004
1186 -1.186e+005 19.63 -1.138e+008 1166*
(barrel/day)
47
959.2 1.728e+004 1186 -1.186e+005 19.63 -1.138e+008 1166
PROPERTIES
48 49
Overall
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
55
Mass Entropy
56
Heat Capacity
57
Mass Heat Capacity
58
(lbmole/ft3) (lb/ft3)
Aqueous Phase 18.02
18.02
3.122
3.122
56.24
56.24
(barrel/day)
1313
1313
(Btu/lb)
-6585
-6585
(Btu/lb-F)
1.089
1.089
19.72
19.72
(Btu/lbmole-F) (Btu/lb-F)
1.095
1.095
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
66
Phase Fraction [Mass Basis]
0.0000
1.000
67
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
68
Mass Exergy
43.03
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 26 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 9 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Aqueous Phase
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
---
---
22
User Property
---
---
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
(psia)
0.0000
---
(Cost/s)
0.0000
0.0000
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.72
19.72
Std. Gas Flow
(MMSCFD)
8.719
8.719
(lb/ft3)
62.30
62.30
(USGPS)
0.6385
0.6385
1.414e-002
(psia)
(Btu/lbmole)
1.414e-002
0.0000
---
1.112
1.112
1.188
1.188
1.445e+004
---
(cSt)
0.1949
0.1949
(lb/ft3)
63.35
63.35
(barrel/day)
1166
1166
1.000
1.000
(ft3/lbmole)
0.3203
0.3203
(Btu/lb)
802.3
---
0.0000
1.0000
(dyne/cm)
47.75
47.75
(Btu/hr-ft-F)
0.3962
0.3962
0.1755
0.1755
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
17.73
17.73
0.9844
0.9844
16.60
16.60
0.9216
0.9216
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
1166
1166
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
54
CO
0.0000
0.0000
55
H2O
959.1953
1.0000
56
Oxygen
0.0000
0.0000
57
Methane
0.0000
58
H2S
59
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1185.5983
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
959.1953
1.0000
1.0000
1185.5983
69
Aspen Technology Inc. Licensed to: LEGENDS
0.0000
Vapour Fraction
17280.0000
17280.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 27 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 9 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Aqueous Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
959.1953
1.0000
17
Oxygen
0.0000
0.0000
18
Methane
0.0000
19
H2S
20
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
0.0000
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1185.5983
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
959.1953
1.0000
1.0000
1185.5983
1.0000
17280.0000
17280.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
0.0000
---
0.0000
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Mixer:
MIX-106 Tee:
51
LOGICAL CONNECTION TEE-103
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Active)
61
364.7 psia Molar:
959.2 lbmole/hrMass:
1.728e+004 *lb/hrStd Ideal Liq Volume:
1186 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 28 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 10
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
310.0
310.0
(psia)
364.7
364.7
(lbmole/hr) (lb/hr)
(Btu/hr)
959.2 1.728e+004 1186 -1.186e+005 19.63 -1.138e+008 1166*
(barrel/day)
22
959.2 1.728e+004 1186 -1.186e+005 19.63 -1.138e+008 1166
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
30
Mass Entropy
31
Heat Capacity
32
Mass Heat Capacity
33
(lbmole/ft3) (lb/ft3)
Aqueous Phase 18.02
18.02
3.122
3.122
56.24
56.24
(barrel/day)
1313
1313
(Btu/lb)
-6585
-6585
(Btu/lb-F)
1.089
1.089
19.72
19.72
(Btu/lbmole-F) (Btu/lb-F)
1.095
1.095
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
34
HHV Molar Basis (Std)
(Btu/lbmole)
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
43.03
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
---
---
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.72
19.72
Std. Gas Flow
(MMSCFD)
8.719
8.719
Licensed to: LEGENDS
(lb/ft3)
62.30
62.30
(USGPS)
0.6385
0.6385
1.414e-002
(psia)
(Btu/lbmole)
1.414e-002
0.0000
---
1.112
1.112
1.188
1.188
1.445e+004
---
(cSt)
0.1949
0.1949
(lb/ft3)
63.35
63.35
(barrel/day)
1166
1166
1.000
1.000
(ft3/lbmole)
0.3203
0.3203
(Btu/lb)
802.3
---
0.0000
1.0000
(dyne/cm)
47.75
47.75
(Btu/hr-ft-F)
0.3962
0.3962
0.1755
0.1755
(cP)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 29 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 10 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Aqueous Phase 17.73
17.73
0.9844
0.9844
16.60
16.60
0.9216
0.9216
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
1166
1166
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
29
CO
0.0000
0.0000
30
H2O
959.1953
1.0000
31
Oxygen
0.0000
0.0000
32
Methane
0.0000
33
H2S
34
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1185.5983
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
959.1953
1.0000
1.0000
1185.5983
1.0000
44
0.0000
Vapour Fraction
17280.0000
17280.0000
Aqueous Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
48
CO
0.0000
0.0000
49
H2O
959.1953
1.0000
50
Oxygen
0.0000
0.0000
51
Methane
0.0000
52
H2S
53
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1185.5983
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
959.1953
1.0000
1.0000
1185.5983
1.0000
63
17280.0000
17280.0000
K VALUE
64 65
0.0000
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
0.0000
---
0.0000
---
---
68 69
Oxygen
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 30 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 10 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Tee:
LOGICAL CONNECTION
TEE-106 Tee:
TEE-103
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
364.7 psia 959.2 lbmole/hrMass:
37
1.728e+004 lb/hrStd Ideal Liq Volume:
1186 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 11
46 47 48
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.2092
0.2092
0.7908
(F)
262.1
262.1
262.1
(psia)
364.7
364.7
364.7
2359
493.5
(lbmole/hr) (lb/hr)
(Btu/hr)
4.220e+004 4047 -1.025e+005 23.15 -2.419e+008 3664*
(barrel/day)
61
8594 1741 -3.824e+004 41.18 -1.887e+007 7.965e+005
1866 3.361e+004 2306 -1.196e+005 18.38 -2.230e+008 2268
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
0.2179 3.898 4.628e+004 -5732
17.41 4.817e-002 0.8388 4.380e+004 -2196
Aqueous Phase 18.02 3.206 57.75 2488 -6637
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 31 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 11 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
3.201e+005
16
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
3.540e+005
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
(lbmole/ft3)
20
CO2 App WT Con
(lbmol/lb)
---
21
LHV Mass Basis (Std)
(Btu/lb)
3743
22
Phase Fraction [Vol. Basis]
0.4303
0.4303
23
Phase Fraction [Mass Basis]
0.2036
0.2036
24
Phase Fraction [Act. Vol. Basis]
0.9463
0.9463
25
Mass Exergy
(Btu/lb)
65.71
---
26
Partial Pressure of CO2
(psia)
0.4503
---
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
(psia)
59
True VP at 37.8 C
(psia)
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.294
2.365
1.020
17.36
10.25
19.24
0.9706
0.5888
1.068
4919
2.033e+004
3.985 1.764e+004 978.9
---
---
---
---
1.394e-005
---
2.414e-007
1.838e+004
---
0.2212 0.5697 0.7964 5.375e-002 ---
(ACFM)
170.8
170.8
---
(lbmole/ft3)
2.492
1.211
3.458
Specific Heat
(Btu/lbmole-F)
17.36
10.25
19.24
Std. Gas Flow
(MMSCFD)
21.44
4.486
16.96
(lb/ft3)
44.57
21.10
62.30
(USGPS)
1.209
---
---
0.9776
19.04
19.04
12.33
---
---
---
0.0000
---
---
1.129
1.240
1.115
1.030
1.287
1.180
(psia)
(Btu/lbmole)
2.234e+004
---
---
1.086
0.2323
(cSt)
---
(lb/ft3)
49.23
4.612e-002
3664
7.965e+005
(barrel/day)
1.209 1.469e-002
63.35 2268
0.7908
0.0000
1.000
(ft3/lbmole)
4.590
20.76
0.3119
(Btu/lb)
1249
---
---
0.2092
0.2092
0.7908
(dyne/cm)
53.19
(Btu/hr-ft-F)
---
2.736e-002
0.3973
---
1.458e-002
0.2149
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
53.19
15.38
8.268
17.26
0.8596
0.4748
0.9580
16.87
7.965
16.30
0.9428
0.4574
0.9050
---
---
14.67
---
---
0.8142
---
---
1.312
---
---
---
---
---
7.988e+005 ---
7.965e+005 ---
62
--2268 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
0.2092
LIQUID VOLUME FRACTION 0.0000
Page 32 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 11 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
0.2092
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
H2O
1918.3906
0.8132
0.8189
2371.1965
0.5859
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
399.3043
0.1693
6405.9987
0.1518
1465.0823
0.3620
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
23
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
34560.0000
42202.3504
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
H2O
52.8597
0.1071
952.2721
0.1108
65.3364
0.0375
35
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Methane
399.2831
0.8091
6405.6590
0.7454
1465.0046
0.8413
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
32.8157
0.0665
986.7648
0.1148
189.9629
0.1091
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.6094
0.0012
26.8191
0.0031
2.2250
0.0013
42
Nitrogen
7.9325
0.0161
222.2130
0.0259
18.8691
0.0108
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
493.5004
1.0000
8593.7281
1.0000
1741.3979
1.0000
48
Aqueous Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
52
CO
0.0000
0.0000
53
H2O
1865.5310
1.0000
54
Oxygen
0.0000
0.0000
55
Methane
0.0212
56
H2S
57
MASS FLOW (lb/hr) 0.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7908 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2305.8602
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.3398
0.0000
0.0777
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Ethane
0.0002
0.0000
0.0062
0.0000
0.0012
0.0000
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
0.0081
0.0000
0.3570
0.0000
0.0296
0.0000
61
Nitrogen
0.0068
0.0000
0.1915
0.0000
0.0163
0.0000
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Total
1865.5673
1.0000
1.0000
2305.9849
1.0000
33607.7279
33608.6223
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 33 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 11 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.1071
---
0.1071
---
---
14
Oxygen
15
Methane
16
7.127e+004
H2S
---
---
---
---
---
---
7.127e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
284.0
---
284.0
21
Nitrogen
4387
---
4387
---
---
---
22
6.040e+005
Air
---
---
6.040e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO Component Splitter:
PRODUCT FROM
LOGICAL CONNECTION
V-080 COBALTO MOLIBDENO Mixer:
MIX-106
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
364.7 psia 2359 lbmole/hrMass:
40
4.220e+004 lb/hrStd Ideal Liq Volume:
4047 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 12
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.2092
0.2092
0.7908
(F)
262.1
262.1
262.1
(psia)
364.7*
364.7
364.7
2359
493.5
(lbmole/hr) (lb/hr)
(Btu/hr)
4.220e+004 4047 -1.025e+005 23.15 -2.419e+008 3664*
(barrel/day)
64
8594 1741 -3.824e+004 41.18 -1.887e+007 7.965e+005
1866 3.361e+004 2306 -1.196e+005 18.38 -2.230e+008 2268
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3)
0.2179
17.41 4.817e-002
Aqueous Phase 18.02 3.206
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 34 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 12 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
3.201e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
3.540e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
---
24
LHV Mass Basis (Std)
(Btu/lb)
3743
25
Phase Fraction [Vol. Basis]
0.4303
0.4303
26
Phase Fraction [Mass Basis]
0.2036
0.2036
27
Phase Fraction [Act. Vol. Basis]
0.9463
0.9463
28
Mass Exergy
(Btu/lb)
65.71
---
29
Partial Pressure of CO2
(psia)
0.4503
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
3.898 4.628e+004
0.8388 4.380e+004
57.75 2488
(Btu/lb)
-5732
-2196
-6637
(Btu/lb-F)
1.294
2.365
1.020
17.36
10.25
19.24
0.9706
0.5888
1.068
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
4919
2.033e+004
3.985 1.764e+004 978.9
---
---
---
---
1.394e-005
---
2.414e-007
1.838e+004
---
0.2212 0.5697 0.7964 5.375e-002 ---
(ACFM)
170.8
170.8
---
(lbmole/ft3)
2.492
1.211
3.458
Specific Heat
(Btu/lbmole-F)
17.36
10.25
19.24
Std. Gas Flow
(MMSCFD)
21.44
4.486
16.96
(lb/ft3)
44.57
21.10
62.30
(USGPS)
1.209
---
---
0.9776
19.04
19.04
12.33
---
---
---
0.0000
---
---
1.129
1.240
1.115
1.030
1.287
1.180
(psia)
(Btu/lbmole)
2.234e+004
---
---
1.086
0.2323
(cSt)
---
(lb/ft3)
49.23
4.612e-002
3664
7.965e+005
(barrel/day)
1.209 1.469e-002
63.35 2268
0.7908
0.0000
1.000
(ft3/lbmole)
4.590
20.76
0.3119
(Btu/lb)
1249
---
---
0.2092
0.2092
0.7908
(dyne/cm)
53.19
(Btu/hr-ft-F)
---
2.736e-002
0.3973
---
1.458e-002
0.2149
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
53.19
15.38
8.268
17.26
0.8596
0.4748
0.9580
16.87
7.965
16.30
0.9428
0.4574
0.9050
---
---
14.67
---
---
0.8142
---
---
1.312
---
---
---
---
---
7.988e+005 ---
7.965e+005 ---
--2268 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 35 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 12 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
1918.3906
0.8132
17
Oxygen
0.0000
0.0000
18
Methane
399.3043
19
H2S
20
Hydrogen
21
Ethane
22
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2371.1965
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6405.9987
0.1518
1465.0823
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
24
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
34560.0000
42202.3504
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
52.8597
0.1071
952.2721
0.1108
65.3364
0.0375
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
399.2831
0.8091
6405.6590
0.7454
1465.0046
0.8413
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
32.8157
0.0665
986.7648
0.1148
189.9629
0.1091
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6094
0.0012
26.8191
0.0031
2.2250
0.0013
43
Nitrogen
7.9325
0.0161
222.2130
0.0259
18.8691
0.0108
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
493.5004
1.0000
8593.7281
1.0000
1741.3979
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
53
CO
0.0000
0.0000
54
H2O
1865.5310
1.0000
55
Oxygen
0.0000
0.0000
56
Methane
0.0212
57
H2S
58
MASS FLOW (lb/hr) 0.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7908 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2305.8602
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.3398
0.0000
0.0777
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0002
0.0000
0.0062
0.0000
0.0012
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0081
0.0000
0.3570
0.0000
0.0296
0.0000
62
Nitrogen
0.0068
0.0000
0.1915
0.0000
0.0163
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
1865.5673
1.0000
1.0000
2305.9849
1.0000
33607.7279
33608.6223
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 36 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 12 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.1071
---
0.1071
---
---
14
Oxygen
15
Methane
16
7.127e+004
H2S
---
---
---
---
---
---
7.127e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
284.0
---
284.0
21
Nitrogen
4387
---
4387
---
---
---
22
6.040e+005
Air
---
---
6.040e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Component Splitter:
V-078 OXIDO DE ZINC Component Splitter:
30
LOGICAL CONNECTION
V-080 COBALTO MOLIBDENO
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
2359 lbmole/hrMass:
40
4047 barrel/day
User Variables
41 42
NOTES
43 44
4.220e+004 lb/hrStd Ideal Liq Volume:
29285
45 46 47
(Last modified Wed Dec 12, 2018, 19:27)
48 49
Description
50 51 52
Material Stream: 13
53 54 55
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
56 57
Overall
58
Vapour / Phase Fraction
59
Temperature:
60
Pressure:
61
Molar Flow
62
Mass Flow
63
Std Ideal Liq Vol Flow
(barrel/day)
64
Molar Enthalpy
(Btu/lbmole)
65
Molar Entropy
(Btu/lbmole-F)
66
Heat Flow
67
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.9586
0.9586
0.0414
(F)
414.1*
414.1
414.1
(psia)
364.7*
364.7
364.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-8.867e+004
-8.747e+004
0.0000 -1.165e+005
39.79
40.55
22.23
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 37 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 13 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Molecular Weight
13
Molar Density
14
Mass Density
15
Act. Volume Flow
16 17 18
Heat Capacity
19
Mass Heat Capacity
20
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.985e+004
21
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
9.104e+004
22
HHV Mass Basis (Std)
23
CO2 Loading
24
CO2 App ML Con
25
CO2 App WT Con
26
LHV Mass Basis (Std)
27 28 29
Phase Fraction [Act. Vol. Basis]
30
Mass Exergy
31
Partial Pressure of CO2
32
Cost Based on Flow
33
Act. Gas Flow
34
Avg. Liq. Density
35
17.89 (lbmole/ft3) (lb/ft3)
4.382e-002
17.88 4.203e-002
Aqueous Phase 18.02 2.914
0.7840
0.7517
52.50
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-4957
-4891
-6466
Mass Entropy
(Btu/lb-F)
2.224
2.267
1.234
10.24
9.751
21.51
0.5723
0.5453
1.194
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
11.46 1.764e+004
4919
5090
979.4
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
3743
3906
0.6362
Phase Fraction [Vol. Basis]
0.9702
0.9702
2.984e-002
Phase Fraction [Mass Basis]
0.9583
0.9583
4.170e-002
---
---
---
342.1
---
---
(Btu/lb) (psia)
9.957e-002
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
0.0000
0.0000
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
10.24
9.751
21.51
36
Std. Gas Flow
(MMSCFD)
0.0000
37
Std. Ideal Liq. Mass Density
38
Act. Liq. Flow
39
Z Factor
40
Watson K
41
User Property
42
Partial Pressure of H2S
43
Cp/(Cp - R)
44
Cp/Cv
45
Heat of Vap.
46
Kinematic Viscosity
47
Liq. Mass Density (Std. Cond)
48
Liq. Vol. Flow (Std. Cond)
49
Liquid Fraction
50
Molar Volume
51
Mass Heat of Vap.
52
Phase Fraction [Molar Basis]
53
Surface Tension
54
Thermal Conductivity
55
Viscosity
56
Cv (Semi-Ideal)
57
Mass Cv (Semi-Ideal)
58
Cv
59
Mass Cv
60
Cv (Ent. Method)
61
Mass Cv (Ent. Method)
62
Cp/Cv (Ent. Method)
63
Reid VP at 37.8 C
(psia)
64
True VP at 37.8 C
(psia)
65 66
0.0000
0.0000
(lb/ft3)
44.57
44.03
62.30
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
0.9253
19.04
19.04
17.57
---
---
---
0.0000
---
---
1.241
1.256
1.102
1.334
1.378
1.214
2.234e+004 ---
(Btu/lb)
---
---
1.140
0.1497
49.23
48.70
63.35
0.0000
0.0000
0.0000
4.141e-002 (ft3/lbmole)
1.335e-002
22.82
0.0000
1.000
23.79
0.3432
1249
---
---
0.9586
0.9586
0.0414
(dyne/cm)
35.00
(Btu/hr-ft-F)
---
2.459e-002
0.3785
---
1.372e-002
0.1259
(cP) (Btu/lbmole-F)
---
35.00
8.252
7.765
19.52
0.4613
0.4342
1.084
7.673
7.078
17.72
0.4289
0.3957
0.9835
---
---
15.78
---
---
0.8758
---
---
1.363
---
---
---
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-20.24
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 38 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 13 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.8132
0.0000
0.8189
0.0000
0.5859
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.1693
0.0000
0.1518
0.0000
0.3620
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0139
0.0000
0.0234
0.0000
0.0469
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0003
0.0000
0.0006
0.0000
0.0006
24
Nitrogen
0.0000
0.0034
0.0000
0.0053
0.0000
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.8051
0.0000
0.8110
0.0000
0.5731
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.1766
0.0000
0.1584
0.0000
0.3731
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0145
0.0000
0.0244
0.0000
0.0484
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0003
0.0000
0.0007
0.0000
0.0006
43
Nitrogen
0.0000
0.0035
0.0000
0.0055
0.0000
0.0048
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
4.141e-002 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
0.0000
1.0000
0.0000
1.0000
0.0000
0.9999
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 39 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 13 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.8052
---
0.8052
14
Oxygen
---
---
---
15
Methane
5547
---
5547
---
---
---
---
---
16
H2S
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
244.5
---
244.5
21
Nitrogen
1872
---
1872
---
---
---
22
1.872e+004
Air
---
---
1.872e+004
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Component Splitter:
30
LOGICAL CONNECTION
V-080 COBALTO MOLIBDENO
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
0.0000 lbmole/hrMass:
40
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 14
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.2092
0.2092
0.7908
(F)
262.1
262.1
262.1
(psia)
364.7*
364.7
364.7
2359
493.5
(lbmole/hr) (lb/hr)
(Btu/hr)
4.220e+004 4047 -1.025e+005 23.15 -2.419e+008 3664*
(barrel/day)
64
8594 1741 -3.824e+004 41.18 -1.887e+007 7.965e+005
1866 3.361e+004 2306 -1.196e+005 18.38 -2.230e+008 2268
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3)
0.2179
17.41 4.817e-002
Aqueous Phase 18.02 3.206
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 40 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 14 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
3.201e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
3.540e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
---
24
LHV Mass Basis (Std)
(Btu/lb)
3743
25
Phase Fraction [Vol. Basis]
0.4303
0.4303
26
Phase Fraction [Mass Basis]
0.2036
0.2036
27
Phase Fraction [Act. Vol. Basis]
0.9463
0.9463
28
Mass Exergy
(Btu/lb)
65.71
---
29
Partial Pressure of CO2
(psia)
0.4503
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
3.898 4.628e+004
0.8388 4.380e+004
57.75 2488
(Btu/lb)
-5732
-2196
-6637
(Btu/lb-F)
1.294
2.365
1.020
17.36
10.25
19.24
0.9706
0.5888
1.068
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
4919
2.033e+004
3.985 1.764e+004 978.9
---
---
---
---
1.394e-005
---
2.414e-007
1.838e+004
---
0.2212 0.5697 0.7964 5.375e-002 ---
(ACFM)
170.8
170.8
---
(lbmole/ft3)
2.492
1.211
3.458
Specific Heat
(Btu/lbmole-F)
17.36
10.25
19.24
Std. Gas Flow
(MMSCFD)
21.44
4.486
16.96
(lb/ft3)
44.57
21.10
62.30
(USGPS)
1.209
---
---
0.9776
19.04
19.04
12.33
---
---
---
0.0000
---
---
1.129
1.240
1.115
1.030
1.287
1.180
(psia)
(Btu/lbmole)
2.234e+004
---
---
1.086
0.2323
(cSt)
---
(lb/ft3)
49.23
4.612e-002
3664
7.965e+005
(barrel/day)
1.209 1.469e-002
63.35 2268
0.7908
0.0000
1.000
(ft3/lbmole)
4.590
20.76
0.3119
(Btu/lb)
1249
---
---
0.2092
0.2092
0.7908
(dyne/cm)
53.19
(Btu/hr-ft-F)
---
2.736e-002
0.3973
---
1.458e-002
0.2149
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
53.19
15.38
8.268
17.26
0.8596
0.4748
0.9580
16.87
7.965
16.30
0.9428
0.4574
0.9050
---
---
14.67
---
---
0.8142
---
---
1.312
---
---
---
---
---
7.988e+005 ---
7.965e+005 ---
--2268 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 41 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 14 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
1918.3906
0.8132
17
Oxygen
0.0000
0.0000
18
Methane
399.3043
19
H2S
20
Hydrogen
21
Ethane
22
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2371.1965
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6405.9987
0.1518
1465.0823
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
24
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
34560.0000
42202.3504
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
52.8597
0.1071
952.2721
0.1108
65.3364
0.0375
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
399.2831
0.8091
6405.6590
0.7454
1465.0046
0.8413
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
32.8157
0.0665
986.7648
0.1148
189.9629
0.1091
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6094
0.0012
26.8191
0.0031
2.2250
0.0013
43
Nitrogen
7.9325
0.0161
222.2130
0.0259
18.8691
0.0108
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
493.5004
1.0000
8593.7281
1.0000
1741.3979
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
53
CO
0.0000
0.0000
54
H2O
1865.5310
1.0000
55
Oxygen
0.0000
0.0000
56
Methane
0.0212
57
H2S
58
MASS FLOW (lb/hr) 0.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7908 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2305.8602
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.3398
0.0000
0.0777
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0002
0.0000
0.0062
0.0000
0.0012
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0081
0.0000
0.3570
0.0000
0.0296
0.0000
62
Nitrogen
0.0068
0.0000
0.1915
0.0000
0.0163
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
1865.5673
1.0000
1.0000
2305.9849
1.0000
33607.7279
33608.6223
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 42 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 14 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.1071
---
0.1071
---
---
14
Oxygen
15
Methane
16
7.127e+004
H2S
---
---
---
---
---
---
7.127e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
284.0
---
284.0
21
Nitrogen
4387
---
4387
---
---
---
22
6.040e+005
Air
---
---
6.040e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Component Splitter:
V-079 OXIDO DE ZINC Component Splitter:
30
LOGICAL CONNECTION
V-078 OXIDO DE ZINC
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
2359 lbmole/hrMass:
40
4047 barrel/day
User Variables
41 42
NOTES
43 44
4.220e+004 lb/hrStd Ideal Liq Volume:
29285
45 46 47
(Last modified Mon Dec 17, 2018, 15:01)
48 49
Description
50 51 52
Material Stream: 15
53 54 55
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
56 57
Overall
58
Vapour / Phase Fraction
59
Temperature:
60
Pressure:
61
Molar Flow
62
Mass Flow
63
Std Ideal Liq Vol Flow
(barrel/day)
64
Molar Enthalpy
(Btu/lbmole)
65
Molar Entropy
(Btu/lbmole-F)
66
Heat Flow
67
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.9586
0.9586
0.0414
(F)
414.1*
414.1
414.1
(psia)
364.7*
364.7
364.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-8.867e+004
-8.747e+004
0.0000 -1.165e+005
39.79
40.55
22.23
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 43 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 15 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Molecular Weight
13
Molar Density
14
Mass Density
15
Act. Volume Flow
16 17 18
Heat Capacity
19
Mass Heat Capacity
20
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.985e+004
21
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
9.104e+004
22
HHV Mass Basis (Std)
23
CO2 Loading
24
CO2 App ML Con
25
CO2 App WT Con
26
LHV Mass Basis (Std)
27 28 29
Phase Fraction [Act. Vol. Basis]
30
Mass Exergy
31
Partial Pressure of CO2
32
Cost Based on Flow
33
Act. Gas Flow
34
Avg. Liq. Density
35
17.89 (lbmole/ft3) (lb/ft3)
4.382e-002
17.88 4.203e-002
Aqueous Phase 18.02 2.914
0.7840
0.7517
52.50
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-4957
-4891
-6466
Mass Entropy
(Btu/lb-F)
2.224
2.267
1.234
10.24
9.751
21.51
0.5723
0.5453
1.194
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
11.46 1.764e+004
4919
5090
979.4
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
3743
3906
0.6362
Phase Fraction [Vol. Basis]
0.9702
0.9702
2.984e-002
Phase Fraction [Mass Basis]
0.9583
0.9583
4.170e-002
---
---
---
342.1
---
---
(Btu/lb) (psia)
9.957e-002
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
0.0000
0.0000
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
10.24
9.751
21.51
36
Std. Gas Flow
(MMSCFD)
0.0000
37
Std. Ideal Liq. Mass Density
38
Act. Liq. Flow
39
Z Factor
40
Watson K
41
User Property
42
Partial Pressure of H2S
43
Cp/(Cp - R)
44
Cp/Cv
45
Heat of Vap.
46
Kinematic Viscosity
47
Liq. Mass Density (Std. Cond)
48
Liq. Vol. Flow (Std. Cond)
49
Liquid Fraction
50
Molar Volume
51
Mass Heat of Vap.
52
Phase Fraction [Molar Basis]
53
Surface Tension
54
Thermal Conductivity
55
Viscosity
56
Cv (Semi-Ideal)
57
Mass Cv (Semi-Ideal)
58
Cv
59
Mass Cv
60
Cv (Ent. Method)
61
Mass Cv (Ent. Method)
62
Cp/Cv (Ent. Method)
63
Reid VP at 37.8 C
(psia)
64
True VP at 37.8 C
(psia)
65 66
0.0000
0.0000
(lb/ft3)
44.57
44.03
62.30
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
0.9253
19.04
19.04
17.57
---
---
---
0.0000
---
---
1.241
1.256
1.102
1.334
1.378
1.214
2.234e+004 ---
(Btu/lb)
---
---
1.140
0.1497
49.23
48.70
63.35
0.0000
0.0000
0.0000
4.141e-002 (ft3/lbmole)
1.335e-002
22.82
0.0000
1.000
23.79
0.3432
1249
---
---
0.9586
0.9586
0.0414
(dyne/cm)
35.00
(Btu/hr-ft-F)
---
2.459e-002
0.3785
---
1.372e-002
0.1259
(cP) (Btu/lbmole-F)
---
35.00
8.252
7.765
19.52
0.4613
0.4342
1.084
7.673
7.078
17.72
0.4289
0.3957
0.9835
---
---
15.78
---
---
0.8758
---
---
1.363
---
---
---
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-20.24
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 44 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 15 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.8132
0.0000
0.8189
0.0000
0.5859
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.1693
0.0000
0.1518
0.0000
0.3620
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0139
0.0000
0.0234
0.0000
0.0469
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0003
0.0000
0.0006
0.0000
0.0006
24
Nitrogen
0.0000
0.0034
0.0000
0.0053
0.0000
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.8051
0.0000
0.8110
0.0000
0.5731
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.1766
0.0000
0.1584
0.0000
0.3731
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0145
0.0000
0.0244
0.0000
0.0484
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0003
0.0000
0.0007
0.0000
0.0006
43
Nitrogen
0.0000
0.0035
0.0000
0.0055
0.0000
0.0048
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
4.141e-002 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
0.0000
1.0000
0.0000
1.0000
0.0000
0.9999
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 45 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 15 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.8052
---
0.8052
14
Oxygen
---
---
---
15
Methane
5547
---
5547
---
---
---
---
---
16
H2S
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
244.5
---
244.5
21
Nitrogen
1872
---
1872
---
---
---
22
1.872e+004
Air
---
---
1.872e+004
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Component Splitter:
30
LOGICAL CONNECTION
V-078 OXIDO DE ZINC
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
0.0000 lbmole/hrMass:
40
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 16
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.2092
0.2092
0.7908
(F)
262.1
262.1
262.1
(psia)
364.7*
364.7
364.7
2359
493.5
(lbmole/hr) (lb/hr)
(Btu/hr)
4.220e+004 4047 -1.025e+005 23.15 -2.419e+008 3664*
(barrel/day)
64
8594 1741 -3.824e+004 41.18 -1.887e+007 7.965e+005
1866 3.361e+004 2306 -1.196e+005 18.38 -2.230e+008 2268
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3)
0.2179
17.41 4.817e-002
Aqueous Phase 18.02 3.206
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 46 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 16 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
3.201e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
3.540e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
---
24
LHV Mass Basis (Std)
(Btu/lb)
3743
25
Phase Fraction [Vol. Basis]
0.4303
0.4303
26
Phase Fraction [Mass Basis]
0.2036
0.2036
27
Phase Fraction [Act. Vol. Basis]
0.9463
0.9463
28
Mass Exergy
(Btu/lb)
65.71
---
29
Partial Pressure of CO2
(psia)
0.4503
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
3.898 4.628e+004
0.8388 4.380e+004
57.75 2488
(Btu/lb)
-5732
-2196
-6637
(Btu/lb-F)
1.294
2.365
1.020
17.36
10.25
19.24
0.9706
0.5888
1.068
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
4919
2.033e+004
3.985 1.764e+004 978.9
---
---
---
---
1.394e-005
---
2.414e-007
1.838e+004
---
0.2212 0.5697 0.7964 5.375e-002 ---
(ACFM)
170.8
170.8
---
(lbmole/ft3)
2.492
1.211
3.458
Specific Heat
(Btu/lbmole-F)
17.36
10.25
19.24
Std. Gas Flow
(MMSCFD)
21.44
4.486
16.96
(lb/ft3)
44.57
21.10
62.30
(USGPS)
1.209
---
---
0.9776
19.04
19.04
12.33
---
---
---
0.0000
---
---
1.129
1.240
1.115
1.030
1.287
1.180
(psia)
(Btu/lbmole)
2.234e+004
---
---
1.086
0.2323
(cSt)
---
(lb/ft3)
49.23
4.612e-002
3664
7.965e+005
(barrel/day)
1.209 1.469e-002
63.35 2268
0.7908
0.0000
1.000
(ft3/lbmole)
4.590
20.76
0.3119
(Btu/lb)
1249
---
---
0.2092
0.2092
0.7908
(dyne/cm)
53.19
(Btu/hr-ft-F)
---
2.736e-002
0.3973
---
1.458e-002
0.2149
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
53.19
15.38
8.268
17.26
0.8596
0.4748
0.9580
16.87
7.965
16.30
0.9428
0.4574
0.9050
---
---
14.67
---
---
0.8142
---
---
1.312
---
---
---
---
---
7.988e+005 ---
7.965e+005 ---
--2268 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 47 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 16 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
1918.3906
0.8132
17
Oxygen
0.0000
0.0000
18
Methane
399.3043
19
H2S
20
Hydrogen
21
Ethane
22
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2371.1965
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6405.9987
0.1518
1465.0823
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
24
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
34560.0000
42202.3504
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2092 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
52.8597
0.1071
952.2721
0.1108
65.3364
0.0375
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
399.2831
0.8091
6405.6590
0.7454
1465.0046
0.8413
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
32.8157
0.0665
986.7648
0.1148
189.9629
0.1091
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6094
0.0012
26.8191
0.0031
2.2250
0.0013
43
Nitrogen
7.9325
0.0161
222.2130
0.0259
18.8691
0.0108
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
493.5004
1.0000
8593.7281
1.0000
1741.3979
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
53
CO
0.0000
0.0000
54
H2O
1865.5310
1.0000
55
Oxygen
0.0000
0.0000
56
Methane
0.0212
57
H2S
58
MASS FLOW (lb/hr) 0.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7908 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2305.8602
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.3398
0.0000
0.0777
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0002
0.0000
0.0062
0.0000
0.0012
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0081
0.0000
0.3570
0.0000
0.0296
0.0000
62
Nitrogen
0.0068
0.0000
0.1915
0.0000
0.0163
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
1865.5673
1.0000
1.0000
2305.9849
1.0000
33607.7279
33608.6223
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 48 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 16 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.1071
---
0.1071
---
---
14
Oxygen
15
Methane
16
7.127e+004
H2S
---
---
---
---
---
---
7.127e+004 ---
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
284.0
---
284.0
21
Nitrogen
4387
---
4387
---
---
---
22
6.040e+005
Air
---
---
6.040e+005
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO LNG:
PRODUCT FROM
E-1 PRECALENTADOR DE GAS-VAPOR DE Component PROCESO Splitter:
30
LOGICAL CONNECTION
V-079 OXIDO DE ZINC
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
2359 lbmole/hrMass:
40
4.220e+004 lb/hrStd Ideal Liq Volume:
4047 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 17
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.9586
0.9586
0.0414
(F)
414.1*
414.1
414.1
(psia)
364.7*
364.7
364.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-8.867e+004
-8.747e+004
0.0000 -1.165e+005
39.79
40.55
22.23
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3)
4.382e-002
17.88 4.203e-002
Aqueous Phase 18.02 2.914
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 49 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 17 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Density
13
Act. Volume Flow
14 15 16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.985e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
9.104e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26 27
Phase Fraction [Act. Vol. Basis]
28
Mass Exergy
29
Partial Pressure of CO2
30
Cost Based on Flow
31
Act. Gas Flow
32
Avg. Liq. Density
33
(lb/ft3)
Aqueous Phase
0.7840
0.7517
52.50
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-4957
-4891
-6466
Mass Entropy
(Btu/lb-F)
2.224
2.267
1.234
10.24
9.751
21.51
0.5723
0.5453
1.194
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
11.46 1.764e+004
4919
5090
979.4
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
3743
3906
0.6362
Phase Fraction [Vol. Basis]
0.9702
0.9702
2.984e-002
Phase Fraction [Mass Basis]
0.9583
0.9583
4.170e-002
---
---
---
342.1
---
---
(Btu/lb) (psia)
9.957e-002
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
0.0000
0.0000
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
10.24
9.751
21.51
34
Std. Gas Flow
(MMSCFD)
0.0000
35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63 64
0.0000
0.0000
(lb/ft3)
44.57
44.03
62.30
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
0.9253
19.04
19.04
17.57
---
---
---
0.0000
---
---
1.241
1.256
1.102
1.334
1.378
1.214
2.234e+004 ---
(Btu/lb)
---
---
1.140
0.1497
49.23
48.70
63.35
0.0000
0.0000
0.0000
4.141e-002 (ft3/lbmole)
1.335e-002
22.82
0.0000
1.000
23.79
0.3432
1249
---
---
0.9586
0.9586
0.0414
(dyne/cm)
35.00
(Btu/hr-ft-F)
---
2.459e-002
0.3785
---
1.372e-002
0.1259
(cP) (Btu/lbmole-F)
---
35.00
8.252
7.765
19.52
0.4613
0.4342
1.084
7.673
7.078
17.72
0.4289
0.3957
0.9835
---
---
15.78
---
---
0.8758
---
---
1.363
---
---
---
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-20.24
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 50 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 17 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.8132
0.0000
0.8189
0.0000
0.5859
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.1693
0.0000
0.1518
0.0000
0.3620
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0139
0.0000
0.0234
0.0000
0.0469
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0003
0.0000
0.0006
0.0000
0.0006
24
Nitrogen
0.0000
0.0034
0.0000
0.0053
0.0000
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9586 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.8051
0.0000
0.8110
0.0000
0.5731
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.1766
0.0000
0.1584
0.0000
0.3731
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0145
0.0000
0.0244
0.0000
0.0484
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0003
0.0000
0.0007
0.0000
0.0006
43
Nitrogen
0.0000
0.0035
0.0000
0.0055
0.0000
0.0048
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
4.141e-002 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
0.0000
1.0000
0.0000
1.0000
0.0000
0.9999
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 51 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 17 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
---
---
---
13
H2O
0.8052
---
0.8052
14
Oxygen
---
---
---
15
Methane
5547
---
5547
---
---
---
---
---
16
H2S
17
Hydrogen
18
Ethane
19
Propane
---
---
---
20
CO2
244.5
---
244.5
21
Nitrogen
1872
---
1872
---
---
---
22
1.872e+004
Air
---
---
1.872e+004
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Component Splitter:
30
LOGICAL CONNECTION
V-079 OXIDO DE ZINC
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 364.7 psia
0.0000 lbmole/hrMass:
40
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 18
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
825.0*
825.0
(psia)
254.7*
254.7
(lbmole/hr) (lb/hr)
(Btu/hr)
2359 4.220e+004 4047 -8.389e+004 45.08 -1.979e+008 3664*
(barrel/day)
64
2359 4.220e+004 4047 -8.389e+004 45.08 -1.979e+008 3664
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.89
(lbmole/ft3)
1.874e-002
17.89 1.874e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 52 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 18 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-4689
-4689
15
Mass Entropy
(Btu/lb-F)
2.520
2.520
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.696e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
8.800e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.3352 5.382e+005
0.3352 5.382e+005
10.31
10.31
0.5763
0.5763
4919
4919
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
3743
3743
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
27
Phase Fraction [Act. Vol. Basis]
1.000
1.000
28
Mass Exergy
450.6
---
29
Partial Pressure of CO2
30
Cost Based on Flow
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(Btu/lb) (psia) (Cost/s)
6.667e-002 0.0000
--0.0000
(ACFM)
2099
2099
(lbmole/ft3)
2.492
2.492
Specific Heat
(Btu/lbmole-F)
10.31
10.31
Std. Gas Flow
(MMSCFD)
21.44
21.44
(lb/ft3)
44.57
44.57
(USGPS)
---
---
0.9861
0.9861
19.04
19.04
---
---
(psia)
(Btu/lbmole)
0.0000
---
1.239
1.239
1.263
1.263
2.254e+004
---
(cSt)
3.896
3.896
(lb/ft3)
49.23
49.23
(barrel/day)
3664
3664
0.0000
0.0000
(ft3/lbmole)
53.37
53.37
(Btu/lb)
1260
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
3.947e-002
3.947e-002
2.092e-002
2.092e-002
8.324
8.324
0.4653
0.4653
8.161
8.161
0.4562
0.4562
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
3664
3664
-3.959
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 53 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 18 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
1918.3906
0.8132
17
Oxygen
0.0000
0.0000
18
Methane
399.3043
19
H2S
20
Hydrogen
21
Ethane
22
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2371.1965
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6405.9987
0.1518
1465.0823
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
24
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
30
0.0000
Vapour Fraction
34560.0000
42202.3504
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
34
CO
0.0000
0.0000
35
H2O
1918.3906
0.8132
36
Oxygen
0.0000
0.0000
37
Methane
399.3043
38
H2S
39
Hydrogen
40
Ethane
41
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2371.1965
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6405.9987
0.1518
1465.0823
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.8159
0.0139
986.7710
0.0234
189.9641
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.6175
0.0003
27.1761
0.0006
2.2546
0.0006
43
Nitrogen
7.9393
0.0034
222.4045
0.0053
18.8854
0.0047
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
2359.0677
1.0000
1.0000
4047.3829
1.0000
49
34560.0000
42202.3504
K VALUE
50 51
0.0000
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 54 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 18 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Tee:
TEE-100 LNG:
LOGICAL CONNECTION
E-1 PRECALENTADOR DE GAS-VAPOR DE PROCESO
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 254.7 psia
2359 lbmole/hrMass:
23
4.220e+004 lb/hrStd Ideal Liq Volume:
4047 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 19
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
825.0
825.0
(psia)
254.7
254.7
26.35*
26.35
471.4
471.4
(lbmole/hr) (lb/hr)
(Btu/hr)
45.21 -8.389e+004 45.08 -2.211e+006 40.93*
(barrel/day)
47
45.21 -8.389e+004 45.08 -2.211e+006 40.93
PROPERTIES
48 49
Overall
Vapour Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
55
Mass Entropy
56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.696e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
8.800e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66
17.89 (lbmole/ft3) (lb/ft3)
1.874e-002 0.3352
17.89 1.874e-002 0.3352
(barrel/day)
6013
6013
(Btu/lb)
-4689
-4689
(Btu/lb-F)
2.520
2.520
(Btu/lbmole-F) (Btu/lb-F)
10.31
0.5763
0.5763
4919
4919
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
3743
3743
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
67
Phase Fraction [Act. Vol. Basis]
1.000
1.000
68
Mass Exergy
450.6
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
10.31
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 55 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 19 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
(psia)
Vapour Phase
6.667e-002
---
(Cost/s)
0.0000
0.0000
(ACFM)
23.44
23.44
(lbmole/ft3)
2.492
2.492
Specific Heat
(Btu/lbmole-F)
10.31
10.31
17
Std. Gas Flow
(MMSCFD)
0.2396
0.2396
18
Std. Ideal Liq. Mass Density
(lb/ft3)
44.57
44.57
19
Act. Liq. Flow
(USGPS)
---
---
20
Z Factor
0.9861
0.9861
21
Watson K
19.04
19.04
22
User Property
---
---
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46 47
(psia)
(Btu/lbmole)
0.0000
---
1.239
1.239
1.263
1.263
2.254e+004
---
(cSt)
3.896
3.896
(lb/ft3)
49.23
49.23
(barrel/day)
40.93
40.93
0.0000
0.0000
(ft3/lbmole)
53.37
53.37
(Btu/lb)
1260
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
3.947e-002
3.947e-002
2.092e-002
2.092e-002
8.324
8.324
0.4653
0.4653
8.161
8.161
0.4562
0.4562
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
40.93
40.93
Viscosity Index
-3.959
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
H2O
21.4303
0.8132
386.0695
0.8189
26.4886
0.5859
56
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Methane
4.4606
0.1693
71.5614
0.1518
16.3664
0.3620
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Ethane
0.3666
0.0139
11.0232
0.0234
2.1221
0.0469
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0069
0.0003
0.3036
0.0006
0.0252
0.0006
63
Nitrogen
0.0887
0.0034
2.4845
0.0053
0.2110
0.0047
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
26.3531
1.0000
471.4422
1.0000
45.2133
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 56 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 19 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
21.4303
0.8132
386.0695
0.8189
26.4886
0.5859
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
4.4606
0.1693
71.5614
0.1518
16.3664
0.3620
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.3666
0.0139
11.0232
0.0234
2.1221
0.0469
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0069
0.0003
0.3036
0.0006
0.0252
0.0006
24
Nitrogen
0.0887
0.0034
2.4845
0.0053
0.2110
0.0047
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
26.3531
1.0000
471.4422
1.0000
45.2133
1.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Conversion Reactor:
H-1
51
Tee:
LOGICAL CONNECTION TEE-100
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Active)
61
254.7 psia Molar:
* Mass: 26.35 lbmole/hr
471.4 lb/hr Std Ideal Liq Volume:
45.21 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 57 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 20
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
825.0
825.0
(psia)
254.7
254.7
(lbmole/hr) (lb/hr)
(Btu/hr)
2333 4.173e+004 4002 -8.389e+004 45.08 -1.957e+008 3623*
(barrel/day)
22
2333 4.173e+004 4002 -8.389e+004 45.08 -1.957e+008 3623
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-4689
-4689
30
Mass Entropy
(Btu/lb-F)
2.520
2.520
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
6.696e+004
6.696e+004
34
HHV Molar Basis (Std)
(Btu/lbmole)
8.800e+004
8.800e+004
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41
17.89 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.874e-002 0.3352 5.322e+005
17.89 1.874e-002 0.3352 5.322e+005
10.31
10.31
0.5763
0.5763
4919
4919
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
3743
3743
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
450.6
---
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lb) (psia) (Cost/s)
6.667e-002 0.0000
--0.0000
(ACFM)
2075
2075
(lbmole/ft3)
2.492
2.492
Specific Heat
(Btu/lbmole-F)
10.31
10.31
Std. Gas Flow
(MMSCFD)
21.20
21.20
(lb/ft3)
44.57
44.57
(USGPS)
---
---
0.9861
0.9861
19.04
19.04
---
---
Licensed to: LEGENDS
(psia)
(Btu/lbmole)
0.0000
---
1.239
1.239
1.263
1.263
2.254e+004
---
(cSt)
3.896
3.896
(lb/ft3)
49.23
49.23
(barrel/day)
3623
3623
0.0000
0.0000
(ft3/lbmole)
53.37
53.37
(Btu/lb)
1260
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
3.947e-002
3.947e-002
2.092e-002
2.092e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 58 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 20 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 8.324
8.324
0.4653
0.4653
8.161
8.161
0.4562
0.4562
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
3623
3623
-3.959
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
29
CO
0.0000
0.0000
30
H2O
1896.9603
0.8132
31
Oxygen
0.0000
0.0000
32
Methane
394.8437
33
H2S
34
Hydrogen
35
Ethane
36
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2344.7079
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6334.4374
0.1518
1448.7158
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.4493
0.0139
975.7478
0.0234
187.8420
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.6106
0.0003
26.8726
0.0006
2.2294
0.0006
38
Nitrogen
7.8506
0.0034
219.9200
0.0053
18.6744
0.0047
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
2332.7145
1.0000
1.0000
4002.1696
1.0000
44
0.0000
Vapour Fraction
34173.9305
41730.9082
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
48
CO
0.0000
0.0000
49
H2O
1896.9603
0.8132
50
Oxygen
0.0000
0.0000
51
Methane
394.8437
52
H2S
53
Hydrogen
54
Ethane
55
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8189
2344.7079
0.5859
0.0000
0.0000
0.0000
0.0000
0.1693
6334.4374
0.1518
1448.7158
0.3620
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32.4493
0.0139
975.7478
0.0234
187.8420
0.0469
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6106
0.0003
26.8726
0.0006
2.2294
0.0006
57
Nitrogen
7.8506
0.0034
219.9200
0.0053
18.6744
0.0047
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
2332.7145
1.0000
1.0000
4002.1696
1.0000
63
34173.9305
41730.9082
K VALUE
64 65
0.0000
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 59 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 20 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Conversion Reactor:
H-1
LOGICAL CONNECTION
Tee:
TEE-100
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
254.7 psia 2333 lbmole/hrMass:
37
4.173e+004 lb/hrStd Ideal Liq Volume:
4002 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 21
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
1.0000
1.0000
(F)
1385*
1385
1385
(psia)
254.7
254.7
254.7
3006
0.0000
(lbmole/hr) (lb/hr)
(Btu/hr)
3006 4.220e+004 5520 -5.149e+004 43.74 -1.548e+008 5900*
(barrel/day)
61
4.220e+004 5520 -5.149e+004 43.74 -1.548e+008 5900
0.0000
0.0000 0.0000 -5.149e+004 43.74 0.0000 0.0000
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 14.04
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
1.285e-002 0.1804 9.999e+005 -3668
14.04 1.285e-002 0.1804 9.999e+005 -3668
Aqueous Phase 14.04 1.285e-002 0.1804 0.0000 -3667
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 60 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 21 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
6.100e+004
6.100e+004
6.100e+004
16
HHV Molar Basis (Std)
(Btu/lbmole)
7.752e+004
7.752e+004
7.752e+004
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22 23 24
Phase Fraction [Act. Vol. Basis]
25
Mass Exergy
26
Partial Pressure of CO2
27
Cost Based on Flow
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.115
3.115
9.448
9.448
3.115 9.448
0.6729
0.6729
0.6729
5521
5521
5521
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
4345
4345
4345
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
688.8
---
---
(psia)
15.62
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
3899
3899
---
(lbmole/ft3)
2.328
2.328
2.328
Specific Heat
(Btu/lbmole-F)
9.448
9.448
9.448
Std. Gas Flow
(MMSCFD)
27.32
27.32
0.0000
(lb/ft3)
32.68
32.68
32.68
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole)
---
1.001
1.001
14.99
14.99
14.99
---
---
---
0.0000
---
---
1.266
1.266
1.266
1.271
1.271
1.271
1.910e+004
---
--0.8475
(cSt)
9.500
9.500
(lb/ft3)
30.58
30.58
30.57
5900
5900
0.0000
(barrel/day)
0.0000
0.0000
1.000
(ft3/lbmole)
77.82
77.82
77.82
(Btu/lb)
1360
---
---
1.0000
1.0000
0.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
0.0000
9.446e-002
9.446e-002
9.529e-002
2.746e-002
2.746e-002
2.449e-003
7.462
7.462
7.462
0.5315
0.5315
0.5315
7.434
7.434
7.434
0.5295
0.5295
0.5295
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
---
5900
5900
0.0000
0.8786
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 139.7565
MOLE FRACTION 0.0465
MASS FLOW (lb/hr) 3914.7054
Vapour Fraction MASS FRACTION 0.0928
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 335.3202
1.0000
LIQUID VOLUME FRACTION 0.0607
Page 61 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 21 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
H2O
1411.2742
0.4695
0.6024
1744.3832
0.3160
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
75.8678
0.0252
1217.1398
0.0288
278.3656
0.0504
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
1153.9894
0.3839
2326.4426
0.0551
2280.2771
0.4131
20
Ethane
32.8159
0.0109
986.7710
0.0234
189.9641
0.0344
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
184.2975
0.0613
8110.8767
0.1922
672.9082
0.1219
23
Nitrogen
7.9393
0.0026
222.4045
0.0053
18.8854
0.0034
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
3005.9406
1.0000
1.0000
5520.1038
1.0000
25424.2464
42202.5863
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
33
CO
139.7565
0.0465
3914.7054
0.0928
335.3202
0.0607
34
H2O
1411.2742
0.4695
25424.2464
0.6024
1744.3832
0.3160
35
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Methane
75.8678
0.0252
1217.1398
0.0288
278.3656
0.0504
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
1153.9894
0.3839
2326.4426
0.0551
2280.2771
0.4131
39
Ethane
32.8159
0.0109
986.7710
0.0234
189.9641
0.0344
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
184.2975
0.0613
8110.8767
0.1922
672.9082
0.1219
42
Nitrogen
7.9393
0.0026
222.4045
0.0053
18.8854
0.0034
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
3005.9406
1.0000
1.0000
5520.1038
1.0000
48
42202.5863
Aqueous Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
52
CO
0.0000
0.0465
0.0000
0.0928
0.0000
0.0607
53
H2O
0.0000
0.4695
0.0000
0.6024
0.0000
0.3160
54
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Methane
0.0000
0.0252
0.0000
0.0288
0.0000
0.0504
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
0.0000
0.3839
0.0000
0.0551
0.0000
0.4131
58
Ethane
0.0000
0.0109
0.0000
0.0234
0.0000
0.0344
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
0.0000
0.0613
0.0000
0.1922
0.0000
0.1219
61
Nitrogen
0.0000
0.0026
0.0000
0.0053
0.0000
0.0034
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 62 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 21 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
1.000
---
1.000
13
H2O
1.000
---
1.000
14
Oxygen
---
---
---
15
Methane
1.000
---
1.000
16
---
---
---
Hydrogen
H2S
1.000
---
1.000
18
Ethane
1.000
---
1.000
19
Propane
---
---
---
20
CO2
1.000
---
1.000
21
Nitrogen
1.000
---
1.000
---
---
---
17
22
Air
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Mixer:
LOGICAL CONNECTION
MIX-100 Conversion Reactor:
30
H-1
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
254.7 psia 3006 lbmole/hrMass:
40
4.220e+004 lb/hrStd Ideal Liq Volume:
5520 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 22
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.0000
0.0000
(F)
1385
1385
1385
(psia)
254.7
254.7
254.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-5.149e+004
-5.149e+004
1.0000
0.0000 -5.149e+004
43.74
43.74
43.74
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 14.04
(lbmole/ft3)
1.285e-002
14.04 1.285e-002
Aqueous Phase 14.04 1.285e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 63 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 22 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Density
13
Act. Volume Flow
14
(lb/ft3)
Vapour Phase
Aqueous Phase
0.1804
0.1804
0.1804
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-3667
-3668
-3667
15
Mass Entropy
(Btu/lb-F)
3.115
3.115
3.115
16
Heat Capacity
9.448
9.448
9.448
17
Mass Heat Capacity
0.6729
0.6729
0.6729
18
LHV Molar Basis (Std)
(Btu/lbmole)
6.100e+004
6.100e+004
6.100e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
7.752e+004
7.752e+004
7.752e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
Phase Fraction [Vol. Basis]
26
Phase Fraction [Mass Basis]
27
Phase Fraction [Act. Vol. Basis]
28
Mass Exergy
29
Partial Pressure of CO2
30
Cost Based on Flow
31
Act. Gas Flow
32
Avg. Liq. Density
33
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
5521
5521
5521
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
4345
4345
4345
---
---
1.000
0.0000
0.0000
1.000
---
---
---
(Btu/lb)
688.8
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
9.448
9.448
9.448
34
Std. Gas Flow
(MMSCFD)
0.0000
35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63 64
0.0000
0.0000
(lb/ft3)
32.68
32.68
32.68
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
1.001
1.001
14.99
14.99
14.99
---
---
---
0.0000
---
---
1.266
1.266
1.266
1.271
1.271
1.271
1.910e+004 0.8475
---
---
9.500
0.8475
30.57
30.58
30.57
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
77.82
77.82
77.82
(Btu/lb)
1360
---
---
0.0000
0.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
---
9.529e-002
9.446e-002
9.529e-002
2.449e-003
2.746e-002
2.449e-003
7.462
7.462
7.462
0.5315
0.5315
0.5315
7.434
7.434
7.434
0.5295
0.5295
0.5295
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
0.8786
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 64 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 22 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0465
0.0000
0.0928
0.0000
0.0607
16
H2O
0.0000
0.4695
0.0000
0.6024
0.0000
0.3160
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0252
0.0000
0.0288
0.0000
0.0504
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.3839
0.0000
0.0551
0.0000
0.4131
21
Ethane
0.0000
0.0109
0.0000
0.0234
0.0000
0.0344
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0613
0.0000
0.1922
0.0000
0.1219
24
Nitrogen
0.0000
0.0026
0.0000
0.0053
0.0000
0.0034
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0465
0.0000
0.0928
0.0000
0.0607
35
H2O
0.0000
0.4695
0.0000
0.6024
0.0000
0.3160
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.0252
0.0000
0.0288
0.0000
0.0504
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.3839
0.0000
0.0551
0.0000
0.4131
40
Ethane
0.0000
0.0109
0.0000
0.0234
0.0000
0.0344
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0613
0.0000
0.1922
0.0000
0.1219
43
Nitrogen
0.0000
0.0026
0.0000
0.0053
0.0000
0.0034
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0465
0.0000
0.0928
0.0000
0.0607
54
H2O
0.0000
0.4695
0.0000
0.6024
0.0000
0.3160
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0252
0.0000
0.0288
0.0000
0.0504
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.3839
0.0000
0.0551
0.0000
0.4131
59
Ethane
0.0000
0.0109
0.0000
0.0234
0.0000
0.0344
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0000
0.0613
0.0000
0.1922
0.0000
0.1219
62
Nitrogen
0.0000
0.0026
0.0000
0.0053
0.0000
0.0034
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 65 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 22 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
1.000
---
1.000
13
H2O
1.000
---
1.000
14
Oxygen
---
---
---
15
Methane
1.000
---
1.000
16
---
---
---
Hydrogen
H2S
1.000
---
1.000
18
Ethane
1.000
---
1.000
19
Propane
---
---
---
20
CO2
1.000
---
1.000
21
Nitrogen
1.000
---
1.000
---
---
---
17
22
Air
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Conversion Reactor:
30
LOGICAL CONNECTION H-1
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
254.7 psia 0.0000 lbmole/hrMass:
40
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 23
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
1223
1223
(psia)
254.7
254.7
(lbmole/hr) (lb/hr)
(Btu/hr)
3650 6.078e+004 6990 -4.216e+004 43.09 -1.539e+008 9896*
(barrel/day)
64
3650 6.078e+004 6990 -4.216e+004 43.09 -1.539e+008 9896
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 16.65
(lbmole/ft3)
1.409e-002
16.65 1.409e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 66 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 23 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-2532
-2532
15
Mass Entropy
(Btu/lb-F)
2.587
2.587
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
5.024e+004
5.024e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
6.384e+004
6.384e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.2346 1.108e+006
0.2346 1.108e+006
9.008
9.008
0.5409
0.5409
3834
3834
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
3017
3017
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
27
Phase Fraction [Act. Vol. Basis]
1.000
1.000
28
Mass Exergy
(Btu/lb)
494.8
---
29
Partial Pressure of CO2
(psia)
12.86
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
(ACFM)
4318
4318
(lbmole/ft3)
2.232
2.232
Specific Heat
(Btu/lbmole-F)
9.008
9.008
Std. Gas Flow
(MMSCFD)
33.18
33.18
(lb/ft3)
37.17
37.17
(USGPS)
---
---
Z Factor
1.002
1.002
38
Watson K
10.31
10.31
39
User Property
---
---
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(psia)
(Btu/lbmole)
0.0000
---
1.283
1.283
1.288
1.288
1.879e+004
---
(cSt)
7.488
7.488
(lb/ft3)
26.25
26.25
(barrel/day)
9896
9896
0.0000
0.0000
(ft3/lbmole)
70.99
70.99
(Btu/lb)
1129
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
7.588e-002
7.588e-002
2.814e-002
2.814e-002
7.022
7.022
0.4217
0.4217
6.994
6.994
0.4200
0.4200
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
9896
9896
-1.779
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 67 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 23 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
CO
139.7565
0.0383
3914.7054
0.0644
335.3202
0.0480
16
H2O
1411.2742
0.3867
25424.2464
0.4183
1744.3832
0.2495
17
Oxygen
135.2105
0.0370
4326.7368
0.0712
260.4106
0.0373
18
Methane
75.8678
0.0208
1217.1398
0.0200
278.3656
0.0398
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1153.9894
0.3162
2326.4426
0.0383
2280.2771
0.3262
21
Ethane
32.8159
0.0090
986.7710
0.0162
189.9641
0.0272
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
184.2975
0.0505
8110.8767
0.1335
672.9082
0.0963
24
Nitrogen
516.5885
0.1415
14471.1926
0.2381
1228.8138
0.1758
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
3649.8002
1.0000
1.0000
6990.4428
1.0000
30
60778.1113
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
34
CO
139.7565
0.0383
3914.7054
0.0644
335.3202
0.0480
35
H2O
1411.2742
0.3867
25424.2464
0.4183
1744.3832
0.2495
36
Oxygen
135.2105
0.0370
4326.7368
0.0712
260.4106
0.0373
37
Methane
75.8678
0.0208
1217.1398
0.0200
278.3656
0.0398
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1153.9894
0.3162
2326.4426
0.0383
2280.2771
0.3262
40
Ethane
32.8159
0.0090
986.7710
0.0162
189.9641
0.0272
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
184.2975
0.0505
8110.8767
0.1335
672.9082
0.0963
43
Nitrogen
516.5885
0.1415
14471.1926
0.2381
1228.8138
0.1758
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
3649.8002
1.0000
1.0000
6990.4428
1.0000
49
K VALUE
50 51
60778.1113
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 68 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 23 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO Conversion Reactor:
PRODUCT FROM
H-1 REFORMADOR SECUNDARIO Mixer:
LOGICAL CONNECTION MIX-100
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
254.7 psia 3650 lbmole/hrMass:
23
6990 barrel/day
User Variables
24 25
NOTES
26 27
6.078e+004 lb/hrStd Ideal Liq Volume:
29285
28 29 30
(Last modified Mon Dec 17, 2018, 15:07)
31 32
Description
33 34 35
Material Stream: 24
36 37 38
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
39 40
Overall
41
Vapour / Phase Fraction
42
Temperature:
43
Pressure:
44
Molar Flow
45
Mass Flow
46
Std Ideal Liq Vol Flow
(barrel/day)
47
Molar Enthalpy
(Btu/lbmole)
48
Molar Entropy
(Btu/lbmole-F)
49
Heat Flow
50
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
982.0
982.0
982.0
(psia)
248.7
248.7
248.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-9.511e+004
-9.511e+004
0.0000 -9.511e+004
44.26
44.26
44.26
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
51
PROPERTIES
52 53
Overall
54
Molecular Weight
55
Molar Density
56
Mass Density
57
Act. Volume Flow
58
Vapour Phase 18.00
(lbmole/ft3)
1.629e-002
Liquid Phase 18.00 1.629e-002
0.2933
0.2933
0.2933
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-5284
-5284
-5284
59
Mass Entropy
(Btu/lb-F)
2.459
2.459
2.459
60
Heat Capacity
9.493
9.493
9.493
61
Mass Heat Capacity
0.5274
0.5274
0.5274
62
LHV Molar Basis (Std)
(Btu/lbmole)
63
HHV Molar Basis (Std)
(Btu/lbmole)
64
HHV Mass Basis (Std)
65
CO2 Loading
66
CO2 App ML Con
67
CO2 App WT Con
68
LHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
1.629e-002
18.00
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1217 1.874e+004
1217 1.874e+004
1217 1.874e+004
1041
1041
1041
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
67.59
67.59
67.59
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 69 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 24 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Phase Fraction [Vol. Basis]
13
Phase Fraction [Mass Basis]
14
Phase Fraction [Act. Vol. Basis]
15
Mass Exergy
16
Partial Pressure of CO2
17
Cost Based on Flow
18
Act. Gas Flow
19
Avg. Liq. Density
20
Vapour Phase
Liquid Phase
---
---
1.000
0.0000
0.0000
1.000
---
---
---
(Btu/lb)
541.7
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
9.493
9.493
9.493
21
Std. Gas Flow
(MMSCFD)
0.0000
22
Std. Ideal Liq. Mass Density
23
Act. Liq. Flow
24
Z Factor
25
Watson K
26
User Property
27
Partial Pressure of H2S
28
Cp/(Cp - R)
29
Cp/Cv
30
Heat of Vap.
31
Kinematic Viscosity
32
Liq. Mass Density (Std. Cond)
33
Liq. Vol. Flow (Std. Cond)
34
Liquid Fraction
35
Molar Volume
36
Mass Heat of Vap.
37
Phase Fraction [Molar Basis]
38
Surface Tension
39
Thermal Conductivity
40
Viscosity
41
Cv (Semi-Ideal)
42
Mass Cv (Semi-Ideal)
43
Cv
44
Mass Cv
45
Cv (Ent. Method)
46
Mass Cv (Ent. Method)
47
Cp/Cv (Ent. Method)
48
Reid VP at 37.8 C
49
True VP at 37.8 C
50 51
0.0000
0.0000
(lb/ft3)
61.35
61.35
61.35
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt)
---
0.9866
0.9866
10.10
10.10
10.10
---
---
---
0.0000
---
---
1.265
1.265
1.265
1.292
1.292
1.292
3.131e+004 0.7088
(lb/ft3) (barrel/day)
---
---
4.806
0.7088
62.38
62.38
62.38
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
61.37
61.37
61.37
(Btu/lb)
1739
---
---
0.0000
0.0000
1.0000
(dyne/cm)
---
(Btu/hr-ft-F)
0.1877
(cP)
---
3.330e-003
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
4.057e-002 2.258e-002
--0.1877 3.330e-003
7.507
7.507
7.507
0.4171
0.4171
0.4171
7.350
7.350
7.350
0.4083
0.4083
0.4083
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-1.939
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
52
COMPOSITION
53 54
Overall Phase
55 56
COMPONENTS
57
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
58
CO
0.0000
0.0009
0.0000
0.0014
0.0000
0.0018
59
H2O
0.0000
0.9844
0.0000
0.9853
0.0000
0.9702
60
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
61
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
62
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Hydrogen
0.0000
0.0077
0.0000
0.0009
0.0000
0.0121
64
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
65
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
CO2
0.0000
0.0019
0.0000
0.0047
0.0000
0.0056
67
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
68
Air
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 70 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 24 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
19
Vapour Phase
20 21
COMPONENTS
22
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
23
CO
0.0000
0.0009
0.0000
0.0014
0.0000
0.0018
24
H2O
0.0000
0.9844
0.0000
0.9853
0.0000
0.9702
25
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
26
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
27
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Hydrogen
0.0000
0.0077
0.0000
0.0009
0.0000
0.0121
29
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
30
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
CO2
0.0000
0.0019
0.0000
0.0047
0.0000
0.0056
32
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
33
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
38
Liquid Phase
39 40
COMPONENTS
41
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
42
CO
0.0000
0.0009
0.0000
0.0014
0.0000
0.0018
43
H2O
0.0000
0.9844
0.0000
0.9853
0.0000
0.9702
44
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
45
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
46
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Hydrogen
0.0000
0.0077
0.0000
0.0009
0.0000
0.0121
48
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
49
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
CO2
0.0000
0.0019
0.0000
0.0047
0.0000
0.0056
51
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
52
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
57
K VALUE
58 59
COMPONENTS
MIXED
LIGHT
HEAVY
60
CO
1.000
1.000
---
61
H2O
1.000
1.000
---
62
Oxygen
1.000
1.000
---
63
Methane
1.000
1.000
---
---
---
---
64
H2S
65
Hydrogen
1.000
1.000
---
66
Ethane
1.000
1.000
---
67
Propane
---
---
---
68
CO2
1.000
1.000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 71 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 24 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
LIGHT
Nitrogen
13
Air
HEAVY
1.000
1.000
---
---
---
---
14
Mercury
---
---
---
15
MEAmine
---
---
---
16
Ammonia
---
---
---
17
UNIT OPERATIONS
18 19
FEED TO
PRODUCT FROM
20
Conversion Reactor:
21
LOGICAL CONNECTION
H-1 REFORMADOR SECUNDARIO
UTILITIES
22 23
( No utilities reference this stream )
24
PROCESS UTILITY
25 26 27
DYNAMICS
28 29
Pressure Specification
(Inactive):
30
Flow Specification
(Inactive) Molar:
248.7 psia 0.0000 lbmole/hrMass:
31
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
32 33
NOTES
34 35 36
Description
37 38 39
Material Stream: 25
40 41 42
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
43 44
Overall
45
Vapour / Phase Fraction
46
Temperature:
47
Pressure:
48
Molar Flow
49
Mass Flow
50
Std Ideal Liq Vol Flow
(barrel/day)
51
Molar Enthalpy
(Btu/lbmole)
52
Molar Entropy
(Btu/lbmole-F)
53
Heat Flow
54
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
1.0000
1.0000
0.0000
(F)
982.0*
982.0
982.0
(psia)
248.7
248.7
(lbmole/hr) (lb/hr)
248.7
1.509e+005
1.509e+005
0.0000
2.717e+006
2.717e+006
0.0000
1.893e+005
1.893e+005
-9.511e+004
-9.511e+004
44.26
44.26
0.0000 -9.511e+004 44.26
(Btu/hr)
-1.436e+010
-1.436e+010
0.0000
(barrel/day)
* 1.862e+005
1.862e+005
0.0000
55
PROPERTIES
56 57
Overall
Vapour Phase
Liquid Phase
58
Molecular Weight
59
Molar Density
60
Mass Density
61
Act. Volume Flow
62
Mass Enthalpy
(Btu/lb)
-5284
-5284
-5284
63
Mass Entropy
(Btu/lb-F)
2.459
2.459
2.459
64
Heat Capacity
9.493
9.493
9.493
65
Mass Heat Capacity
0.5274
0.5274
0.5274
66
LHV Molar Basis (Std)
(Btu/lbmole)
67
HHV Molar Basis (Std)
(Btu/lbmole)
68
HHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.629e-002 0.2933 3.960e+007
1217 1.874e+004 1041
18.00 1.629e-002 0.2933 3.960e+007
1217 1.874e+004 1041
18.00 1.629e-002 0.2933 0.0000
1217 1.874e+004 1041
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 72 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 25 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
CO2 Loading
13
CO2 App ML Con
14
CO2 App WT Con
15
LHV Mass Basis (Std)
16 17 18
Phase Fraction [Act. Vol. Basis]
19
Mass Exergy
20
Partial Pressure of CO2
21
Cost Based on Flow
22
Act. Gas Flow
23
Avg. Liq. Density
24 25 26
Std. Ideal Liq. Mass Density
27
Act. Liq. Flow
28
Z Factor
29
Watson K
30
User Property
31
Partial Pressure of H2S
32
Cp/(Cp - R)
33
Cp/Cv
34
Heat of Vap.
35
Kinematic Viscosity
36
Liq. Mass Density (Std. Cond)
37
Liq. Vol. Flow (Std. Cond)
38
Liquid Fraction
39
Molar Volume
40
Mass Heat of Vap.
41
Phase Fraction [Molar Basis]
42
Surface Tension
43
Thermal Conductivity
44
Viscosity
45
Cv (Semi-Ideal)
46
Mass Cv (Semi-Ideal)
47
Cv
48
Mass Cv
49
Cv (Ent. Method)
50
Mass Cv (Ent. Method)
51
Cp/Cv (Ent. Method)
52
Reid VP at 37.8 C
53
True VP at 37.8 C
54
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
55
Viscosity Index
Vapour Phase
Liquid Phase
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
67.59
67.59
67.59
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
541.7
---
---
(psia)
0.4746
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1.544e+005
1.544e+005
---
(lbmole/ft3)
3.408
3.408
Specific Heat
(Btu/lbmole-F)
9.493
9.493
9.493
Std. Gas Flow
(MMSCFD)
1372
1372
0.0000
(lb/ft3)
61.35
61.35
61.35
(USGPS)
---
---
---
---
0.9866
0.9866
10.10
10.10
10.10
---
---
---
0.0000
---
---
1.265
1.265
1.265
1.292
1.292
1.292
(psia)
(Btu/lbmole) (cSt)
3.131e+004 4.806
(lb/ft3)
62.38
(barrel/day)
1.862e+005
3.408
---
---
4.806
0.7088
62.38 1.862e+005
62.38 0.0000
0.0000
0.0000
1.000
(ft3/lbmole)
61.37
61.37
61.37
(Btu/lb)
1739
---
---
1.0000
1.0000
0.0000
---
0.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
--4.057e-002
4.057e-002
2.258e-002
2.258e-002
0.1877 3.330e-003
7.507
7.507
7.507
0.4171
0.4171
0.4171
7.350
7.350
7.350
0.4083
0.4083
0.4083
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
1.862e+005 -1.939
56
1.862e+005 ---
--0.0000 ---
COMPOSITION
57 58
Overall Phase
59 60
COMPONENTS
61
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0014
335.6551
0.0018
0.9853
183673.4882
0.9702
62
CO
139.8961
0.0009
63
H2O
148599.0282
0.9844
64
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
65
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
66
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Hydrogen
1156.4711
0.0077
2331.4459
0.0009
2285.1811
0.0121
68
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
69
Aspen Technology Inc. Licensed to: LEGENDS
3918.6150 2.677026425e+06
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0010
Page 73 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 25 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
16
CO2
288.0576
0.0019
12677.3302
0.0047
1051.7579
0.0056
17
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
18
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Total
150949.1460
0.0000
1.0000
23
2.717102502e+06
1.0000
189315.9286
Vapour Phase
24 25
COMPONENTS
26
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
1.0000
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0014
335.6551
0.0018
0.9853
183673.4882
0.9702
27
CO
139.8961
0.0009
28
H2O
148599.0282
0.9844
29
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
30
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
31
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Hydrogen
1156.4711
0.0077
2331.4459
0.0009
2285.1811
0.0121
33
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
34
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
CO2
288.0576
0.0019
12677.3302
0.0047
1051.7579
0.0056
36
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
37
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Total
150949.1460
3918.6150 2.677026425e+06
1.0000
42
2.717102502e+06
1.0000
189315.9286
Liquid Phase
43 44
COMPONENTS
45
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
46
CO
0.0000
0.0009
0.0000
0.0014
0.0000
0.0018
47
H2O
0.0000
0.9844
0.0000
0.9853
0.0000
0.9702
48
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
49
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
50
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Hydrogen
0.0000
0.0077
0.0000
0.0009
0.0000
0.0121
52
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
53
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
CO2
0.0000
0.0019
0.0000
0.0047
0.0000
0.0056
55
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
56
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
61
K VALUE
62 63
COMPONENTS
MIXED
LIGHT
HEAVY
64
CO
1.000
1.000
---
65
H2O
1.000
1.000
---
66
Oxygen
1.000
1.000
---
67
Methane
1.000
1.000
---
---
---
68 69
H2S
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 74 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 25 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
Hydrogen
1.000
1.000
---
13
Ethane
1.000
1.000
---
14
Propane
---
---
---
15
CO2
1.000
1.000
---
16
Nitrogen
1.000
1.000
---
---
---
---
17
Air
18
Mercury
---
---
---
19
MEAmine
---
---
---
20
Ammonia
---
---
---
21
UNIT OPERATIONS
22 23 24
FEED TO LNG:
PRODUCT FROM
E-1 PRECALENTADOR DE GAS-VAPOR DE Conversion PROCESO Reactor:
25
LOGICAL CONNECTION
H-1 REFORMADOR SECUNDARIO
UTILITIES
26 27
( No utilities reference this stream )
28
PROCESS UTILITY
29 30 31
DYNAMICS
32 33
Pressure Specification
(Inactive):
34
Flow Specification
(Inactive) Molar:
248.7 psia 1.509e+005 lbmole/hr Mass:
35
2.717e+006 lb/hrStd Ideal Liq Volume: 1.893e+005 barrel/day
User Variables
36 37
NOTES
38 39 40
Description
41 42 43
Material Stream: 26
44 45 46
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
47 48
Overall
Vapour Phase
49
Vapour / Phase Fraction
50
Temperature:
51
Pressure:
52
Molar Flow
53
Mass Flow
54
Std Ideal Liq Vol Flow
(barrel/day)
1.893e+005
1.893e+005
55
Molar Enthalpy
(Btu/lbmole)
-9.540e+004
-9.540e+004
56
Molar Entropy
(Btu/lbmole-F)
57
Heat Flow
58
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
951.0
951.0
(psia)
244.7
(lbmole/hr) (lb/hr)
244.7
1.509e+005
1.509e+005
2.717e+006
2.717e+006
44.08
44.08
(Btu/hr)
-1.440e+010
-1.440e+010
(barrel/day)
* 1.862e+005
1.862e+005
59
PROPERTIES
60 61
Overall
Vapour Phase
62
Molecular Weight
63
Molar Density
64
Mass Density
65
Act. Volume Flow
66
Mass Enthalpy
(Btu/lb)
-5300
-5300
67
Mass Entropy
(Btu/lb-F)
2.449
2.449
68
Heat Capacity
9.451
9.451
69
Aspen Technology Inc. Licensed to: LEGENDS
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F)
1.640e-002 0.2952 3.934e+007
18.00 1.640e-002 0.2952 3.934e+007
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 75 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 26 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Heat Capacity
13
Vapour Phase
(Btu/lb-F)
0.5250
LHV Molar Basis (Std)
(Btu/lbmole)
1217
14
HHV Molar Basis (Std)
(Btu/lbmole)
15
HHV Mass Basis (Std)
16
CO2 Loading
17
CO2 App ML Con
18
CO2 App WT Con
19
LHV Mass Basis (Std)
20 21
(Btu/lb)
1.874e+004
0.5250 1217 1.874e+004
1041
1041
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
67.59
67.59
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
22
Phase Fraction [Act. Vol. Basis]
1.000
1.000
23
Mass Exergy
(Btu/lb)
530.7
---
24
Partial Pressure of CO2
(psia)
0.4670
---
25
Cost Based on Flow
(Cost/s)
0.0000
0.0000
26
Act. Gas Flow
27
Avg. Liq. Density
28
(ACFM)
1.534e+005
1.534e+005
(lbmole/ft3)
3.408
3.408
Specific Heat
(Btu/lbmole-F)
9.451
9.451
29
Std. Gas Flow
(MMSCFD)
1372
1372
30
Std. Ideal Liq. Mass Density
61.35
61.35
31
Act. Liq. Flow
32
Z Factor
33
Watson K
34
User Property
35
Partial Pressure of H2S
36
Cp/(Cp - R)
37
Cp/Cv
38
Heat of Vap.
39
Kinematic Viscosity
40
Liq. Mass Density (Std. Cond)
41
Liq. Vol. Flow (Std. Cond)
42
Liquid Fraction
43
Molar Volume
44
Mass Heat of Vap.
45
Phase Fraction [Molar Basis]
46
Surface Tension
47
Thermal Conductivity
48
Viscosity
49
Cv (Semi-Ideal)
50
Mass Cv (Semi-Ideal)
51
Cv
52
Mass Cv
53
Cv (Ent. Method)
54
Mass Cv (Ent. Method)
55
Cp/Cv (Ent. Method)
56
Reid VP at 37.8 C
57
True VP at 37.8 C
58
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
59
Viscosity Index
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
---
0.9856
0.9856
10.10
10.10
---
---
0.0000
---
1.266
1.266
1.295
1.295
3.130e+004 4.652 62.38 1.862e+005
--4.652 62.38 1.862e+005
0.0000
0.0000
(ft3/lbmole)
60.98
60.98
(Btu/lb)
1739
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
3.954e-002
3.954e-002
2.200e-002
2.200e-002
7.465
7.465
0.4147
0.4147
7.300
7.300
0.4056
0.4056
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.862e+005 -2.091
60
1.862e+005 ---
COMPOSITION
61 62
Overall Phase
63 64
COMPONENTS
65
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
66
CO
139.8961
0.0009
67
H2O
148599.0282
0.9844
68
Oxygen
135.4346
0.0009
69
Aspen Technology Inc. Licensed to: LEGENDS
MASS FLOW (lb/hr) 3918.6150 2.677026425e+06 4333.9059
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0014
335.6551
0.0018
0.9853
183673.4882
0.9702
0.0016
260.8421
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0014
Page 76 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 26 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14 15
Methane
16
H2S
17
Hydrogen
18
Ethane
19
Propane
20
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
1156.4711
0.0077
2331.4459
0.0009
2285.1811
0.0121
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
CO2
288.0576
0.0019
12677.3302
0.0047
1051.7579
0.0056
21
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
22
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Total
150949.1460
1.0000
27
2.717102502e+06
1.0000
189315.9286
Vapour Phase
28 29
COMPONENTS
30
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
1.0000
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0014
335.6551
0.0018
0.9853
183673.4882
0.9702
31
CO
139.8961
0.0009
32
H2O
148599.0282
0.9844
33
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
34
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
35
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Hydrogen
1156.4711
0.0077
2331.4459
0.0009
2285.1811
0.0121
37
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
38
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
CO2
288.0576
0.0019
12677.3302
0.0047
1051.7579
0.0056
40
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
41
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Total
150949.1460
3918.6150 2.677026425e+06
1.0000
2.717102502e+06
46
189315.9286
1.0000
K VALUE
47 48
1.0000
COMPONENTS
MIXED
LIGHT
HEAVY
49
CO
---
---
---
50
H2O
---
---
---
51
Oxygen
---
---
---
52
Methane
---
---
---
---
---
---
53
H2S
54
Hydrogen
---
---
---
55
Ethane
---
---
---
56
Propane
---
---
---
57
CO2
---
---
---
58
Nitrogen
---
---
---
---
---
---
59
Air
60
Mercury
---
---
---
61
MEAmine
---
---
---
62
Ammonia
---
---
---
63
UNIT OPERATIONS
64 65 66
FEED TO Conversion Reactor:
PRODUCT FROM D-2 Convertidor de CO2-1 LNG:
LOGICAL CONNECTION
E-1 PRECALENTADOR DE GAS-VAPOR DE PROCESO
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 77 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 26 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Inactive):
18
Flow Specification
(Inactive) Molar:
244.7 psia 1.509e+005 lbmole/hr Mass:
19
2.717e+006 lb/hrStd Ideal Liq Volume: 1.893e+005 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: 27
28 29 30
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
39
Molar Enthalpy
(Btu/lbmole)
40
Molar Entropy
(Btu/lbmole-F)
41
Heat Flow
42
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
700.0
700.0
700.0
(psia)
241.7
241.7
241.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-9.774e+004
-9.774e+004
0.0000 -9.774e+004
42.29
42.29
42.29
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
43
PROPERTIES
44 45
Overall
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Vapour Phase 18.00
(lbmole/ft3)
1.999e-002
Liquid Phase 18.00 1.999e-002
0.3599
0.3599
0.3599
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-5430
-5430
-5430
51
Mass Entropy
(Btu/lb-F)
2.349
2.349
2.349
52
Heat Capacity
9.167
9.167
9.167
53
Mass Heat Capacity
0.5092
0.5092
0.5092
54
LHV Molar Basis (Std)
(Btu/lbmole)
55
HHV Molar Basis (Std)
(Btu/lbmole)
56
HHV Mass Basis (Std)
57
CO2 Loading
58
CO2 App ML Con
59
CO2 App WT Con
60
LHV Mass Basis (Std)
61
Phase Fraction [Vol. Basis]
62
Phase Fraction [Mass Basis]
63
Phase Fraction [Act. Vol. Basis]
64
Mass Exergy
65
Partial Pressure of CO2
66
Cost Based on Flow
67
Act. Gas Flow
68
Avg. Liq. Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
1.999e-002
18.00
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1211 1.873e+004
1211 1.873e+004
1211 1.873e+004
1041
1041
1041
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
67.27
67.27
67.27
---
---
1.000
0.0000
0.0000
1.000
---
---
---
(Btu/lb)
454.5
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
---
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 78 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 27 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Specific Heat
(Btu/lbmole-F)
9.167
9.167
9.167
13
Std. Gas Flow
(MMSCFD)
0.0000
0.0000
0.0000
14
Std. Ideal Liq. Mass Density
(lb/ft3)
61.32
61.32
61.32
15
Act. Liq. Flow
(USGPS)
0.0000
---
0.0000
16
Z Factor
17
Watson K
18
User Property
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
41
True VP at 37.8 C
42 43
(psia)
(Btu/lbmole) (cSt)
---
0.9715
0.9715
10.22
10.22
10.22
---
---
---
0.0000
---
---
1.277
1.277
1.277
1.328
1.328
1.328
3.129e+004 0.6239
(lb/ft3) (barrel/day)
---
---
3.029
0.6239
62.37
62.37
62.37
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
50.02
50.02
50.02
(Btu/lb)
1739
---
---
0.0000
0.0000
1.0000
---
0.3093
(dyne/cm)
0.3093
(Btu/hr-ft-F)
0.1928
(cP)
3.597e-003
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
3.103e-002 1.746e-002
0.1928 3.597e-003
7.181
7.181
7.181
0.3989
0.3989
0.3989
6.905
6.905
6.905
0.3836
0.3836
0.3836
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-4.143
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
44
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
50
CO
0.0000
0.0006
0.0000
0.0009
0.0000
0.0012
51
H2O
0.0000
0.9841
0.0000
0.9849
0.0000
0.9694
52
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
53
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
54
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Hydrogen
0.0000
0.0080
0.0000
0.0009
0.0000
0.0126
56
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
57
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
CO2
0.0000
0.0022
0.0000
0.0055
0.0000
0.0065
59
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
60
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 79 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 27 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0006
0.0000
0.0009
0.0000
0.0012
16
H2O
0.0000
0.9841
0.0000
0.9849
0.0000
0.9694
17
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
18
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0080
0.0000
0.0009
0.0000
0.0126
21
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0022
0.0000
0.0055
0.0000
0.0065
24
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0006
0.0000
0.0009
0.0000
0.0012
35
H2O
0.0000
0.9841
0.0000
0.9849
0.0000
0.9694
36
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
37
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0080
0.0000
0.0009
0.0000
0.0126
40
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0022
0.0000
0.0055
0.0000
0.0065
43
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
1.000
1.000
---
53
H2O
1.000
1.000
---
54
Oxygen
1.000
1.000
---
55
Methane
1.000
1.000
---
---
---
---
56
H2S
57
Hydrogen
1.000
1.000
---
58
Ethane
1.000
1.000
---
59
Propane
---
---
---
60
CO2
1.000
1.000
---
61
Nitrogen
1.000
1.000
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 80 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 27 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Conversion Reactor:
13
LOGICAL CONNECTION
D-2 Convertidor de CO2-1
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
241.7 psia 0.0000 lbmole/hrMass:
23
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 28
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
1.0000
1.0000
0.0000
(F)
700.0*
700.0
700.0
(psia)
241.7
241.7
(lbmole/hr) (lb/hr)
241.7
1.509e+005
1.509e+005
0.0000
2.717e+006
2.717e+006
0.0000
1.894e+005
1.894e+005
-9.774e+004
-9.774e+004
42.29
42.29
0.0000 -9.774e+004 42.29
(Btu/hr)
-1.475e+010
-1.475e+010
0.0000
(barrel/day)
* 1.862e+005
1.862e+005
0.0000
47
PROPERTIES
48 49
Overall
Vapour Phase
Liquid Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-5430
-5430
-5430
55
Mass Entropy
(Btu/lb-F)
2.349
2.349
2.349
56
Heat Capacity
9.167
9.167
9.167
57
Mass Heat Capacity
0.5092
0.5092
0.5092
58
LHV Molar Basis (Std)
(Btu/lbmole)
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66 67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
0.3599 3.228e+007
1211 1.873e+004
1.999e-002 0.3599 3.228e+007
1211 1.873e+004
18.00 1.999e-002 0.3599 0.0000
1211 1.873e+004
1041
1041
1041
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
67.27
67.27
67.27
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
454.5
---
---
Licensed to: LEGENDS
(Btu/lb)
1.999e-002
18.00
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 81 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 28 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Liquid Phase
(psia)
0.5396
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1.258e+005
1.258e+005
---
(lbmole/ft3)
3.407
3.407
Specific Heat
(Btu/lbmole-F)
9.167
9.167
9.167
Std. Gas Flow
(MMSCFD)
1372
1372
0.0000
(lb/ft3)
61.32
61.32
61.32
(USGPS)
---
---
---
---
0.9715
0.9715
10.22
10.22
10.22
---
---
---
0.0000
---
---
1.277
1.277
1.277
1.328
1.328
1.328
(psia)
(Btu/lbmole) (cSt)
3.129e+004 3.029
(lb/ft3)
62.37
(barrel/day)
1.862e+005
3.407
---
---
3.029
0.6239
62.37 1.862e+005
62.37 0.0000
0.0000
0.0000
1.000
(ft3/lbmole)
50.02
50.02
50.02
(Btu/lb)
1739
---
---
1.0000
1.0000
0.0000
---
0.3093
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
--3.103e-002
3.103e-002
1.746e-002
1.746e-002
0.1928 3.597e-003
7.181
7.181
7.181
0.3989
0.3989
0.3989
6.905
6.905
6.905
0.3836
0.3836
0.3836
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
1.862e+005 -4.143
48
1.862e+005 ---
--0.0000 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53 54
CO
55
H2O
56
MOLAR FLOW (lbmole/hr) 90.9324
MOLE FRACTION 0.0006
MASS FLOW (lb/hr) 2547.0997
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
57
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
60
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
63
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
69
Aspen Technology Inc. Licensed to: LEGENDS
150949.1460
1.0000
2.676144340e+06
Vapour Fraction
2.717102487e+06
1.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
189413.4567
1.0000
Page 82 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 28 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14 15
CO
16
H2O
17
MOLAR FLOW (lbmole/hr) 90.9324
MOLE FRACTION
MASS FLOW (lb/hr)
0.0006
2547.0997
MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
18
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
21
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
24
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
150949.1460
2.676144340e+06
Phase Fraction
1.0000
30
2.717102487e+06
1.0000
189413.4567
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0006
0.0000
0.0009
0.0000
0.0012
35
H2O
0.0000
0.9841
0.0000
0.9849
0.0000
0.9694
36
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
37
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0080
0.0000
0.0009
0.0000
0.0126
40
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0022
0.0000
0.0055
0.0000
0.0065
43
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0066
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
1.000
1.000
---
53
H2O
1.000
1.000
---
54
Oxygen
1.000
1.000
---
55
Methane
1.000
1.000
---
---
---
---
56
H2S
57
Hydrogen
1.000
1.000
---
58
Ethane
1.000
1.000
---
59
Propane
---
---
---
60
CO2
1.000
1.000
---
61
Nitrogen
1.000
1.000
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 83 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 28 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
LNG:
LNG-100 Conversion Reactor:
13
LOGICAL CONNECTION
D-2 Convertidor de CO2-1
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
241.7 psia 1.509e+005 lbmole/hr Mass:
23
2.717e+006 lb/hrStd Ideal Liq Volume: 1.894e+005 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 29
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
1.894e+005
1.894e+005
43
Molar Enthalpy
(Btu/lbmole)
-9.778e+004
-9.778e+004
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
695.0
695.0
(psia)
241.7
(lbmole/hr) (lb/hr)
241.7
1.509e+005
1.509e+005
2.717e+006
2.717e+006
42.25
42.25
(Btu/hr)
-1.476e+010
-1.476e+010
(barrel/day)
* 1.862e+005
1.862e+005
47
PROPERTIES
48 49
Overall
Vapour Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-5432
-5432
55
Mass Entropy
(Btu/lb-F)
2.347
2.347
56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
0.3616 3.212e+007
18.00 2.009e-002 0.3616 3.212e+007
9.162
9.162
0.5090
0.5090
1211 1.873e+004
1211 1.873e+004
1041
1041
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
67.27
67.27
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
67
Phase Fraction [Act. Vol. Basis]
1.000
1.000
68
Mass Exergy
453.1
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
2.009e-002
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 84 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 29 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Vapour Phase
(psia)
0.5396
---
(Cost/s)
0.0000
0.0000
(ACFM)
1.253e+005
1.253e+005
(lbmole/ft3)
3.407
3.407
Specific Heat
(Btu/lbmole-F)
9.162
9.162
17
Std. Gas Flow
(MMSCFD)
1372
1372
18
Std. Ideal Liq. Mass Density
61.32
61.32
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt)
---
---
0.9711
0.9711
10.22
10.22
---
---
0.0000
---
1.277
1.277
1.328
1.328
3.129e+004 3.000
(lb/ft3)
62.37
(barrel/day)
1.862e+005
--3.000 62.37 1.862e+005
0.0000
0.0000
(ft3/lbmole)
49.79
49.79
(Btu/lb)
1739
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
3.086e-002
3.086e-002
1.737e-002
1.737e-002
7.176
7.176
0.3987
0.3987
6.897
6.897
0.3832
0.3832
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.862e+005 -4.197
48
1.862e+005 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53 54
CO
55
H2O
56
MOLAR FLOW (lbmole/hr) 90.9324
MOLE FRACTION 0.0006
MASS FLOW (lb/hr) 2547.0997
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
57
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
60
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
63
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
69
Aspen Technology Inc. Licensed to: LEGENDS
150949.1460
1.0000
2.676144340e+06
Vapour Fraction
2.717102487e+06
1.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
189413.4567
1.0000
Page 85 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 29 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14 15
CO
16
H2O
17
MOLE FRACTION
90.9324
MASS FLOW (lb/hr)
0.0006
Phase Fraction MASS FRACTION
2547.0997
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
18
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
21
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
24
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
150949.1460
2.676144340e+06
1.000
1.0000
2.717102487e+06
30
1.0000
189413.4567
1.0000
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Cooler:
E-100
51
LNG:
LOGICAL CONNECTION LNG-100
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Inactive) Molar:
61
241.7 psia 1.509e+005 lbmole/hr Mass:
2.717e+006 lb/hrStd Ideal Liq Volume: 1.894e+005 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 86 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 30
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Vapour Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
1.894e+005
1.894e+005
18
Molar Enthalpy
(Btu/lbmole)
-9.980e+004
-9.980e+004
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
473.0*
473.0
(psia)
241.7
(lbmole/hr) (lb/hr)
241.7
1.509e+005
1.509e+005
2.717e+006
2.717e+006
40.31
40.31
(Btu/hr)
-1.506e+010
-1.506e+010
(barrel/day)
* 1.862e+005
1.862e+005
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-5544
-5544
30
Mass Entropy
(Btu/lb-F)
2.240
2.240
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
34
HHV Molar Basis (Std)
(Btu/lbmole)
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.563e-002 0.4614 2.517e+007
18.00 2.563e-002 0.4614 2.517e+007
9.047
9.047
0.5026
0.5026
1211 1.873e+004
1211 1.873e+004
1041
1041
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
67.27
67.27
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
(Btu/lb)
398.9
---
44
Partial Pressure of CO2
(psia)
0.5396
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48
(ACFM)
9.815e+004
9.815e+004
(lbmole/ft3)
3.407
3.407
Specific Heat
(Btu/lbmole-F)
9.047
9.047
49
Std. Gas Flow
(MMSCFD)
1372
1372
50
Std. Ideal Liq. Mass Density
61.32
61.32
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
---
0.9421
0.9421
10.22
10.22
---
---
0.0000
---
1.281
1.281
1.379
1.379
3.129e+004 1.844 62.37 1.862e+005
--1.844 62.37 1.862e+005
0.0000
0.0000
(ft3/lbmole)
39.01
39.01
(Btu/lb)
1739
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
2.346e-002
2.346e-002
1.363e-002
1.363e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 87 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 30 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 7.062
7.062
0.3923
0.3923
6.563
6.563
0.3646
0.3646
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.862e+005
1.862e+005
---
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28 29
CO
30
H2O
31
MOLAR FLOW (lbmole/hr) 90.9324
MOLE FRACTION
MASS FLOW (lb/hr)
0.0006
2547.0997
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
32
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
35
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
38
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
150949.1460
2.676144340e+06
Vapour Fraction
1.0000
44
2.717102487e+06
1.0000
189413.4567
Vapour Phase
45 46
COMPONENTS
47 48
CO
49
H2O
50
MOLAR FLOW (lbmole/hr) 90.9324
MOLE FRACTION 0.0006
MASS FLOW (lb/hr) 2547.0997
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0009
218.1758
0.0012
0.9849
183612.9675
0.9694
148550.0646
0.9841
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
51
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
1205.4348
0.0080
2430.1565
0.0009
2381.9330
0.0126
54
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
337.0213
0.0022
14832.2047
0.0055
1230.5343
0.0065
57
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0066
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
150949.1460
1.0000
63
2.717102487e+06
1.0000
189413.4567
1.0000
K VALUE
64 65
2.676144340e+06
1.0000
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 88 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 30 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO Conversion Reactor:
PRODUCT FROM
LOGICAL CONNECTION
D-2B Convertidor de CO2 Cooler:
E-100
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
241.7 psia 1.509e+005 lbmole/hr Mass:
37
2.717e+006 lb/hrStd Ideal Liq Volume: 1.894e+005 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 31
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.0000
0.0000
1.0000
(F)
472.5
472.5
472.5
(psia)
235.7
235.7
235.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-1.152e+005
-9.980e+004
0.0000 -1.152e+005
23.69
40.36
23.69
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 18.02
(lbmole/ft3) (lb/ft3)
2.265
18.00 2.497e-002
Aqueous Phase 18.02 2.265
40.80
0.4495
40.80
(barrel/day)
0.0000
0.0000
0.0000
(Btu/lb)
-6394
-5544
-6394
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 89 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 31 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
(Btu/lb-F)
Vapour Phase
Aqueous Phase
1.315
2.242
1.315
23.44
9.031
23.44
(Btu/lb-F)
1.301
0.5017
1.301
LHV Molar Basis (Std)
(Btu/lbmole)
2.104
1207
16
HHV Molar Basis (Std)
(Btu/lbmole)
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
Phase Fraction [Vol. Basis]
23
Phase Fraction [Mass Basis]
24
Phase Fraction [Act. Vol. Basis]
25
Mass Exergy
26
Partial Pressure of CO2
27
Cost Based on Flow
28
Act. Gas Flow
29
Avg. Liq. Density
30
(Btu/lbmole-F)
(Btu/lb)
1.763e+004
1.873e+004
2.104 1.763e+004
978.8
1040
978.8
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
0.1168
67.07
0.1168
---
---
1.000
0.0000
0.0000
1.000
---
---
---
(Btu/lb)
113.2
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
23.44
9.031
23.44
31
Std. Gas Flow
(MMSCFD)
0.0000
32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
0.0000
0.0000
(lb/ft3)
62.30
61.30
62.30
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt)
---
0.9435
9.468
10.30
9.468
---
---
---
0.0000
---
---
1.093
1.282
1.093
1.093
1.377
1.093
1.529e+004 0.1672
(lb/ft3)
1.040e-002
---
---
1.891
0.1672
63.35
62.36
63.35
(barrel/day)
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
0.4415
40.04
0.4415
(Btu/lb)
848.5
---
---
0.0000
0.0000
1.0000
(dyne/cm)
27.39
(Btu/hr-ft-F)
0.3597
2.343e-002
0.3597
0.1093
1.362e-002
0.1093
(cP) (Btu/lbmole-F)
---
27.39
21.46
7.045
21.46
1.191
0.3914
1.191
21.46
6.561
21.46
1.191
0.3645
1.191
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
253.6
---
253.6
0.0000
0.0000
0.0000
---
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
0.0000
LIQUID VOLUME FRACTION 0.0000
Page 90 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 31 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
H2O
0.0000
1.0000
0.0000
0.9999
0.0000
0.9999
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0004
0.0000
0.0006
0.0000
0.0007
34
H2O
0.0000
0.9839
0.0000
0.9847
0.0000
0.9688
35
Oxygen
0.0000
0.0009
0.0000
0.0016
0.0000
0.0014
36
Methane
0.0000
0.0005
0.0000
0.0004
0.0000
0.0015
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0082
0.0000
0.0009
0.0000
0.0129
39
Ethane
0.0000
0.0002
0.0000
0.0004
0.0000
0.0010
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0000
0.0024
0.0000
0.0060
0.0000
0.0071
42
Nitrogen
0.0000
0.0035
0.0000
0.0054
0.0000
0.0065
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
48
Aqueous Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
52
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
H2O
0.0000
1.0000
0.0000
0.9999
0.0000
0.9999
54
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 91 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 31 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
572.4
---
572.4
13
H2O
0.9839
---
0.9839
14
Oxygen
309.2
---
309.2
15
Methane
1890
---
1890
---
---
---
Hydrogen
448.4
---
448.4
18
Ethane
4838
---
4838
19
Propane
---
---
---
20
CO2
150.1
---
150.1
21
Nitrogen
912.9
---
912.9
---
---
---
16
H2S
17
22
Air
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Conversion Reactor:
30
LOGICAL CONNECTION
D-2B Convertidor de CO2
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
235.7 psia 0.0000 lbmole/hrMass:
40
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 32
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
1.0000
1.0000
0.0000
(F)
472.5
472.5
472.5
(psia)
235.7
235.7
(lbmole/hr) (lb/hr)
235.7
1.509e+005
1.509e+005
0.0000
2.717e+006
2.717e+006
0.0000
1.895e+005
1.895e+005
-9.980e+004
-9.980e+004
40.36
40.36
0.0000 -1.152e+005 23.69
(Btu/hr)
-1.506e+010
-1.506e+010
0.0000
(barrel/day)
* 1.863e+005
1.863e+005
0.0000
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 18.00
(lbmole/ft3)
2.497e-002
18.00 2.497e-002
Aqueous Phase 18.02 2.265
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 92 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 32 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-5544
-5544
-6394
15
Mass Entropy
(Btu/lb-F)
2.242
2.242
1.315
16
Heat Capacity
9.031
9.031
23.44
17
Mass Heat Capacity
(Btu/lb-F)
0.5017
0.5017
1.301
18
LHV Molar Basis (Std)
(Btu/lbmole)
1207
1207
19
HHV Molar Basis (Std)
(Btu/lbmole)
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26 27
Phase Fraction [Act. Vol. Basis]
28
Mass Exergy
29
Partial Pressure of CO2
30
Cost Based on Flow
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
(Btu/lbmole-F)
(Btu/lb)
0.4495 2.584e+007
1.873e+004
0.4495 2.584e+007
1.873e+004
40.80 0.0000
2.104 1.763e+004
1040
1040
978.8
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
67.07
67.07
0.1168
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
397.5
---
---
(psia)
0.5759
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1.007e+005
1.007e+005
---
(lbmole/ft3)
3.405
3.405
Specific Heat
(Btu/lbmole-F)
9.031
9.031
23.44
Std. Gas Flow
(MMSCFD)
1372
1372
0.0000
(lb/ft3)
61.30
61.30
62.30
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F)
3.458
---
0.9435
10.30
10.30
9.468
---
---
---
0.0000
---
---
1.282
1.282
1.093
1.377
1.377
1.093
3.004e+004 1.891 62.36 1.863e+005
1.040e-002
---
---
1.891
0.1672
62.36 1.863e+005
63.35 0.0000
0.0000
0.0000
1.000
40.04
40.04
0.4415
1669
---
---
1.0000
1.0000
0.0000
---
---
27.39
2.343e-002
2.343e-002
0.3597
1.362e-002
1.362e-002
0.1093
7.045
7.045
21.46
0.3914
0.3914
1.191
6.561
6.561
21.46
0.3645
0.3645
1.191
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
253.6
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
1.863e+005 ---
1.863e+005 ---
0.0000 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 93 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 32 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14 15
CO
16
H2O
17
MOLAR FLOW (lbmole/hr) 59.1061
MOLE FRACTION 0.0004
MASS FLOW (lb/hr) 1655.6148
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0006
141.8143
0.0007
0.9847
183573.6290
0.9688
148518.2382
0.9839
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
18
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1237.2611
0.0082
2494.3185
0.0009
2444.8217
0.0129
21
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
368.8476
0.0024
16232.8731
0.0060
1346.7389
0.0071
24
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0065
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
150949.1460
2.675570985e+06
Vapour Fraction
1.0000
2.717102478e+06
30
1.0000
Vapour Phase
31 32
COMPONENTS
33 34
CO
35
H2O
36
MOLAR FLOW (lbmole/hr) 59.1061
MOLE FRACTION 0.0004
MASS FLOW (lb/hr) 1655.6148
Phase Fraction MASS FRACTION
1.0000 1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0006
141.8143
0.0007
0.9847
183573.6290
0.9688
148518.2382
0.9839
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
37
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1237.2611
0.0082
2494.3185
0.0009
2444.8217
0.0129
40
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
368.8476
0.0024
16232.8731
0.0060
1346.7389
0.0071
43
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0065
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
150949.1460
2.675570985e+06
189476.8501
1.0000
49
2.717102478e+06
1.0000
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
189476.8501 Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000 0.0000 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
0.0000
1.0000
0.0000
0.9999
0.0000
0.9999
55
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 94 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 32 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
572.4
---
572.4
13
H2O
0.9839
---
0.9839
14
Oxygen
309.2
---
309.2
15
Methane
1890
---
1890
---
---
---
Hydrogen
448.4
---
448.4
18
Ethane
4838
---
4838
19
Propane
---
---
---
20
CO2
150.1
---
150.1
21
Nitrogen
912.9
---
912.9
---
---
---
16
H2S
17
22
Air
23
Mercury
---
---
---
24
MEAmine
---
---
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Valve:
VLV-100 Conversion Reactor:
30
LOGICAL CONNECTION
D-2B Convertidor de CO2
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
235.7 psia 1.509e+005 lbmole/hr Mass:
40
2.717e+006 lb/hrStd Ideal Liq Volume: 1.895e+005 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 33
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
1.895e+005
1.895e+005
60
Molar Enthalpy
(Btu/lbmole)
-9.980e+004
-9.980e+004
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
471.9
471.9
(psia)
231.7*
(lbmole/hr) (lb/hr)
231.7
1.509e+005
1.509e+005
2.717e+006
2.717e+006
40.39
40.39
(Btu/hr)
-1.506e+010
-1.506e+010
(barrel/day)
* 1.863e+005
1.863e+005
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 18.00
(lbmole/ft3)
2.454e-002
18.00 2.454e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 95 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 33 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-5544
-5544
15
Mass Entropy
(Btu/lb-F)
2.244
2.244
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
19
HHV Molar Basis (Std)
(Btu/lbmole)
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.4417 2.629e+007
0.4417 2.629e+007
9.020
9.020
0.5011
0.5011
1207 1.873e+004
1207 1.873e+004
1040
1040
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
67.07
67.07
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
27
Phase Fraction [Act. Vol. Basis]
1.000
1.000
28
Mass Exergy
(Btu/lb)
396.6
---
29
Partial Pressure of CO2
(psia)
0.5662
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33
(ACFM)
1.025e+005
1.025e+005
(lbmole/ft3)
3.405
3.405
Specific Heat
(Btu/lbmole-F)
9.020
9.020
34
Std. Gas Flow
(MMSCFD)
1372
1372
35
Std. Ideal Liq. Mass Density
61.30
61.30
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
---
0.9444
0.9444
10.30
10.30
---
---
0.0000
---
1.282
1.282
1.375
1.375
3.012e+004 1.922 62.36 1.863e+005
--1.922 62.36 1.863e+005
0.0000
0.0000
(ft3/lbmole)
40.75
40.75
(Btu/lb)
1673
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
2.339e-002
2.339e-002
1.360e-002
1.360e-002
7.034
7.034
0.3908
0.3908
6.559
6.559
0.3644
0.3644
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.863e+005 ---
1.863e+005 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 96 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 33 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14 15
CO
16
H2O
17
MOLAR FLOW (lbmole/hr) 59.1061
MOLE FRACTION
MASS FLOW (lb/hr)
0.0004
1655.6148
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0006
141.8143
0.0007
0.9847
183573.6290
0.9688
148518.2382
0.9839
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
18
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1237.2611
0.0082
2494.3185
0.0009
2444.8217
0.0129
21
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
368.8476
0.0024
16232.8731
0.0060
1346.7389
0.0071
24
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0065
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
150949.1460
2.675570985e+06
Vapour Fraction
1.0000
30
2.717102478e+06
1.0000
189476.8501
Vapour Phase
31 32
COMPONENTS
33 34
CO
35
H2O
36
MOLAR FLOW (lbmole/hr) 59.1061
MOLE FRACTION 0.0004
MASS FLOW (lb/hr) 1655.6148
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0006
141.8143
0.0007
0.9847
183573.6290
0.9688
148518.2382
0.9839
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
37
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1237.2611
0.0082
2494.3185
0.0009
2444.8217
0.0129
40
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
368.8476
0.0024
16232.8731
0.0060
1346.7389
0.0071
43
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0065
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
150949.1460
1.0000
49
2.717102478e+06
1.0000
189476.8501
1.0000
K VALUE
50 51
2.675570985e+06
1.0000
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 97 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 33 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Cooler:
E-102
LOGICAL CONNECTION
Valve:
VLV-100
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 231.7 psia
1.509e+005 lbmole/hr Mass:
23
2.717e+006 lb/hrStd Ideal Liq Volume: 1.895e+005 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 34
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
1.895e+005
43
Molar Enthalpy
(Btu/lbmole)
-1.209e+005
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Aqueous Phase
0.0156
0.0156
0.9844
(F)
110.0*
110.0
110.0
(psia)
231.7
231.7
(lbmole/hr) (lb/hr)
1.509e+005 2.717e+006
14.21
2349 3.772e+004 5579 -2.337e+004 31.06
231.7 1.486e+005 2.679e+006 1.839e+005 -1.225e+005 13.95
(Btu/hr)
-1.825e+010
-5.490e+007
-1.820e+010
(barrel/day)
* 1.863e+005
3.801e+006
1.807e+005
47
PROPERTIES
48 49
Overall
Vapour Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-6717
-1455
-6791
55
Mass Entropy
(Btu/lb-F)
0.7896
1.934
0.7735
56
Heat Capacity
57
Mass Heat Capacity
58
18.00 (lbmole/ft3) (lb/ft3) (barrel/day)
25.88 4.488e+005
3.799e-002 0.6102 2.642e+005
18.03 3.442 62.06 1.846e+005
18.39
7.432
18.57
(Btu/lb-F)
1.022
0.4628
1.030
LHV Molar Basis (Std)
(Btu/lbmole)
1207
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
(lbmole/ft3)
63
CO2 App WT Con
(lbmol/lb)
64
LHV Mass Basis (Std)
(Btu/lb)
65
Phase Fraction [Vol. Basis]
2.945e-002
2.945e-002
0.9706
66
Phase Fraction [Mass Basis]
1.388e-002
1.388e-002
0.9861
67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lbmole-F)
1.438
16.06
(Btu/lb)
(Btu/lb)
1.873e+004
7.748e+004 8.874e+004
1.714 1.762e+004
1040
5525
---
---
977.3
---
---
2.053e-003
---
---
3.308e-005
67.07
4824
9.508e-002
---
0.5888
0.5888
0.4112
4.357
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 98 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 34 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Aqueous Phase
(psia)
27.64
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1030
1030
---
(lbmole/ft3)
3.405
1.799
3.454
Specific Heat
(Btu/lbmole-F)
18.39
7.432
18.57
Std. Gas Flow
(MMSCFD)
1372
21.35
1351
(lb/ft3)
61.30
28.90
62.28
(USGPS)
89.72
---
---
0.9975
10.30
10.51
8.466
---
---
---
0.0000
---
---
1.121
1.365
1.120
1.002
1.391
1.157
(psia)
(Btu/lbmole) (cSt)
3.012e+004 ---
(lb/ft3)
62.36
(barrel/day) (ft3/lbmole) (Btu/lb)
1.863e+005
89.72 1.101e-002
---
---
1.395
0.6158
4.242e-002 3.801e+006
63.37 1.807e+005
0.9844
0.0000
1.000
0.6955
26.32
0.2905
1673
---
---
0.0156
0.0156
0.9844
(dyne/cm)
68.86
(Btu/hr-ft-F)
---
4.305e-002
0.3672
---
1.363e-002
0.6121
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
68.86
16.41
5.447
16.58
0.9116
0.3391
0.9197
18.35
5.345
16.05
1.019
0.3328
0.8900
---
---
15.85
---
---
0.8789
---
---
1.172
---
---
---
---
---
232.7
3.982e+006 -4.417
48
3.801e+006 ---
1.807e+005 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53 54
CO
55
H2O
56
MOLAR FLOW (lbmole/hr) 59.1061
MOLE FRACTION 0.0004
MASS FLOW (lb/hr) 1655.6148
MASS FRACTION
0.0156
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
0.0006
141.8143
0.0007
0.9847
183573.6290
0.9688
148518.2382
0.9839
Oxygen
135.4346
0.0009
4333.9059
0.0016
260.8421
0.0014
57
Methane
75.8678
0.0005
1217.1398
0.0004
278.3656
0.0015
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1237.2611
0.0082
2494.3185
0.0009
2444.8217
0.0129
60
Ethane
32.8159
0.0002
986.7714
0.0004
189.9642
0.0010
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
368.8476
0.0024
16232.8731
0.0060
1346.7389
0.0071
63
Nitrogen
521.5746
0.0035
14610.8690
0.0054
1240.6743
0.0065
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
69
Aspen Technology Inc. Licensed to: LEGENDS
150949.1460
1.0000
2.675570985e+06
Vapour Fraction
2.717102478e+06
1.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
189476.8501
1.0000
Page 99 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 34 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.556e-002
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
16
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
17
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
18
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
21
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
24
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
30
37720.7641
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9844 LIQUID VOLUME FRACTION
34
CO
35
H2O
36
Oxygen
0.6059
0.0000
19.3875
0.0000
1.1669
0.0000
37
Methane
0.0012
0.0000
0.0186
0.0000
0.0043
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
2.2934
0.0000
4.6235
0.0000
4.5317
0.0000
40
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
88.6369
0.0006
3900.8838
0.0015
323.6317
0.0018
43
Nitrogen
5.0873
0.0000
142.5111
0.0001
12.1013
0.0001
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.1299 148503.7872
148600.5418
0.0000 0.9993
1.0000
49
2.679381713e+06
0.0000
0.3118
0.9985
0.0000
183555.7671
1.0000
0.9981
183897.5147
1.0000
K VALUE
50 51
3.6398 2.675310649e+06
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
2.872e+004
---
53
H2O
6.157e-003
---
6.157e-003
54
Oxygen
1.408e+004
---
1.408e+004
55
Methane
4.136e+006
---
4.136e+006
56
H2S
57
---
---
2.872e+004
---
Hydrogen
3.407e+004
---
3.407e+004
58
Ethane
1.389e+008
---
1.389e+008
59
Propane
---
---
---
60
CO2
200.0
---
200.0
61
Nitrogen
6424
---
6424
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 100 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 34 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Separator:
D-10
LOGICAL CONNECTION
Cooler:
E-102
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
231.7 psia 1.509e+005 lbmole/hr Mass:
23
2.717e+006 lb/hrStd Ideal Liq Volume: 1.895e+005 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 35
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
1.0000
1.0000
0.0000
(F)
110.0
110.0
110.0
(psia)
231.7
231.7
231.7
2349
2349
0.0000
(lbmole/hr) (lb/hr)
3.772e+004 5579 -2.337e+004 31.06
3.772e+004 5579 -2.337e+004 31.06
0.0000 0.0000 -1.225e+005 13.95
(Btu/hr)
-5.490e+007
-5.490e+007
0.0000
(barrel/day)
* 3.801e+006
3.801e+006
0.0000
47
PROPERTIES
48 49
Overall
Vapour Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-1455
-1455
-6791
55
Mass Entropy
(Btu/lb-F)
1.934
1.934
0.7735
56
Heat Capacity
7.432
7.432
18.57
57
Mass Heat Capacity
0.4628
0.4628
1.030
58
LHV Molar Basis (Std)
(Btu/lbmole)
7.748e+004
7.748e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
8.874e+004
8.874e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66 67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
16.06 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
0.6102 2.642e+005
3.799e-002 0.6102 2.642e+005
18.03 3.442 62.06 0.0000
1.714 1.762e+004
5525
5525
977.3
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
(Btu/lb)
4824
4824
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
183.2
---
---
Licensed to: LEGENDS
(Btu/lb)
3.799e-002
16.06
(Btu/lb)
--9.508e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 101 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 35 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Aqueous Phase
(psia)
27.64
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1030
1030
---
(lbmole/ft3)
1.799
1.799
3.454
Specific Heat
(Btu/lbmole-F)
7.432
7.432
18.57
Std. Gas Flow
(MMSCFD)
21.35
21.35
0.0000
(lb/ft3)
28.90
28.90
62.28
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
0.9975
10.51
10.51
1.101e-002 8.466
---
---
---
0.0000
---
---
1.365
1.365
1.120
1.391
1.391
1.157
5706
---
---
1.395
1.395
0.6158
4.242e-002
4.242e-002
63.37
3.801e+006
3.801e+006
0.0000
0.0000
0.0000
1.000
26.32
26.32
0.2905
355.3
---
---
1.0000
1.0000
0.0000
---
---
68.86
4.305e-002
4.305e-002
0.3672
1.363e-002
1.363e-002
0.6121
5.447
5.447
16.58
0.3391
0.3391
0.9197
5.345
5.345
16.05
0.3328
0.3328
0.8900
---
---
15.85
---
---
0.8789
---
---
1.172
---
---
---
---
---
232.7
3.801e+006 -30.38
48
3.801e+006 ---
0.0000 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
54
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
55
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
56
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
57
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
60
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
63
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
2348.6041
1.0000
1.0000
5579.3353
69
Aspen Technology Inc. Licensed to: LEGENDS
37720.7641
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 102 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 35 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
16
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
17
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
18
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
21
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
24
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
30
37720.7641
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.9993
0.0000
0.9985
0.0000
0.9981
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0006
0.0000
0.0015
0.0000
0.0018
43
Nitrogen
0.0000
0.0000
0.0000
0.0001
0.0000
0.0001
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
2.872e+004
---
53
H2O
6.157e-003
---
6.157e-003
54
Oxygen
1.408e+004
---
1.408e+004
55
Methane
4.136e+006
---
4.136e+006
56
H2S
57
---
---
2.872e+004
---
Hydrogen
3.407e+004
---
3.407e+004
58
Ethane
1.389e+008
---
1.389e+008
59
Propane
---
---
---
60
CO2
200.0
---
200.0
61
Nitrogen
6424
---
6424
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 103 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 35 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Cooler:
Cooler
LOGICAL CONNECTION
Separator:
13
D-10
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
231.7 psia 2349 lbmole/hrMass:
23
3.772e+004 lb/hrStd Ideal Liq Volume:
5579 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 36
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
-1.225e+005
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Aqueous Phase
0.0000
0.0000
1.0000
(F)
110.0
110.0
110.0
(psia)
231.7
231.7
(lbmole/hr) (lb/hr)
231.7
1.486e+005
0.0000
1.486e+005
2.679e+006
0.0000
2.679e+006
1.839e+005
0.0000
13.95
-2.337e+004 31.06
1.839e+005 -1.225e+005 13.95
(Btu/hr)
-1.820e+010
0.0000
-1.820e+010
(barrel/day)
* 1.807e+005
0.0000
1.807e+005
47
PROPERTIES
48 49
Overall
Vapour Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-6791
-1455
-6791
55
Mass Entropy
(Btu/lb-F)
0.7735
1.934
0.7735
56
Heat Capacity
57
Mass Heat Capacity
58
18.03 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F)
3.442 62.06 1.846e+005
16.06 3.799e-002 0.6102 0.0000
18.03 3.442 62.06 1.846e+005
18.57
7.432
18.57
(Btu/lb-F)
1.030
0.4628
1.030
LHV Molar Basis (Std)
(Btu/lbmole)
1.714
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
(lbmole/ft3)
2.053e-003
63
CO2 App WT Con
(lbmol/lb)
64
LHV Mass Basis (Std)
(Btu/lb)
65
Phase Fraction [Vol. Basis]
66
(Btu/lb)
1.762e+004
7.748e+004 8.874e+004
977.3
5525
---
---
1.714 1.762e+004 977.3 ---
---
2.053e-003
3.308e-005
---
3.308e-005
9.508e-002
4824
9.508e-002
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
67
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
68
Mass Exergy
1.785
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 104 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 36 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Aqueous Phase
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
3.454
1.799
3.454
Specific Heat
(Btu/lbmole-F)
18.57
7.432
18.57
Std. Gas Flow
(MMSCFD)
1351
0.0000
1351
(lb/ft3)
62.28
28.90
62.28
(USGPS)
89.72
---
---
0.9975
8.466
10.51
8.466
---
---
---
0.0000
---
---
1.120
1.365
1.120
1.157
1.391
1.157
(psia)
(Btu/lbmole) (cSt)
1.631e+004 0.6158
(lb/ft3)
63.37
(barrel/day) (ft3/lbmole) (Btu/lb)
1.807e+005
89.72 1.101e-002
---
---
1.395
0.6158
4.242e-002 0.0000
63.37 1.807e+005
1.000
0.0000
1.000
0.2905
26.32
0.2905
904.5
---
---
0.0000
0.0000
1.0000
(dyne/cm)
68.86
(Btu/hr-ft-F)
0.3672
4.305e-002
0.3672
0.6121
1.363e-002
0.6121
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
68.86
16.58
5.447
16.58
0.9197
0.3391
0.9197
16.05
5.345
16.05
0.8900
0.3328
0.8900
15.85
---
15.85
0.8789
---
0.8789
1.172
---
1.172
---
---
---
232.7
---
232.7
1.807e+005 -4.382
48
0.0000 ---
1.807e+005 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
54
CO
55
H2O
56
Oxygen
0.6059
0.0000
19.3875
0.0000
1.1669
0.0000
57
Methane
0.0012
0.0000
0.0186
0.0000
0.0043
0.0000
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
2.2934
0.0000
4.6235
0.0000
4.5317
0.0000
60
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
88.6369
0.0006
3900.8838
0.0015
323.6317
0.0018
63
Nitrogen
5.0873
0.0000
142.5111
0.0001
12.1013
0.0001
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
69
Aspen Technology Inc. Licensed to: LEGENDS
0.1299 148503.7872
148600.5418
0.0000 0.9993
1.0000
3.6398 2.675310649e+06
2.679381713e+06
0.0000 0.9985
1.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.3118 183555.7671
183897.5147
0.0000 0.9981
1.0000
Page 105 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 36 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0251
0.0000
0.0438
0.0000
0.0254
16
H2O
0.0000
0.0062
0.0000
0.0069
0.0000
0.0032
17
Oxygen
0.0000
0.0574
0.0000
0.1144
0.0000
0.0465
18
Methane
0.0000
0.0323
0.0000
0.0323
0.0000
0.0499
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.5258
0.0000
0.0660
0.0000
0.4374
21
Ethane
0.0000
0.0140
0.0000
0.0262
0.0000
0.0340
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.1193
0.0000
0.3269
0.0000
0.1834
24
Nitrogen
0.0000
0.2199
0.0000
0.3836
0.0000
0.2202
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
35
H2O
36
Oxygen
0.6059
0.0000
19.3875
0.0000
1.1669
0.0000
37
Methane
0.0012
0.0000
0.0186
0.0000
0.0043
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
2.2934
0.0000
4.6235
0.0000
4.5317
0.0000
40
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
88.6369
0.0006
3900.8838
0.0015
323.6317
0.0018
43
Nitrogen
5.0873
0.0000
142.5111
0.0001
12.1013
0.0001
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.1299 148503.7872
148600.5418
0.0000 0.9993
1.0000
49
2.679381713e+06
0.0000
0.3118
0.9985
0.0000
183555.7671
1.0000
0.9981
183897.5147
1.0000
K VALUE
50 51
3.6398 2.675310649e+06
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
2.872e+004
---
53
H2O
6.157e-003
---
6.157e-003
54
Oxygen
1.408e+004
---
1.408e+004
55
Methane
4.136e+006
---
4.136e+006
56
H2S
57
---
---
2.872e+004
---
Hydrogen
3.407e+004
---
3.407e+004
58
Ethane
1.389e+008
---
1.389e+008
59
Propane
---
---
---
60
CO2
200.0
---
200.0
61
Nitrogen
6424
---
6424
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 106 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 36 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Pump:
P-100
Separator:
13
LOGICAL CONNECTION D-10
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
231.7 psia 1.486e+005 lbmole/hr Mass:
23
User Variables
24 25
NOTES
26 27
2.679e+006 lb/hrStd Ideal Liq Volume: 1.839e+005 barrel/day
29285
28 29 30
(Last modified Mon Dec 17, 2018, 16:57)
31 32
Description
33 34 35
Material Stream: 37
36 37 38
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
39 40
Overall
41
Vapour / Phase Fraction
42
Temperature:
43
Pressure:
44
Molar Flow
45
Mass Flow
46
Std Ideal Liq Vol Flow
(barrel/day)
47
Molar Enthalpy
(Btu/lbmole)
48
Molar Entropy
(Btu/lbmole-F)
49
Heat Flow
50
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
110.0*
110.0
(psia)
229.7*
229.7
(lbmole/hr) (lb/hr)
2349 3.772e+004 5579 -2.337e+004 31.08
2349 3.772e+004 5579 -2.337e+004 31.08
(Btu/hr)
-5.489e+007
-5.489e+007
(barrel/day)
* 3.801e+006
3.801e+006
51
PROPERTIES
52 53
Overall
Vapour Phase
54
Molecular Weight
55
Molar Density
56
Mass Density
57
Act. Volume Flow
58
Mass Enthalpy
(Btu/lb)
-1455
-1455
59
Mass Entropy
(Btu/lb-F)
1.935
1.935
60
Heat Capacity
61
Mass Heat Capacity
62
LHV Molar Basis (Std)
(Btu/lbmole)
7.748e+004
7.748e+004
63
HHV Molar Basis (Std)
(Btu/lbmole)
8.874e+004
8.874e+004
64
HHV Mass Basis (Std)
65
CO2 Loading
66
CO2 App ML Con
67
CO2 App WT Con
68
LHV Mass Basis (Std)
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
16.06 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.767e-002 0.6049 2.665e+005
16.06 3.767e-002 0.6049 2.665e+005
7.431
7.431
0.4627
0.4627
5525
5525
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
4824
4824
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 107 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 37 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Phase Fraction [Vol. Basis]
1.000
1.000
13
Phase Fraction [Mass Basis]
1.000
1.000
14
Phase Fraction [Act. Vol. Basis]
1.000
1.000
15
Mass Exergy
(Btu/lb)
182.6
---
16
Partial Pressure of CO2
(psia)
27.40
---
17
Cost Based on Flow
(Cost/s)
0.0000
0.0000
18
Act. Gas Flow
19
Avg. Liq. Density
20 21 22
Std. Ideal Liq. Mass Density
23
Act. Liq. Flow
24
Z Factor
25
Watson K
26
User Property
27
Partial Pressure of H2S
28
Cp/(Cp - R)
29
Cp/Cv
30
Heat of Vap.
31
Kinematic Viscosity
32
Liq. Mass Density (Std. Cond)
33
Liq. Vol. Flow (Std. Cond)
34
Liquid Fraction
35
Molar Volume
36
Mass Heat of Vap.
37
Phase Fraction [Molar Basis]
38
Surface Tension
39
Thermal Conductivity
40
Viscosity
41
Cv (Semi-Ideal)
42
Mass Cv (Semi-Ideal)
43
Cv
44
Mass Cv
45
Cv (Ent. Method)
46
Mass Cv (Ent. Method)
47
Cp/Cv (Ent. Method)
48
Reid VP at 37.8 C
49
True VP at 37.8 C
50
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
51
Viscosity Index
(ACFM)
1039
1039
(lbmole/ft3)
1.799
1.799
Specific Heat
(Btu/lbmole-F)
7.431
7.431
Std. Gas Flow
(MMSCFD)
21.35
21.35
(lb/ft3)
28.90
28.90
(USGPS)
---
---
0.9975
0.9975
10.51
10.51
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.365
1.365
1.390
1.390
5705
---
1.407
1.407
4.242e-002
4.242e-002
3.801e+006
3.801e+006
0.0000
0.0000
(ft3/lbmole)
26.55
26.55
(Btu/lb)
355.2
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
4.304e-002
4.304e-002
1.363e-002
1.363e-002
5.445
5.445
0.3391
0.3391
5.344
5.344
0.3328
0.3328
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.801e+006 -30.27
52
3.801e+006 ---
COMPOSITION
53 54
Overall Phase
55 56
COMPONENTS
57
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
58
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
59
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
60
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
61
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
62
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
64
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
65
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
67
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
68
Air
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 108 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 37 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
19
37720.7641
Vapour Phase
20 21
COMPONENTS
MOLAR FLOW (lbmole/hr)
22
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
23
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
24
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
25
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
26
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
27
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
29
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
30
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
32
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
33
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
37720.7641
38
K VALUE
39 40
COMPONENTS
MIXED
LIGHT
HEAVY
41
CO
---
---
---
42
H2O
---
---
---
43
Oxygen
---
---
---
44
Methane
---
---
---
---
---
---
45
H2S
46
Hydrogen
---
---
---
47
Ethane
---
---
---
48
Propane
---
---
---
49
CO2
---
---
---
50
Nitrogen
---
---
---
---
---
---
51
Air
52
Mercury
---
---
---
53
MEAmine
---
---
---
54
Ammonia
---
---
---
55
UNIT OPERATIONS
56 57 58
FEED TO Separator:
PRODUCT FROM
D-15 SEPARADOR DE CONDENSADO Cooler:
59
LOGICAL CONNECTION Cooler
UTILITIES
60 61
( No utilities reference this stream )
62
PROCESS UTILITY
63 64 65
DYNAMICS
66 67
Pressure Specification
(Active):
68
Flow Specification
(Inactive) Molar:
69
Aspen Technology Inc. Licensed to: LEGENDS
* 229.7 psia
2349 lbmole/hrMass:
3.772e+004 lb/hrStd Ideal Liq Volume:
Aspen HYSYS Version 8.8 (34.0.0.8909)
5579 barrel/day
Page 109 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 37 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
User Variables
10 11
NOTES
12 13 14
Description
15 16 17
Material Stream: 38
18 19 20
CONDITIONS
21 22
Overall
23
Vapour / Phase Fraction
24
Temperature:
25
Pressure:
26
Molar Flow
27
Mass Flow
28
Std Ideal Liq Vol Flow
(barrel/day)
29
Molar Enthalpy
(Btu/lbmole)
30
Molar Entropy
(Btu/lbmole-F)
31
Heat Flow
32
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
1.0000
1.0000
0.0000
(F)
110.0
110.0
110.0
(psia)
229.7
229.7
229.7
2349
2349
0.0000
(lbmole/hr) (lb/hr)
3.772e+004 5579 -2.337e+004 31.08
3.772e+004 5579 -2.337e+004 31.08
0.0000 0.0000 -1.225e+005 13.95
(Btu/hr)
-5.489e+007
-5.489e+007
0.0000
(barrel/day)
* 3.801e+006
3.801e+006
0.0000
33
PROPERTIES
34 35
Overall
Vapour Phase
Aqueous Phase
36
Molecular Weight
37
Molar Density
38
Mass Density
39
Act. Volume Flow
40
Mass Enthalpy
(Btu/lb)
-1455
-1455
-6791
41
Mass Entropy
(Btu/lb-F)
1.935
1.935
0.7735
42
Heat Capacity
7.431
7.431
18.57
43
Mass Heat Capacity
0.4627
0.4627
1.030
44
LHV Molar Basis (Std)
(Btu/lbmole)
7.748e+004
7.748e+004
45
HHV Molar Basis (Std)
(Btu/lbmole)
8.874e+004
8.874e+004
46
HHV Mass Basis (Std)
47
CO2 Loading
48
CO2 App ML Con
49
CO2 App WT Con
50
LHV Mass Basis (Std)
51 52 53
Phase Fraction [Act. Vol. Basis]
54
Mass Exergy
55
Partial Pressure of CO2
56
Cost Based on Flow
57
Act. Gas Flow
58
Avg. Liq. Density
59 60 61
Std. Ideal Liq. Mass Density
62
Act. Liq. Flow
63
Z Factor
64
Watson K
65
User Property
66
Partial Pressure of H2S
67
16.06 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.767e-002 0.6049 2.665e+005
16.06 3.767e-002 0.6049 2.665e+005
18.03 2.906 52.39 0.0000
1.851 1.762e+004
5525
5525
977.3
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
4824
4824
0.1027
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
182.6
---
---
(psia)
27.40
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1039
1039
---
(lbmole/ft3)
1.799
1.799
3.454
Specific Heat
(Btu/lbmole-F)
7.431
7.431
18.57
Std. Gas Flow
(MMSCFD)
21.35
21.35
0.0000
(lb/ft3)
28.90
28.90
62.28
(USGPS)
0.0000
---
0.0000
---
0.9975
10.51
10.51
8.465
---
---
---
0.0000
---
---
Cp/(Cp - R)
1.365
1.365
1.120
68
Cp/Cv
1.390
1.390
1.157
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
1.293e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 110 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 38 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Heat of Vap.
13
Kinematic Viscosity
14
Liq. Mass Density (Std. Cond)
15
Liq. Vol. Flow (Std. Cond)
16
Liquid Fraction
17
Molar Volume
18
Mass Heat of Vap.
19
Phase Fraction [Molar Basis]
20
Surface Tension
21
Thermal Conductivity
22
Viscosity
23
Cv (Semi-Ideal)
24
Mass Cv (Semi-Ideal)
25
Cv
26
Mass Cv
27
Cv (Ent. Method)
28
Mass Cv (Ent. Method)
29
Cp/Cv (Ent. Method)
30
Reid VP at 37.8 C
31
True VP at 37.8 C
32
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
33
Viscosity Index
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Aqueous Phase
5705
---
---
1.407
1.407
0.7294
4.242e-002
4.242e-002
63.37
3.801e+006
3.801e+006
0.0000
0.0000
0.0000
1.000
26.55
26.55
0.3442
355.2
---
---
1.0000
1.0000
0.0000
---
---
68.86
4.304e-002
4.304e-002
0.3672
1.363e-002
1.363e-002
0.6121
5.445
5.445
16.58
0.3391
0.3391
0.9196
5.344
5.344
16.05
0.3328
0.3328
0.8900
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
248.8
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
3.801e+006 -30.27
34
3.801e+006 ---
0.0000 ---
COMPOSITION
35 36
Overall Phase
37 38
COMPONENTS
39
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
40
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
41
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
42
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
43
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
44
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
46
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
47
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
49
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
50
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
55
37720.7641
Vapour Phase
56 57
COMPONENTS
58
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
59
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
60
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
61
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
62
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
63
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
65
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
66
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
68
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.2202
Page 111 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 38 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
20
37720.7641
Aqueous Phase
21 22
COMPONENTS
MOLAR FLOW (lbmole/hr)
23
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
24
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
H2O
0.0000
0.9993
0.0000
0.9985
0.0000
0.9981
26
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
CO2
0.0000
0.0006
0.0000
0.0015
0.0000
0.0018
33
Nitrogen
0.0000
0.0000
0.0000
0.0001
0.0000
0.0001
34
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
39
K VALUE
40 41
COMPONENTS
MIXED
LIGHT
HEAVY
42
CO
2.727e+004
---
43
H2O
6.157e-003
---
6.157e-003
44
Oxygen
1.333e+004
---
1.333e+004
45
Methane
3.988e+006
---
3.988e+006
46
H2S
47
---
2.727e+004
---
---
Hydrogen
3.150e+004
---
3.150e+004
48
Ethane
1.392e+008
---
1.392e+008
49
Propane
---
---
---
50
CO2
196.7
---
196.7
51
Nitrogen
6090
---
6090
---
---
---
52
Air
53
Mercury
---
---
---
54
MEAmine
---
---
---
55
Ammonia
---
---
---
56
UNIT OPERATIONS
57 58 59
FEED TO Recycle:
PRODUCT FROM RCY-4
60
Separator:
LOGICAL CONNECTION
D-15 SEPARADOR DE CONDENSADO
UTILITIES
61 62
( No utilities reference this stream )
63
PROCESS UTILITY
64 65 66
DYNAMICS
67 68
Pressure Specification
69
Aspen Technology Inc. Licensed to: LEGENDS
(Inactive):
229.7 psia
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 112 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 38 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
DYNAMICS
10 11
Fluid Package:
Flow Specification
(Inactive) Molar:
2349 lbmole/hrMass:
12
3.772e+004 lb/hrStd Ideal Liq Volume:
5579 barrel/day
User Variables
13 14
NOTES
15 16 17
Description
18 19 20
Material Stream: 39
21 22 23
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
24 25
Overall
26
Vapour / Phase Fraction
27
Temperature:
28
Pressure:
29
Molar Flow
30
Mass Flow
31
Std Ideal Liq Vol Flow
(barrel/day)
32
Molar Enthalpy
(Btu/lbmole)
33
Molar Entropy
(Btu/lbmole-F)
34
Heat Flow
35
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.0000
0.0000
1.0000
(F)
110.0
110.0
110.0
(psia)
229.7
229.7
229.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
-1.225e+005
-2.337e+004
0.0000 -1.225e+005
13.95
31.08
13.95
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
36
PROPERTIES
37 38
Overall
39
Molecular Weight
40
Molar Density
41
Mass Density
42
Act. Volume Flow
43
Mass Enthalpy
44
Mass Entropy
45
Heat Capacity
46
Mass Heat Capacity
47
Vapour Phase 18.03
(lbmole/ft3) (lb/ft3)
2.906
16.06 3.767e-002
Aqueous Phase 18.03 2.906
52.39
0.6049
52.39
0.0000
0.0000
0.0000
(Btu/lb)
-6791
-1455
-6791
(Btu/lb-F)
0.7735
1.935
0.7735
(barrel/day)
(Btu/lbmole-F)
18.57
7.431
18.57
(Btu/lb-F)
1.030
0.4627
1.030
LHV Molar Basis (Std)
(Btu/lbmole)
1.851
48
HHV Molar Basis (Std)
(Btu/lbmole)
49
HHV Mass Basis (Std)
50
CO2 Loading
51
CO2 App ML Con
52
CO2 App WT Con
53
LHV Mass Basis (Std)
54
Phase Fraction [Vol. Basis]
55
Phase Fraction [Mass Basis]
56
Phase Fraction [Act. Vol. Basis]
57
Mass Exergy
58
Partial Pressure of CO2
59
Cost Based on Flow
60
Act. Gas Flow
61
Avg. Liq. Density
62
(Btu/lb)
1.762e+004
7.748e+004 8.874e+004
1.851 1.762e+004
977.3
5525
977.3
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
0.1027
4824
0.1027
---
---
1.000
0.0000
0.0000
1.000
---
---
---
(Btu/lb)
1.779
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
18.57
7.431
18.57
63
Std. Gas Flow
(MMSCFD)
0.0000
64
Std. Ideal Liq. Mass Density
65
Act. Liq. Flow
66
Z Factor
67
Watson K
68
User Property
69
Aspen Technology Inc. Licensed to: LEGENDS
0.0000
0.0000
(lb/ft3)
62.28
28.90
62.28
(USGPS)
0.0000
---
0.0000
---
0.9975
8.465
10.51
1.293e-002 8.465
---
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 113 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 39 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of H2S
13
Cp/(Cp - R)
14
Cp/Cv
15
Heat of Vap.
16
Kinematic Viscosity
17
Liq. Mass Density (Std. Cond)
18
Liq. Vol. Flow (Std. Cond)
19
Liquid Fraction
20
Molar Volume
21
Mass Heat of Vap.
22
Phase Fraction [Molar Basis]
23
Surface Tension
24
Thermal Conductivity
25
Viscosity
26
Cv (Semi-Ideal)
27
Mass Cv (Semi-Ideal)
28
Cv
29
Mass Cv
30
Cv (Ent. Method)
31
Mass Cv (Ent. Method)
32
Cp/Cv (Ent. Method)
33
Reid VP at 37.8 C
34
True VP at 37.8 C
35 36
(psia)
(Btu/lbmole) (cSt)
Vapour Phase ---
---
1.120
1.365
1.120
1.157
1.390
1.157
1.641e+004 0.7294
(lb/ft3)
Aqueous Phase
0.0000
63.37
---
---
1.407
0.7294
4.242e-002
63.37
(barrel/day)
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
0.3442
26.55
0.3442
(Btu/lb)
0.0000
910.1
---
---
0.0000
0.0000
1.0000
(dyne/cm)
68.86
(Btu/hr-ft-F)
0.3672
4.304e-002
0.3672
0.6121
1.363e-002
0.6121
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
68.86
16.58
5.445
16.58
0.9196
0.3391
0.9196
16.05
5.344
16.05
0.8900
0.3328
0.8900
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
248.8
---
248.8
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-4.382
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
37
COMPOSITION
38 39
Overall Phase
40 41
COMPONENTS
42
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
43
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
H2O
0.0000
0.9993
0.0000
0.9985
0.0000
0.9981
45
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
CO2
0.0000
0.0006
0.0000
0.0015
0.0000
0.0018
52
Nitrogen
0.0000
0.0000
0.0000
0.0001
0.0000
0.0001
53
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
58
Vapour Phase
59 60
COMPONENTS
61
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
62
CO
0.0000
0.0251
0.0000
0.0438
0.0000
0.0254
63
H2O
0.0000
0.0062
0.0000
0.0069
0.0000
0.0032
64
Oxygen
0.0000
0.0574
0.0000
0.1144
0.0000
0.0465
65
Methane
0.0000
0.0323
0.0000
0.0323
0.0000
0.0499
66
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Hydrogen
0.0000
0.5258
0.0000
0.0660
0.0000
0.4374
68
Ethane
0.0000
0.0140
0.0000
0.0262
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0340
Page 114 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 39 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
CO2
0.0000
0.1193
0.0000
0.3269
0.0000
0.1834
17
Nitrogen
0.0000
0.2199
0.0000
0.3836
0.0000
0.2202
18
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
23
Aqueous Phase
24 25
COMPONENTS
26
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
27
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
H2O
0.0000
0.9993
0.0000
0.9985
0.0000
0.9981
29
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
CO2
0.0000
0.0006
0.0000
0.0015
0.0000
0.0018
36
Nitrogen
0.0000
0.0000
0.0000
0.0001
0.0000
0.0001
37
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
42
K VALUE
43 44
COMPONENTS
MIXED
LIGHT
HEAVY
45
CO
2.727e+004
---
46
H2O
6.157e-003
---
6.157e-003
47
Oxygen
1.333e+004
---
1.333e+004
48
Methane
3.988e+006
---
3.988e+006
49
H2S
50
---
2.727e+004
---
---
Hydrogen
3.150e+004
---
3.150e+004
51
Ethane
1.392e+008
---
1.392e+008
52
Propane
---
---
---
53
CO2
196.7
---
196.7
54
Nitrogen
6090
---
6090
---
---
---
55
Air
56
Mercury
---
---
---
57
MEAmine
---
---
---
58
Ammonia
---
---
---
59
UNIT OPERATIONS
60 61
FEED TO
62
PRODUCT FROM Separator:
63
LOGICAL CONNECTION
D-15 SEPARADOR DE CONDENSADO
UTILITIES
64 65
( No utilities reference this stream )
66
PROCESS UTILITY
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 115 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 39 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
DYNAMICS
10 11
Pressure Specification
(Inactive):
12
Flow Specification
(Inactive) Molar:
229.7 psia 0.0000 lbmole/hrMass:
13
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
14 15
NOTES
16 17 18
Description
19 20 21
Material Stream: 40
22 23 24
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
25 26
Overall
27
Vapour / Phase Fraction
28
Temperature:
29
Pressure:
30
Molar Flow
31
Mass Flow
32
Std Ideal Liq Vol Flow
(barrel/day)
33
Molar Enthalpy
(Btu/lbmole)
34
Molar Entropy
(Btu/lbmole-F)
35
Heat Flow
36
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
111.8
111.8
(psia)
229.7
229.7
(lbmole/hr) (lb/hr)
2205 3.254e+004 5101 -1.658e+004 30.47
2205 3.254e+004 5101 -1.658e+004 30.47
(Btu/hr)
-3.657e+007
-3.657e+007
(barrel/day)
* 3.569e+006
3.569e+006
37
PROPERTIES
38 39
Overall
Vapour Phase
40
Molecular Weight
41
Molar Density
42
Mass Density
43
Act. Volume Flow
44
Mass Enthalpy
(Btu/lb)
-1124
-1124
45
Mass Entropy
(Btu/lb-F)
2.065
2.065
46
Heat Capacity
47
Mass Heat Capacity
48
LHV Molar Basis (Std)
(Btu/lbmole)
7.899e+004
7.899e+004
49
HHV Molar Basis (Std)
(Btu/lbmole)
9.052e+004
9.052e+004
50
HHV Mass Basis (Std)
51
CO2 Loading
52
CO2 App ML Con
53
CO2 App WT Con
54
LHV Mass Basis (Std)
55 56
14.76 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.746e-002 0.5528 2.516e+005
14.76 3.746e-002 0.5528 2.516e+005
7.300
7.300
0.4947
0.4947
6134
6134
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
5353
5353
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
57
Phase Fraction [Act. Vol. Basis]
1.000
1.000
58
Mass Exergy
(Btu/lb)
199.0
---
59
Partial Pressure of CO2
(psia)
19.12
---
60
Cost Based on Flow
(Cost/s)
0.0000
0.0000
61
Act. Gas Flow
62
Avg. Liq. Density
63
(ACFM)
981.0
981.0
(lbmole/ft3)
1.848
1.848
Specific Heat
(Btu/lbmole-F)
7.300
7.300
64
Std. Gas Flow
(MMSCFD)
20.04
20.04
65
Std. Ideal Liq. Mass Density
(lb/ft3)
27.27
27.27
66
Act. Liq. Flow
(USGPS)
---
---
67
Z Factor
0.9998
0.9998
68
Watson K
10.71
10.71
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 116 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 40 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
User Property
13
Partial Pressure of H2S
14
Cp/(Cp - R)
15
Cp/Cv
16
Heat of Vap.
17
Kinematic Viscosity
18
Liq. Mass Density (Std. Cond)
19
Liq. Vol. Flow (Std. Cond)
20
Liquid Fraction
21
Molar Volume
22
Mass Heat of Vap.
23
Phase Fraction [Molar Basis]
24
Surface Tension
25
Thermal Conductivity
26
Viscosity
27
Cv (Semi-Ideal)
28
Mass Cv (Semi-Ideal)
29
Cv
30
Mass Cv
31
Cv (Ent. Method)
32
Mass Cv (Ent. Method)
33
Cp/Cv (Ent. Method)
34
Reid VP at 37.8 C
35
True VP at 37.8 C
36
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
37
Viscosity Index
Vapour Phase ---
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
---
0.0000
---
1.374
1.374
1.395
1.395
5610
---
1.500
1.500
3.897e-002
3.897e-002
3.569e+006
3.569e+006
0.0000
0.0000
(ft3/lbmole)
26.69
26.69
(Btu/lb)
380.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
4.605e-002
4.605e-002
1.329e-002
1.329e-002
5.314
5.314
0.3601
0.3601
5.232
5.232
0.3546
0.3546
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.569e+006 -28.38
38
3.569e+006 ---
COMPOSITION
39 40
Overall Phase
41 42
COMPONENTS
43
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
44
CO
58.2972
0.0264
1632.9560
0.0502
139.8734
0.0274
45
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Oxygen
130.6356
0.0592
4180.3394
0.1285
251.5994
0.0493
47
Methane
72.2034
0.0327
1158.3525
0.0356
264.9207
0.0519
48
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Hydrogen
1226.5292
0.5562
2472.6829
0.0760
2423.6154
0.4752
50
Ethane
23.3595
0.0106
702.4180
0.0216
135.2231
0.0265
51
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
CO2
183.5713
0.0832
8078.9173
0.2483
670.2567
0.1314
53
Nitrogen
510.1373
0.2313
14290.4765
0.4391
1213.4684
0.2379
54
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
MEAmine
0.4159
0.0002
25.4075
0.0008
1.7107
0.0003
57
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Total
2205.1494
1.0000
1.0000
5100.6678
1.0000
59
32541.5499
Vapour Phase
60 61
COMPONENTS
62
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
63
CO
58.2972
0.0264
1632.9560
0.0502
139.8734
0.0274
64
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Oxygen
130.6356
0.0592
4180.3394
0.1285
251.5994
0.0493
66
Methane
72.2034
0.0327
1158.3525
0.0356
264.9207
0.0519
67
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Hydrogen
1226.5292
0.5562
2472.6829
0.0760
2423.6154
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.4752
Page 117 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 40 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14 15
Ethane
16
Propane
17
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
23.3595
0.0106
702.4180
0.0216
135.2231
0.0265
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
CO2
183.5713
0.0832
8078.9173
0.2483
670.2567
0.1314
18
Nitrogen
510.1373
0.2313
14290.4765
0.4391
1213.4684
0.2379
19
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
MEAmine
0.4159
0.0002
25.4075
0.0008
1.7107
0.0003
22
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Total
2205.1494
1.0000
1.0000
5100.6678
1.0000
32541.5499
24
K VALUE
25 26
COMPONENTS
MIXED
LIGHT
HEAVY
27
CO
---
---
---
28
H2O
---
---
---
29
Oxygen
---
---
---
30
Methane
---
---
---
---
---
---
31
H2S
32
Hydrogen
---
---
---
33
Ethane
---
---
---
34
Propane
---
---
---
35
CO2
---
---
---
36
Nitrogen
---
---
---
---
---
---
37
Air
38
Mercury
---
---
---
39
MEAmine
---
---
---
40
Ammonia
---
---
---
41
UNIT OPERATIONS
42 43 44
FEED TO
PRODUCT FROM
Component Splitter:
X-100
45
Absorber:
LOGICAL CONNECTION T-100
UTILITIES
46 47
( No utilities reference this stream )
48
PROCESS UTILITY
49 50 51
DYNAMICS
52 53
Pressure Specification
(Inactive):
54
Flow Specification
(Inactive) Molar:
55
229.7 psia 2205 lbmole/hrMass:
3.254e+004 lb/hrStd Ideal Liq Volume:
5101 barrel/day
User Variables
56 57
NOTES
58 59 60
Description
61 62 63 64 65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 118 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 41
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
134.1
134.1
(psia)
228.7*
228.7
223.2
223.2
(lbmole/hr) (lb/hr) (barrel/day)
8896
8896
742.4
742.4
-1.373e+005 36.71
-1.373e+005 36.71
(Btu/hr)
-3.066e+007
-3.066e+007
(barrel/day)
* 3.598e+005
3.598e+005
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-3446
-3446
30
Mass Entropy
(Btu/lb-F)
0.9212
0.9212
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
3.162e+004
3.162e+004
34
HHV Molar Basis (Std)
(Btu/lbmole)
3.162e+004
3.162e+004
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41
39.85 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.751e-002 1.495 2.544e+004
39.85 3.751e-002 1.495 2.544e+004
9.315
9.315
0.2337
0.2337
793.3
793.3
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
793.3
793.3
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
(Btu/lb)
72.54
---
44
Partial Pressure of CO2
(psia)
169.3
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48
(ACFM)
99.19
99.19
(lbmole/ft3)
1.285
1.285
Specific Heat
(Btu/lbmole-F)
9.315
9.315
49
Std. Gas Flow
(MMSCFD)
2.029
2.029
50
Std. Ideal Liq. Mass Density
(lb/ft3)
51.22
51.22
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
0.9569
0.9569
53
Watson K
8.145
8.145
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.271
1.271
1.359
1.359
8471
---
0.7497
0.7497
0.1057 3.598e+005
0.1057 3.598e+005
0.0000
0.0000
(ft3/lbmole)
26.66
26.66
(Btu/lb)
212.6
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
1.295e-002
1.295e-002
1.795e-002
1.795e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 119 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 41 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 7.329
7.329
0.1839
0.1839
6.855
6.855
0.1720
0.1720
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.598e+005
3.598e+005
-44.10
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
29
CO
58.0057
0.2599
1624.7912
0.1826
139.1740
0.1875
30
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
165.2142
0.7401
7271.0256
0.8174
603.2310
0.8125
38
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
223.2198
1.0000
8895.8168
1.0000
742.4051
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
48
CO
58.0057
0.2599
1624.7912
0.1826
139.1740
0.1875
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
165.2142
0.7401
7271.0256
0.8174
603.2310
0.8125
57
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
223.2198
1.0000
8895.8168
1.0000
742.4051
1.0000
63
K VALUE
64 65
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 120 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 41 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Mixer:
MIX-101 Component Splitter:
27
LOGICAL CONNECTION X-100
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Inactive) Molar:
* 228.7 psia
223.2 lbmole/hrMass:
37
8896 lb/hr Std Ideal Liq Volume:
742.4 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 42
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
Vapour Phase
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
2.117e+004
57
Molar Enthalpy
(Btu/lbmole)
-1.143e+005
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Liquid Phase
0.0167
0.0167
0.9833
(F)
116.8
116.8
116.8
(psia)
228.7
228.7
228.7
5218
87.07
(lbmole/hr) (lb/hr)
3.104e+005
6.450
2665 243.1 -7.565e+004 35.79
5131 3.077e+005 2.093e+004 -1.149e+005 5.952
(Btu/hr)
-5.964e+008
-6.586e+006
-5.898e+008
(barrel/day)
* 2.102e+004
1.407e+005
2.074e+004
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 59.49
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
0.7091 42.18 3.145e+004 -1921
30.60 3.761e-002 1.151 9896 -2472
Liquid Phase 59.98 1.017 61.02 2.156e+004 -1916
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 121 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 42 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
5.477e+005
8.452e+004
5.555e+005
16
HHV Molar Basis (Std)
(Btu/lbmole)
6.052e+005
8.728e+004
6.140e+005
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
Phase Fraction [Vol. Basis]
1.148e-002
1.148e-002
0.9885
23
Phase Fraction [Mass Basis]
8.584e-003
8.584e-003
0.9914
24
Phase Fraction [Act. Vol. Basis]
25
Mass Exergy
26
Partial Pressure of CO2
27
Cost Based on Flow
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.1084
1.170
41.50
8.070
42.07
0.6976
0.2637
0.7014
1.017e+004
9.923e-002
2852
1.024e+004
---
---
4.862e-002
(lbmole/ft3)
---
---
4.676e-002
(lbmol/lb)
---
---
7.663e-004
(Btu/lb)
9206
2762
9262
0.3146
0.3146
0.6854
(Btu/lb)
3.691
---
---
(psia)
68.33
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
38.59
38.59
---
(lbmole/ft3)
1.053
1.531
1.048
Specific Heat
(Btu/lbmole-F)
41.50
8.070
42.07
Std. Gas Flow
(MMSCFD)
47.43
0.7914
46.64
(lb/ft3)
62.67
46.86
62.85
(USGPS)
10.48
---
---
0.9830
9.085
7.836
9.096
---
---
---
0.0000
---
---
1.050
1.326
1.050
1.003
1.383
2.745
(psia)
(Btu/lbmole) (cSt)
5.317e+004 ---
(lb/ft3)
63.12
(barrel/day) (ft3/lbmole) (Btu/lb)
2.102e+004
10.48 3.634e-002
---
---
0.9974
8.933
8.094e-002 1.407e+005
63.43 2.074e+004
0.9833
0.0000
1.000
1.410
26.59
0.9829
893.8
---
---
0.0167
0.0167
0.9833
(dyne/cm)
43.51
(Btu/hr-ft-F)
---
1.751e-002
0.1022
---
1.839e-002
8.732
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
43.51
39.52
6.084
40.08
0.6643
0.1988
0.6683
41.38
5.834
15.33
0.6956
0.1906
0.2555
---
---
18.71
(Btu/lb-F)
---
---
0.3119
---
---
2.249
Reid VP at 37.8 C
(psia)
60.63
---
39.43
59
True VP at 37.8 C
(psia)
782.2
---
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
1.615e+005 22.64
62
1.407e+005 ---
225.9 2.074e+004 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 58.6847
MOLE FRACTION 0.0112
MASS FLOW (lb/hr) 1643.8102
Vapour Fraction MASS FRACTION 0.0053
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 140.8031
0.0167
LIQUID VOLUME FRACTION 0.0066
Page 122 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 42 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0167
LIQUID VOLUME FRACTION
15
H2O
14.4510
0.0028
260.3363
0.0008
17.8619
0.0008
16
Oxygen
4.1931
0.0008
134.1791
0.0004
8.0757
0.0004
17
Methane
3.6632
0.0007
58.7686
0.0002
13.4407
0.0006
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
8.4386
0.0016
17.0122
0.0001
16.6746
0.0008
20
Ethane
9.4564
0.0018
284.3530
0.0009
54.7410
0.0026
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
261.8536
0.0502
11524.0976
0.0371
956.0815
0.0452
23
Nitrogen
6.3500
0.0012
177.8814
0.0006
15.1047
0.0007
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
4850.9181
0.9296
27
Ammonia
0.0000
0.0000
28
Total
5218.0085
1.0000
29
296312.9955 0.0000 310413.4339
0.9546 0.0000 1.0000
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
19950.8243 0.0000 21173.6077 Phase Fraction
MASS FRACTION
0.9422 0.0000 1.0000 1.669e-002
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
33
CO
44.3154
0.5090
1241.3140
0.4659
106.3267
0.4374
34
H2O
0.0130
0.0001
0.2344
0.0001
0.0161
0.0001
35
Oxygen
2.2520
0.0259
72.0642
0.0270
4.3373
0.0178
36
Methane
1.5760
0.0181
25.2828
0.0095
5.7823
0.0238
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
7.0584
0.0811
14.2298
0.0053
13.9474
0.0574
39
Ethane
1.1015
0.0127
33.1231
0.0124
6.3766
0.0262
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
26.0140
0.2988
1144.8694
0.4297
94.9826
0.3908
42
Nitrogen
4.7155
0.0542
132.0943
0.0496
11.2167
0.0461
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0222
0.0003
1.3572
0.0005
0.0914
0.0004
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
87.0680
1.0000
2664.5692
1.0000
243.0770
1.0000
48
Liquid Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9833 LIQUID VOLUME FRACTION
52
CO
14.3693
0.0028
402.4962
0.0013
34.4764
0.0016
53
H2O
14.4380
0.0028
260.1019
0.0008
17.8459
0.0009
54
Oxygen
1.9411
0.0004
62.1148
0.0002
3.7385
0.0002
55
Methane
2.0873
0.0004
33.4858
0.0001
7.6584
0.0004
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
1.3802
0.0003
2.7824
0.0000
2.7272
0.0001
58
Ethane
8.3549
0.0016
251.2299
0.0008
48.3645
0.0023
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
235.8396
0.0460
10379.2282
0.0337
861.0990
0.0411
61
Nitrogen
1.6345
0.0003
45.7871
0.0001
3.8880
0.0002
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
4850.8958
0.9454
65
Ammonia
0.0000
0.0000
66
Total
5130.9405
1.0000
296311.6383 0.0000 307748.8647
0.9628 0.0000 1.0000
19950.7329 0.0000 20930.5307
0.9532 0.0000 1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 123 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 42 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
13
H2O
14
Oxygen
68.37
68.37
---
15
Methane
44.49
44.49
---
---
---
---
16
181.7
181.7
5.311e-002
H2S
---
5.311e-002
---
17
Hydrogen
301.4
301.4
---
18
Ethane
7.770
7.770
---
19
Propane
---
---
---
20
CO2
6.500
6.500
---
21
Nitrogen
170.0
170.0
---
---
---
---
---
---
---
22
Air
23
Mercury
24
MEAmine
25
Ammonia
2.699e-004 ---
26
---
---
---
UNIT OPERATIONS
27 28 29
2.699e-004
FEED TO
PRODUCT FROM
Heater:
E-108
Mixer:
LOGICAL CONNECTION MIX-101
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
228.7 psia 5218 lbmole/hrMass:
40
3.104e+005 lb/hrStd Ideal Liq Volume: 2.117e+004 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 43
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
2.117e+004
60
Molar Enthalpy
(Btu/lbmole)
-1.107e+005
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Liquid Phase
0.0227
0.0227
0.9773
(F)
200.0*
200.0
200.0
(psia)
225.7
225.7
225.7
5218
118.6
(lbmole/hr) (lb/hr)
3.104e+005
12.21
4012 357.8 -9.611e+004 37.69
5099 3.064e+005 2.082e+004 -1.111e+005 11.62
(Btu/hr)
-5.778e+008
-1.140e+007
-5.664e+008
(barrel/day)
* 2.102e+004
1.915e+005
2.065e+004
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 59.49
(lbmole/ft3)
0.5799
33.82 3.240e-002
Liquid Phase 60.09 0.9555
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 124 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 43 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-1861
-2842
-1849
15
Mass Entropy
(Btu/lb-F)
0.2053
1.114
0.1934
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
5.477e+005
7.104e+004
5.588e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
6.052e+005
7.378e+004
6.176e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
Phase Fraction [Vol. Basis]
1.690e-002
1.690e-002
0.9831
26
Phase Fraction [Mass Basis]
1.293e-002
1.293e-002
0.9871
27
Phase Fraction [Act. Vol. Basis]
28
Mass Exergy
29
Partial Pressure of CO2
30
Cost Based on Flow
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
34.50 3.846e+004
1.096 1.565e+004
57.41 2.281e+004
43.47
8.715
44.28
0.7308
0.2577
0.7369
1.017e+004
2181
1.028e+004
---
---
4.284e-002
(lbmole/ft3)
---
---
3.893e-002
(lbmol/lb)
---
---
6.781e-004
(Btu/lb)
9206
2100
9299
0.4069
0.4069
0.5931
(Btu/lb)
11.50
---
---
(psia)
102.9
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
61.02
61.02
---
(lbmole/ft3)
1.053
1.417
1.047
Specific Heat
(Btu/lbmole-F)
43.47
8.715
44.28
Std. Gas Flow
(MMSCFD)
47.43
1.078
46.35
(lb/ft3)
62.67
47.94
62.92
(USGPS)
11.09
---
---
0.9840
9.085
8.109
9.097
---
---
---
0.0000
---
---
1.048
1.295
1.047
1.003
1.342
2.837
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
5.347e+004 --63.12 2.102e+004
11.09 3.337e-002
---
---
1.159
4.057
8.955e-002 1.915e+005
63.43 2.065e+004
0.9773
0.0000
1.000
(ft3/lbmole)
1.725
30.86
1.047
(Btu/lb)
898.8
---
---
0.0227
0.0227
0.9773
(dyne/cm)
35.78
(Btu/hr-ft-F)
---
1.798e-002
---
2.035e-002
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
35.78 9.423e-002 3.731
41.49
6.729
42.29
0.6974
0.1990
0.7039
43.33
6.492
15.61
0.7283
0.1919
0.2597
---
---
15.85
(Btu/lb-F)
---
---
0.2638
---
---
2.794
Reid VP at 37.8 C
(psia)
60.63
---
35.00
62
True VP at 37.8 C
(psia)
782.2
---
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
2.122e+005 17.04
1.915e+005 ---
206.0 2.065e+004 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 125 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 43 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
0.0227
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
CO
58.6847
0.0112
1643.8102
0.0053
140.8031
0.0066
16
H2O
14.4510
0.0028
260.3363
0.0008
17.8619
0.0008
17
Oxygen
4.1931
0.0008
134.1791
0.0004
8.0757
0.0004
18
Methane
3.6632
0.0007
58.7686
0.0002
13.4407
0.0006
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
8.4386
0.0016
17.0122
0.0001
16.6746
0.0008
21
Ethane
9.4564
0.0018
284.3530
0.0009
54.7410
0.0026
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
261.8536
0.0502
11524.0976
0.0371
956.0815
0.0452
24
Nitrogen
6.3500
0.0012
177.8814
0.0006
15.1047
0.0007
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
4850.9181
0.9296
28
Ammonia
0.0000
0.0000
29
Total
5218.0085
1.0000
30
296312.9955 0.0000 310413.4339
0.9546 0.0000 1.0000
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
19950.8243 0.0000 21173.6077 Phase Fraction
MASS FRACTION
0.9422 0.0000 1.0000 2.273e-002
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
34
CO
45.7020
0.3853
1280.1549
0.3190
109.6537
0.3065
35
H2O
0.0818
0.0007
1.4731
0.0004
0.1011
0.0003
36
Oxygen
2.5625
0.0216
81.9996
0.0204
4.9353
0.0138
37
Methane
1.8937
0.0160
30.3812
0.0076
6.9483
0.0194
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
7.0207
0.0592
14.1538
0.0035
13.8729
0.0388
40
Ethane
1.9461
0.0164
58.5198
0.0146
11.2657
0.0315
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
54.0742
0.4558
2379.7885
0.5931
197.4360
0.5518
43
Nitrogen
4.8547
0.0409
135.9935
0.0339
11.5478
0.0323
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.4905
0.0041
29.9613
0.0075
2.0173
0.0056
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
118.6262
1.0000
4012.4257
1.0000
357.7781
1.0000
49
Liquid Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9773 LIQUID VOLUME FRACTION
53
CO
12.9826
0.0025
363.6553
0.0012
31.1495
0.0015
54
H2O
14.3692
0.0028
258.8633
0.0008
17.7609
0.0009
55
Oxygen
1.6306
0.0003
52.1794
0.0002
3.1405
0.0002
56
Methane
1.7695
0.0003
28.3874
0.0001
6.4923
0.0003
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
1.4178
0.0003
2.8584
0.0000
2.8017
0.0001
59
Ethane
7.5103
0.0015
225.8333
0.0007
43.4753
0.0021
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
207.7794
0.0407
9144.3091
0.0298
758.6455
0.0364
62
Nitrogen
1.4953
0.0003
41.8879
0.0001
3.5569
0.0002
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
4850.4276
0.9512
66
Ammonia
0.0000
0.0000
67
Total
5099.3823
1.0000
296283.0342 0.0000 306401.0082
0.9670 0.0000 1.0000
19948.8070 0.0000 20815.8296
0.9583 0.0000 1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 126 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 43 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
151.3
151.3
---
13
H2O
0.2446
0.2446
---
14
Oxygen
67.55
67.55
---
15
Methane
46.01
46.01
---
---
---
---
16
H2S
17
Hydrogen
212.9
212.9
---
18
Ethane
11.14
11.14
---
19
Propane
---
---
---
20
CO2
11.19
11.19
---
21
Nitrogen
139.6
139.6
---
---
---
---
---
---
---
22
Air
23
Mercury
24
MEAmine
25
Ammonia
4.347e-003 ---
26
---
---
---
UNIT OPERATIONS
27 28 29
4.347e-003
FEED TO
PRODUCT FROM
Distillation:
T-102
Heater:
LOGICAL CONNECTION E-108
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
225.7 psia 5218 lbmole/hrMass:
40
3.104e+005 lb/hrStd Ideal Liq Volume: 2.117e+004 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 44
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
60 61 62
Heat Flow
63
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
1.0000
1.0000
0.0000
(F)
110.0*
110.0
110.0
(psia)
228.7*
228.7
1982
1982
(lbmole/hr) (lb/hr)
2.365e+004
2.364e+004
(barrel/day)
4358
4358
Molar Enthalpy
(Btu/lbmole)
-2980
-2976
Molar Entropy
(Btu/lbmole-F)
29.12
29.12
228.7 7.459e-002 4.534 0.3063 -1.122e+005 4.192
(Btu/hr)
-5.907e+006
-5.898e+006
-8373
(barrel/day)
* 3.209e+006
3.209e+006
0.3061
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 11.93
(lbmole/ft3)
3.732e-002
11.93 3.732e-002
Liquid Phase 60.78 1.008
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 127 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 44 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-249.8
-249.5
15
Mass Entropy
(Btu/lb-F)
2.441
2.441
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
8.432e+004
8.430e+004
5.826e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
9.715e+004
9.713e+004
6.440e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.4453 2.270e+005
0.4452 2.270e+005
61.24 0.3165 -1847 6.898e-002
7.106
7.105
43.03
0.5956
0.5956
0.7080
8143
8143
1.060e+004
---
---
1.548e-003
(lbmole/ft3)
---
---
1.547e-003
(lbmol/lb)
---
---
2.526e-005
(Btu/lb)
7068
7067
Phase Fraction [Vol. Basis]
0.9999
0.9999
7.027e-005
26
Phase Fraction [Mass Basis]
0.9998
0.9998
1.917e-004
27
Phase Fraction [Act. Vol. Basis]
1.000
1.000
1.394e-006
28
Mass Exergy
(Btu/lb)
245.9
---
29
Partial Pressure of CO2
(psia)
2.118
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
9586
---
(ACFM)
885.0
885.0
---
(lbmole/ft3)
1.944
1.944
1.041
Specific Heat
(Btu/lbmole-F)
7.106
7.105
Std. Gas Flow
(MMSCFD)
18.02
18.02
23.19
23.19
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
1.538e-004
(Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
63.28
---
1.538e-004 3.713e-002
---
1.002
11.65
11.66
9.113
---
---
---
0.0000
---
---
1.388
1.388
1.048
1.404
1.404
2.900
5000
---
---
---
1.730
10.75
3.150e-002
3.149e-002
63.31
3.209e+006
3.209e+006
0.3061
3.764e-005 (ft3/lbmole)
43.03 6.780e-004
26.79
0.0000
1.000
26.79
0.9925
419.1
---
---
1.0000
1.0000
0.0000
---
---
46.13
5.261e-002
5.261e-002
0.1082
1.234e-002
1.234e-002
10.55
5.120
5.119
41.05
0.4292
0.4291
0.6753
5.060
5.059
14.84
0.4242
0.4241
0.2441
---
---
18.84
---
---
0.3099
---
---
2.284
---
---
9.733
---
---
3.209e+006 -23.63
3.209e+006 ---
236.7 0.3061 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 128 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 44 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
CO
0.2915
0.0001
8.1648
0.0003
0.6994
0.0002
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
130.6356
0.0659
4180.3394
0.1768
251.5994
0.0577
18
Methane
72.2034
0.0364
1158.3525
0.0490
264.9207
0.0608
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1226.5292
0.6189
2472.6829
0.1046
2423.6154
0.5561
21
Ethane
23.3595
0.0118
702.4180
0.0297
135.2231
0.0310
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
18.3571
0.0093
807.8917
0.0342
67.0257
0.0154
24
Nitrogen
510.1373
0.2574
14290.4765
0.6044
1213.4684
0.2784
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1981.9296
1.0000
1.0000
4358.2627
1.0000
30
23645.7332
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.2915
0.0001
8.1648
0.0003
0.6994
0.0002
35
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Oxygen
130.6355
0.0659
4180.3371
0.1768
251.5993
0.0577
37
Methane
72.2034
0.0364
1158.3515
0.0490
264.9205
0.0608
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1226.5290
0.6189
2472.6826
0.1046
2423.6151
0.5561
40
Ethane
23.3594
0.0118
702.4143
0.0297
135.2224
0.0310
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
18.3570
0.0093
807.8867
0.0342
67.0253
0.0154
43
Nitrogen
510.1372
0.2574
14290.4734
0.6045
1213.4681
0.2784
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.3420
0.0002
20.8891
0.0009
1.4065
0.0003
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
1981.8550
1.0000
1.0000
4357.9564
1.0000
49
23641.1995
Liquid Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
3.764e-005 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Oxygen
0.0001
0.0010
0.0023
0.0005
0.0001
0.0004
56
Methane
0.0001
0.0008
0.0010
0.0002
0.0002
0.0007
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0001
0.0019
0.0003
0.0001
0.0003
0.0009
59
Ethane
0.0001
0.0016
0.0037
0.0008
0.0007
0.0023
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0001
0.0015
0.0050
0.0011
0.0004
0.0014
62
Nitrogen
0.0001
0.0014
0.0030
0.0007
0.0003
0.0008
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0740
0.9917
4.5184
0.9966
0.3042
0.9934
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
0.0746
1.0000
4.5337
1.0000
0.3063
1.0000
68 69
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Aspen HYSYS Version 8.8 (34.0.0.8909)
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1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 44 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
13
H2O
14
Oxygen
69.17
69.17
---
15
Methane
44.20
44.20
---
---
---
---
16
189.3
189.3
4.265e-002
H2S
---
4.265e-002
---
17
Hydrogen
322.1
322.1
---
18
Ethane
7.222
7.222
---
19
Propane
---
---
---
20
CO2
6.032
6.032
---
21
Nitrogen
177.6
177.6
---
---
---
---
---
---
---
22
Air
23
Mercury
24
MEAmine
25
Ammonia
1.740e-004 ---
26
---
---
---
UNIT OPERATIONS
27 28 29
1.740e-004
FEED TO
PRODUCT FROM
LNG:
LNG-100 Component Splitter:
30
LOGICAL CONNECTION X-100
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 228.7 psia
1982 lbmole/hrMass:
40
2.365e+004 lb/hrStd Ideal Liq Volume:
4358 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 45
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
4358
4358
60
Molar Enthalpy
(Btu/lbmole)
486.0
486.0
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
585.0*
585.0
(psia)
228.7
228.7
(lbmole/hr) (lb/hr)
1982 2.365e+004
33.53
1982 2.365e+004
33.53
(Btu/hr)
9.633e+005
9.633e+005
(barrel/day)
* 3.209e+006
3.209e+006
64
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 11.93
(lbmole/ft3)
2.031e-002
11.93 2.031e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 130 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 45 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
40.74
40.74
15
Mass Entropy
(Btu/lb-F)
2.811
2.811
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
8.432e+004
8.432e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
9.715e+004
9.715e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25 26
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.2423 4.172e+005
0.2423 4.172e+005
7.511
7.511
0.6296
0.6296
8143
8143
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7068
7068
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
27
Phase Fraction [Act. Vol. Basis]
1.000
1.000
28
Mass Exergy
(Btu/lb)
337.9
---
29
Partial Pressure of CO2
(psia)
2.118
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
(ACFM)
1627
1627
(lbmole/ft3)
1.944
1.944
Specific Heat
(Btu/lbmole-F)
7.511
7.511
Std. Gas Flow
(MMSCFD)
18.02
18.02
(lb/ft3)
23.19
23.19
(USGPS)
---
---
Z Factor
1.005
1.005
38
Watson K
11.65
11.65
39
User Property
---
---
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.359
1.359
1.363
1.363
5000
---
5.288
5.288
3.150e-002
3.150e-002
3.209e+006
3.209e+006
0.0000
0.0000
(ft3/lbmole)
49.24
49.24
(Btu/lb)
419.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
8.346e-002
8.346e-002
2.052e-002
2.052e-002
5.525
5.525
0.4631
0.4631
5.513
5.513
0.4621
0.4621
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.209e+006 -7.696
3.209e+006 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 131 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 45 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
CO
0.2915
0.0001
8.1648
0.0003
0.6994
0.0002
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
130.6356
0.0659
4180.3394
0.1768
251.5994
0.0577
18
Methane
72.2034
0.0364
1158.3525
0.0490
264.9207
0.0608
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1226.5292
0.6189
2472.6829
0.1046
2423.6154
0.5561
21
Ethane
23.3595
0.0118
702.4180
0.0297
135.2231
0.0310
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
18.3571
0.0093
807.8917
0.0342
67.0257
0.0154
24
Nitrogen
510.1373
0.2574
14290.4765
0.6044
1213.4684
0.2784
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1981.9296
1.0000
1.0000
4358.2627
1.0000
30
23645.7332
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.2915
0.0001
8.1648
0.0003
0.6994
0.0002
35
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Oxygen
130.6356
0.0659
4180.3394
0.1768
251.5994
0.0577
37
Methane
72.2034
0.0364
1158.3525
0.0490
264.9207
0.0608
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1226.5292
0.6189
2472.6829
0.1046
2423.6154
0.5561
40
Ethane
23.3595
0.0118
702.4180
0.0297
135.2231
0.0310
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
18.3571
0.0093
807.8917
0.0342
67.0257
0.0154
43
Nitrogen
510.1373
0.2574
14290.4765
0.6044
1213.4684
0.2784
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
1981.9296
1.0000
1.0000
4358.2627
1.0000
49
K VALUE
50 51
23645.7332
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 132 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 45 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Conversion Reactor:
D-1 METANADOR LNG:
LOGICAL CONNECTION LNG-100
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
228.7 psia 1982 lbmole/hrMass:
23
2.365e+004 lb/hrStd Ideal Liq Volume:
4358 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 46
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
44
Molar Entropy
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
618.7
618.7
618.7
(psia)
225.7
225.7
225.7
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(Btu/lbmole)
489.3
489.2
489.3
(Btu/lbmole-F)
33.98
33.98
33.98
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
47
PROPERTIES
48 49
Overall
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Vapour Phase 12.01
(lbmole/ft3)
1.942e-002
Liquid Phase 12.01 1.942e-002
0.2332
0.2332
0.2332
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
40.74
40.74
40.74
55
Mass Entropy
(Btu/lb-F)
2.830
2.830
2.830
56
Heat Capacity
7.564
7.564
7.564
57
Mass Heat Capacity
0.6298
0.6298
0.6298
58
LHV Molar Basis (Std)
(Btu/lbmole)
8.465e+004
8.465e+004
8.465e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
9.756e+004
9.756e+004
9.756e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
Phase Fraction [Vol. Basis]
66
Phase Fraction [Mass Basis]
67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
1.942e-002
12.01
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
8124
8124
8124
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
7048
7048
7048
(Btu/lb)
---
---
1.000
0.0000
0.0000
1.000
---
---
---
345.1
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 133 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 46 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Vapour Phase
Liquid Phase
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
7.564
7.564
7.564
17
Std. Gas Flow
(MMSCFD)
0.0000
18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46 47
0.0000
0.0000
(lb/ft3)
23.38
23.38
23.38
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
---
1.004
1.004
11.64
11.64
11.64
---
---
---
0.0000
---
---
1.356
1.356
1.356
1.359
1.359
1.359
5168
---
---
0.5358
5.628
0.5358
3.171e-002
(barrel/day)
3.171e-002
3.171e-002
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
51.50
51.50
51.50
(Btu/lb)
430.3
---
---
0.0000
0.0000
1.0000
(dyne/cm)
5.591e-002
(Btu/hr-ft-F)
4.133e-002
8.439e-002
4.133e-002
2.001e-003
2.103e-002
2.001e-003
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
5.591e-002
5.578
5.578
5.578
0.4645
0.4645
0.4645
5.566
5.566
5.566
0.4634
0.4634
0.4634
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
0.0000
Viscosity Index
-7.043
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
55
H2O
0.0000
0.0066
0.0000
0.0099
0.0000
0.0037
56
Oxygen
0.0000
0.0663
0.0000
0.1768
0.0000
0.0582
57
Methane
0.0000
0.0400
0.0000
0.0534
0.0000
0.0668
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0000
0.6098
0.0000
0.1024
0.0000
0.5487
60
Ethane
0.0000
0.0119
0.0000
0.0297
0.0000
0.0313
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0000
0.0061
0.0000
0.0222
0.0000
0.0101
63
Nitrogen
0.0000
0.2591
0.0000
0.6044
0.0000
0.2807
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0002
0.0000
0.0011
0.0000
0.0004
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
0.0000
1.0000
0.0000
1.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 134 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 46 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
16
H2O
0.0000
0.0066
0.0000
0.0099
0.0000
0.0037
17
Oxygen
0.0000
0.0664
0.0000
0.1768
0.0000
0.0582
18
Methane
0.0000
0.0400
0.0000
0.0534
0.0000
0.0668
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.6098
0.0000
0.1024
0.0000
0.5487
21
Ethane
0.0000
0.0119
0.0000
0.0297
0.0000
0.0313
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0061
0.0000
0.0222
0.0000
0.0101
24
Nitrogen
0.0000
0.2591
0.0000
0.6044
0.0000
0.2807
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0002
0.0000
0.0011
0.0000
0.0004
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
35
H2O
0.0000
0.0066
0.0000
0.0099
0.0000
0.0037
36
Oxygen
0.0000
0.0663
0.0000
0.1768
0.0000
0.0582
37
Methane
0.0000
0.0400
0.0000
0.0534
0.0000
0.0668
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.6098
0.0000
0.1024
0.0000
0.5487
40
Ethane
0.0000
0.0119
0.0000
0.0297
0.0000
0.0313
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0061
0.0000
0.0222
0.0000
0.0101
43
Nitrogen
0.0000
0.2591
0.0000
0.6044
0.0000
0.2807
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0002
0.0000
0.0011
0.0000
0.0004
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
1.000
1.000
---
53
H2O
1.000
1.000
---
54
Oxygen
1.000
1.000
---
55
Methane
1.000
1.000
---
---
---
---
56
H2S
57
Hydrogen
1.000
1.000
---
58
Ethane
1.000
1.000
---
59
Propane
---
---
---
60
CO2
1.000
1.000
---
61
Nitrogen
1.000
1.000
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
1.000
1.000
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 135 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 46 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Conversion Reactor:
13
LOGICAL CONNECTION D-1 METANADOR
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
225.7 psia 0.0000 lbmole/hrMass:
23
0.0000 barrel/day
User Variables
24 25
NOTES
26 27
0.0000 lb/hr Std Ideal Liq Volume:
29285
28 29 30
(Last modified Tue Dec 11, 2018, 17:29)
31 32
Description
33 34 35
Material Stream: 47
36 37 38
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
39 40
Overall
Vapour Phase
Liquid Phase
41
Vapour / Phase Fraction
42
Temperature:
43
Pressure:
44
Molar Flow
45
Mass Flow
46
Std Ideal Liq Vol Flow
(barrel/day)
4323
4323
0.0000
47
Molar Enthalpy
(Btu/lbmole)
489.2
489.2
489.3
48
Molar Entropy
(Btu/lbmole-F)
33.98
33.98
49
Heat Flow
50
Liq Vol Flow @Std Cond
1.0000
1.0000
0.0000
(F)
618.7
618.7
618.7
(psia)
225.7
225.7
225.7
1969
1969
0.0000
(lbmole/hr) (lb/hr)
2.365e+004
2.365e+004
0.0000
33.98
(Btu/hr)
9.633e+005
9.633e+005
0.0000
(barrel/day)
* 3.188e+006
3.188e+006
0.0000
51
PROPERTIES
52 53
Overall
Vapour Phase
Liquid Phase
54
Molecular Weight
55
Molar Density
56
Mass Density
57
Act. Volume Flow
58
Mass Enthalpy
(Btu/lb)
40.74
40.74
40.74
59
Mass Entropy
(Btu/lb-F)
2.830
2.830
2.830
60
Heat Capacity
7.564
7.564
7.564
61
Mass Heat Capacity
0.6298
0.6298
0.6298
62
LHV Molar Basis (Std)
(Btu/lbmole)
8.465e+004
8.465e+004
8.465e+004
63
HHV Molar Basis (Std)
(Btu/lbmole)
9.756e+004
9.756e+004
9.756e+004
64
HHV Mass Basis (Std)
65
CO2 Loading
66
CO2 App ML Con
67
CO2 App WT Con
68
LHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
12.01 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.942e-002 0.2332 4.334e+005
12.01 1.942e-002 0.2332 4.334e+005
12.01 1.942e-002 0.2332 0.0000
8124
8124
8124
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
7048
7048
7048
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 136 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 47 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Phase Fraction [Vol. Basis]
1.000
1.000
---
13
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
14
Phase Fraction [Act. Vol. Basis]
15
Mass Exergy
16
Partial Pressure of CO2
17
Cost Based on Flow
18
Act. Gas Flow
19
Avg. Liq. Density
20 21 22
Std. Ideal Liq. Mass Density
23
Act. Liq. Flow
24
Z Factor
25
Watson K
26
User Property
27
Partial Pressure of H2S
28
Cp/(Cp - R)
29
Cp/Cv
30
Heat of Vap.
31
Kinematic Viscosity
32
Liq. Mass Density (Std. Cond)
33
Liq. Vol. Flow (Std. Cond)
34
Liquid Fraction
35
Molar Volume
36
Mass Heat of Vap.
37
Phase Fraction [Molar Basis]
38
Surface Tension
39
Thermal Conductivity
40
Viscosity
41
Cv (Semi-Ideal)
42
Mass Cv (Semi-Ideal)
43
Cv
44
Mass Cv
45
Cv (Ent. Method)
46
Mass Cv (Ent. Method)
47
Cp/Cv (Ent. Method)
48
Reid VP at 37.8 C
49
True VP at 37.8 C
50
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
51
Viscosity Index
1.000
1.000
0.0000
(Btu/lb)
345.1
---
---
(psia)
1.368
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
1690
1690
---
(lbmole/ft3)
1.947
1.947
1.947
Specific Heat
(Btu/lbmole-F)
7.564
7.564
7.564
Std. Gas Flow
(MMSCFD)
17.90
17.90
0.0000
(lb/ft3)
23.38
23.38
23.38
(USGPS)
---
---
---
---
1.004
1.004
11.64
11.64
11.64
---
---
---
0.0000
---
---
1.356
1.356
1.356
1.359
1.359
1.359
5168
---
---
5.628
5.628
0.5358
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
3.171e-002
3.171e-002
3.188e+006
3.188e+006
3.171e-002 0.0000
0.0000
0.0000
1.000
(ft3/lbmole)
51.50
51.50
51.50
(Btu/lb)
430.3
---
---
1.0000
1.0000
0.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
5.591e-002
8.439e-002
8.439e-002
4.133e-002
2.103e-002
2.103e-002
2.001e-003
5.578
5.578
5.578
0.4645
0.4645
0.4645
5.566
5.566
5.566
0.4634
0.4634
0.4634
---
---
---
---
---
---
---
---
---
(psia)
---
---
---
(psia)
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
3.188e+006 -7.043
52
3.188e+006 ---
--0.0000 ---
COMPOSITION
53 54
Overall Phase
55 56
COMPONENTS
57
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
58
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
59
H2O
12.9520
0.0066
233.3318
0.0099
16.0091
0.0037
60
Oxygen
130.6356
0.0664
4180.3394
0.1768
251.5994
0.0582
61
Methane
78.7305
0.0400
1263.0648
0.0534
288.8689
0.0668
62
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Hydrogen
1200.5231
0.6098
2420.2547
0.1024
2372.2276
0.5487
64
Ethane
23.3595
0.0119
702.4180
0.0297
135.2231
0.0313
65
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
CO2
11.9321
0.0061
525.1296
0.0222
43.5667
0.0101
67
Nitrogen
510.1373
0.2591
14290.4765
0.6044
1213.4684
0.2807
68
Air
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 137 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 47 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
17
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Total
1968.8755
1.0000
1.0000
4323.1284
1.0000
19
23645.7292
Vapour Phase
20 21
COMPONENTS
22
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
23
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
24
H2O
12.9520
0.0066
233.3318
0.0099
16.0091
0.0037
25
Oxygen
130.6356
0.0664
4180.3394
0.1768
251.5994
0.0582
26
Methane
78.7305
0.0400
1263.0648
0.0534
288.8689
0.0668
27
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Hydrogen
1200.5231
0.6098
2420.2547
0.1024
2372.2276
0.5487
29
Ethane
23.3595
0.0119
702.4180
0.0297
135.2231
0.0313
30
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
CO2
11.9321
0.0061
525.1296
0.0222
43.5667
0.0101
32
Nitrogen
510.1373
0.2591
14290.4765
0.6044
1213.4684
0.2807
33
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
36
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Total
1968.8755
1.0000
1.0000
4323.1284
1.0000
38
23645.7292
Liquid Phase
39 40
COMPONENTS
41
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
42
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
43
H2O
0.0000
0.0066
0.0000
0.0099
0.0000
0.0037
44
Oxygen
0.0000
0.0663
0.0000
0.1768
0.0000
0.0582
45
Methane
0.0000
0.0400
0.0000
0.0534
0.0000
0.0668
46
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Hydrogen
0.0000
0.6098
0.0000
0.1024
0.0000
0.5487
48
Ethane
0.0000
0.0119
0.0000
0.0297
0.0000
0.0313
49
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
CO2
0.0000
0.0061
0.0000
0.0222
0.0000
0.0101
51
Nitrogen
0.0000
0.2591
0.0000
0.6044
0.0000
0.2807
52
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
MEAmine
0.0000
0.0002
0.0000
0.0011
0.0000
0.0004
55
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
57
K VALUE
58 59
COMPONENTS
MIXED
LIGHT
HEAVY
60
CO
1.000
1.000
---
61
H2O
1.000
1.000
---
62
Oxygen
1.000
1.000
---
63
Methane
1.000
1.000
---
---
---
---
64
H2S
65
Hydrogen
1.000
1.000
---
66
Ethane
1.000
1.000
---
67
Propane
---
---
---
68
CO2
1.000
1.000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 138 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 47 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
LIGHT
Nitrogen
13
Air
HEAVY
1.000
1.000
---
---
---
---
14
Mercury
---
---
---
15
MEAmine
1.000
1.000
---
16
Ammonia
---
---
---
17
UNIT OPERATIONS
18 19 20
FEED TO
PRODUCT FROM
LNG:
LNG-101 Conversion Reactor:
21
LOGICAL CONNECTION D-1 METANADOR
UTILITIES
22 23
( No utilities reference this stream )
24
PROCESS UTILITY
25 26 27
DYNAMICS
28 29
Pressure Specification
(Inactive):
30
Flow Specification
(Inactive) Molar:
225.7 psia 1969 lbmole/hrMass:
31
2.365e+004 lb/hrStd Ideal Liq Volume:
4323 barrel/day
User Variables
32 33
NOTES
34 35 36
Description
37 38 39
Material Stream: 48
40 41 42
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
43 44
Overall
Vapour Phase
45
Vapour / Phase Fraction
46
Temperature:
47
Pressure:
48
Molar Flow
49
Mass Flow
50
Std Ideal Liq Vol Flow
(barrel/day)
4323
4323
51
Molar Enthalpy
(Btu/lbmole)
-177.8
-177.8
52
Molar Entropy
(Btu/lbmole-F)
53
Heat Flow
54
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
530.0*
530.0
(psia)
225.7
225.7
(lbmole/hr) (lb/hr)
1969 2.365e+004
33.34
1969 2.365e+004
33.34
(Btu/hr)
-3.501e+005
-3.501e+005
(barrel/day)
* 3.188e+006
3.188e+006
55
PROPERTIES
56 57
Overall
Vapour Phase
58
Molecular Weight
59
Molar Density
60
Mass Density
61
Act. Volume Flow
62
Mass Enthalpy
(Btu/lb)
-14.81
-14.81
63
Mass Entropy
(Btu/lb-F)
2.776
2.776
64
Heat Capacity
65
Mass Heat Capacity
66
LHV Molar Basis (Std)
(Btu/lbmole)
8.465e+004
8.465e+004
67
HHV Molar Basis (Std)
(Btu/lbmole)
9.756e+004
9.756e+004
68
HHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
12.01 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.116e-002 0.2541 3.978e+005
12.01 2.116e-002 0.2541 3.978e+005
7.477
7.477
0.6226
0.6226
8124
8124
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 139 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 48 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
CO2 Loading
13
CO2 App ML Con
14
CO2 App WT Con
15
LHV Mass Basis (Std)
16 17
Vapour Phase ---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7048
7048
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
18
Phase Fraction [Act. Vol. Basis]
1.000
1.000
19
Mass Exergy
(Btu/lb)
318.4
---
20
Partial Pressure of CO2
(psia)
1.368
---
21
Cost Based on Flow
(Cost/s)
0.0000
0.0000
22
Act. Gas Flow
23
Avg. Liq. Density
24 25 26
Std. Ideal Liq. Mass Density
27
Act. Liq. Flow
28
(ACFM)
1551
1551
(lbmole/ft3)
1.947
1.947
Specific Heat
(Btu/lbmole-F)
7.477
7.477
Std. Gas Flow
(MMSCFD)
17.90
17.90
(lb/ft3)
23.38
23.38
(USGPS)
---
---
Z Factor
1.004
1.004
29
Watson K
11.64
11.64
30
User Property
---
---
31
Partial Pressure of H2S
32
Cp/(Cp - R)
33
Cp/Cv
34
Heat of Vap.
35
Kinematic Viscosity
36
Liq. Mass Density (Std. Cond)
37
Liq. Vol. Flow (Std. Cond)
38
Liquid Fraction
39
Molar Volume
40
Mass Heat of Vap.
41
Phase Fraction [Molar Basis]
42
Surface Tension
43
Thermal Conductivity
44
Viscosity
45
Cv (Semi-Ideal)
46
Mass Cv (Semi-Ideal)
47
Cv
48
Mass Cv
49
Cv (Ent. Method)
50
Mass Cv (Ent. Method)
51
Cp/Cv (Ent. Method)
52
Reid VP at 37.8 C
53
True VP at 37.8 C
54
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
55
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.362
1.362
1.366
1.366
5168
---
4.786
4.786
3.171e-002
3.171e-002
3.188e+006
3.188e+006
0.0000
0.0000
(ft3/lbmole)
47.26
47.26
(Btu/lb)
430.3
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
7.923e-002
7.923e-002
1.948e-002
1.948e-002
5.491
5.491
0.4572
0.4572
5.476
5.476
0.4559
0.4559
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.188e+006 -8.874
56
3.188e+006 ---
COMPOSITION
57 58
Overall Phase
59 60
COMPONENTS
61
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
62
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
63
H2O
12.9520
0.0066
233.3318
0.0099
16.0091
0.0037
64
Oxygen
130.6356
0.0664
4180.3394
0.1768
251.5994
0.0582
65
Methane
78.7305
0.0400
1263.0648
0.0534
288.8689
0.0668
66
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Hydrogen
1200.5231
0.6098
2420.2547
0.1024
2372.2276
0.5487
68
Ethane
23.3595
0.0119
702.4180
0.0297
135.2231
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0313
Page 140 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 48 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14 15
Propane
16
CO2
17
Nitrogen
18
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
11.9321
0.0061
525.1296
0.0222
43.5667
0.0101
510.1373
0.2591
14290.4765
0.6044
1213.4684
0.2807
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
21
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Total
1968.8755
1.0000
1.0000
4323.1284
1.0000
23
23645.7292
Vapour Phase
24 25
COMPONENTS
26
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
27
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
28
H2O
12.9520
0.0066
233.3318
0.0099
16.0091
0.0037
29
Oxygen
130.6356
0.0664
4180.3394
0.1768
251.5994
0.0582
30
Methane
78.7305
0.0400
1263.0648
0.0534
288.8689
0.0668
31
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Hydrogen
1200.5231
0.6098
2420.2547
0.1024
2372.2276
0.5487
33
Ethane
23.3595
0.0119
702.4180
0.0297
135.2231
0.0313
34
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
CO2
11.9321
0.0061
525.1296
0.0222
43.5667
0.0101
36
Nitrogen
510.1373
0.2591
14290.4765
0.6044
1213.4684
0.2807
37
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
40
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Total
1968.8755
1.0000
1.0000
4323.1284
1.0000
23645.7292
42
K VALUE
43 44
COMPONENTS
MIXED
LIGHT
HEAVY
45
CO
---
---
---
46
H2O
---
---
---
47
Oxygen
---
---
---
48
Methane
---
---
---
---
---
---
49
H2S
50
Hydrogen
---
---
---
51
Ethane
---
---
---
52
Propane
---
---
---
53
CO2
---
---
---
54
Nitrogen
---
---
---
---
---
---
55
Air
56
Mercury
---
---
---
57
MEAmine
---
---
---
58
Ammonia
---
---
---
59
UNIT OPERATIONS
60 61 62
FEED TO Cooler:
63
PRODUCT FROM E-101
LNG:
LOGICAL CONNECTION LNG-101
UTILITIES
64 65
( No utilities reference this stream )
66
PROCESS UTILITY
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 141 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 48 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
DYNAMICS
10 11
Pressure Specification
(Inactive):
12
Flow Specification
(Inactive) Molar:
225.7 psia 1969 lbmole/hrMass:
13
2.365e+004 lb/hrStd Ideal Liq Volume:
4323 barrel/day
User Variables
14 15
NOTES
16 17 18
Description
19 20 21
Material Stream: 49
22 23 24
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
25 26
Overall
Vapour Phase
27
Vapour / Phase Fraction
28
Temperature:
29
Pressure:
30
Molar Flow
31
Mass Flow
32
Std Ideal Liq Vol Flow
(barrel/day)
4323
4318
33
Molar Enthalpy
(Btu/lbmole)
-3346
-3110
34
Molar Entropy
(Btu/lbmole-F)
35
Heat Flow
36
Liq Vol Flow @Std Cond
Liquid Phase
Aqueous Phase
0.9980
0.9980
0.0001
0.0019
(F)
100.0*
100.0
100.0
100.0
(psia)
220.7
220.7
220.7
220.7
1969
1965
0.2592
3.646
14.07
65.69
(lbmole/hr) (lb/hr)
2.365e+004
29.18
2.357e+004
29.21
(Btu/hr)
-6.588e+006
-6.111e+006
(barrel/day)
* 3.188e+006
3.181e+006
37
0.9507 -1.136e+005 6.286 -2.944e+004 0.9716
4.508 -1.226e+005 13.60 -4.471e+005 4.433
PROPERTIES
38 39
Overall
Vapour Phase
Liquid Phase
Aqueous Phase
40
Molecular Weight
41
Molar Density
42
Mass Density
43
Act. Volume Flow
44
Mass Enthalpy
(Btu/lb)
-278.6
-259.3
-2093
-6805
45
Mass Entropy
(Btu/lb-F)
2.429
2.435
0.1158
0.7551
46
Heat Capacity
47
Mass Heat Capacity
48
LHV Molar Basis (Std)
(Btu/lbmole)
8.465e+004
8.475e+004
4.940e+005
49
HHV Molar Basis (Std)
(Btu/lbmole)
9.756e+004
9.765e+004
5.487e+005
50
HHV Mass Basis (Std)
51
CO2 Loading
52
CO2 App ML Con
(lbmole/ft3)
53
CO2 App WT Con
(lbmol/lb)
54
LHV Mass Basis (Std)
(Btu/lb)
55
Phase Fraction [Vol. Basis]
0.9987
0.9987
2.199e-004
1.043e-003
56
Phase Fraction [Mass Basis]
0.9966
0.9966
5.950e-004
2.778e-003
57
Phase Fraction [Act. Vol. Basis]
1.000
1.000
4.352e-006
1.969e-005
58
Mass Exergy
(Btu/lb)
240.6
---
---
59
Partial Pressure of CO2
(psia)
1.340
---
---
---
60
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
0.0000
61
Act. Gas Flow
62
Avg. Liq. Density
63 64 65
Std. Ideal Liq. Mass Density
66
Act. Liq. Flow
67
Z Factor
68
Watson K
69
Aspen Technology Inc.
12.01 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.676e-002 0.4415 2.289e+005
11.99 3.669e-002 0.4400 2.289e+005
54.29
18.02
1.112
3.458
60.36
62.31
0.9964
4.507
7.130
7.105
39.23
18.56
0.5937
0.5924
0.7226
1.030 15.28 1.765e+004
8124
8142
1.011e+004
---
---
1.236e-003
---
---
1.156e-003
1.115e-004
---
---
1.915e-005
1.789e-006
7048
7066
9101
979.4 1.373
0.8482
---
(ACFM)
892.6
892.6
---
---
(lbmole/ft3)
1.947
1.945
1.165
3.458
Specific Heat
(Btu/lbmole-F)
7.130
7.105
Std. Gas Flow
(MMSCFD)
17.90
17.86
23.38
23.33
Licensed to: LEGENDS
(lb/ft3) (USGPS)
2.675e-003
39.23 2.356e-003 63.26
18.56 3.314e-002 62.30
---
4.843e-004
2.191e-003
---
1.002
3.305e-002
1.063e-002
11.64
11.64
9.110
Aspen HYSYS Version 8.8 (34.0.0.8909)
8.332
Page 142 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 49 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
User Property
13
Partial Pressure of H2S
14
Cp/(Cp - R)
15
Cp/Cv
16
Heat of Vap.
17
Kinematic Viscosity
18
Liq. Mass Density (Std. Cond)
19
Liq. Vol. Flow (Std. Cond)
20
Liquid Fraction
21
Molar Volume
22
Mass Heat of Vap.
23
Phase Fraction [Molar Basis]
24
Surface Tension
25
Thermal Conductivity
26
Viscosity
27
Cv (Semi-Ideal)
28
Mass Cv (Semi-Ideal)
29
Cv
30
Mass Cv
31
Cv (Ent. Method)
32
Mass Cv (Ent. Method)
33
Cp/Cv (Ent. Method)
34
Reid VP at 37.8 C
(psia)
35
True VP at 37.8 C
(psia)
36
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
37
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
Vapour Phase
(Btu/lb)
Aqueous Phase
---
---
0.0000
---
---
---
1.386
1.388
1.053
1.120
1.402
1.406
1.751
1.154
5165
---
---
---
---
1.728
10.21
0.6813
---
3.171e-002
3.167e-002
61.90
63.35
3.188e+006
3.181e+006
0.9716
4.433
1.984e-003 (ft3/lbmole)
Liquid Phase
---
27.20
0.0000
1.000
1.000
27.26
0.8994
0.2892
430.0
---
---
---
0.9980
0.9980
0.0001
0.0019
(dyne/cm)
---
50.63
69.87
(Btu/hr-ft-F)
---
5.128e-002
0.1358
0.3633
---
1.218e-002
9.875
0.6799
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
5.144
5.119
37.24
16.57
0.4284
0.4268
0.6860
0.9199
5.084
5.055
22.40
16.08
0.4234
0.4215
0.4125
0.8925
---
---
23.79
15.91
---
---
0.4382
0.8829
---
---
1.649
1.167
---
---
9.275
3393
---
---
220.6
203.8
0.9716
4.433
---
---
3.181e+006 -23.99
38
3.181e+006 ---
COMPOSITION
39 40
Overall Phase
41 42
COMPONENTS
43
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9980
LIQUID VOLUME FRACTION
44
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
45
H2O
12.9520
0.0066
233.3318
0.0099
16.0091
0.0037
46
Oxygen
130.6356
0.0664
4180.3394
0.1768
251.5994
0.0582
47
Methane
78.7305
0.0400
1263.0648
0.0534
288.8689
0.0668
48
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Hydrogen
1200.5231
0.6098
2420.2547
0.1024
2372.2276
0.5487
50
Ethane
23.3595
0.0119
702.4180
0.0297
135.2231
0.0313
51
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
CO2
11.9321
0.0061
525.1296
0.0222
43.5667
0.0101
53
Nitrogen
510.1373
0.2591
14290.4765
0.6044
1213.4684
0.2807
54
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
MEAmine
0.4159
0.0002
25.4075
0.0011
1.7107
0.0004
57
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Total
1968.8755
1.0000
1.0000
4323.1284
1.0000
59
23645.7292
Vapour Phase
60 61
COMPONENTS
62
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9980 LIQUID VOLUME FRACTION
63
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
64
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
65
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
66
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
67
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.5494
Page 143 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 49 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
COMPONENTS
14 15
Ethane
16
Propane
17
CO2
18
Nitrogen
19
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
0.9980
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
22
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
23565.9660
24
Liquid Phase
25 26
COMPONENTS
27
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.316e-004 LIQUID VOLUME FRACTION
28
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
H2O
0.0395
0.1522
0.7107
0.0505
0.0488
0.0513
30
Oxygen
0.0002
0.0008
0.0069
0.0005
0.0004
0.0004
31
Methane
0.0002
0.0006
0.0027
0.0002
0.0006
0.0006
32
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
Hydrogen
0.0004
0.0016
0.0008
0.0001
0.0008
0.0008
34
Ethane
0.0003
0.0011
0.0083
0.0006
0.0016
0.0017
35
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
CO2
0.0003
0.0010
0.0119
0.0008
0.0010
0.0010
37
Nitrogen
0.0004
0.0014
0.0098
0.0007
0.0008
0.0009
38
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
MEAmine
0.2180
0.8413
13.3183
0.9466
0.8967
0.9432
41
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Total
0.2592
1.0000
14.0693
1.0000
0.9507
1.0000
43
Aqueous Phase
44 45
COMPONENTS
46
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.852e-003 LIQUID VOLUME FRACTION
47
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
H2O
3.6458
0.9999
65.6787
0.9998
4.5063
0.9997
49
Oxygen
0.0000
0.0000
0.0005
0.0000
0.0000
0.0000
50
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
Hydrogen
0.0001
0.0000
0.0001
0.0000
0.0001
0.0000
53
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
CO2
0.0001
0.0000
0.0052
0.0001
0.0004
0.0001
56
Nitrogen
0.0001
0.0000
0.0042
0.0001
0.0004
0.0001
57
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
MEAmine
0.0001
0.0000
0.0052
0.0001
0.0004
0.0001
60
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Total
3.6462
1.0000
65.6939
1.0000
4.5076
1.0000
62
K VALUE
63 64
COMPONENTS
MIXED
65
CO
66
H2O
67
Oxygen
68 69
Methane
Aspen Technology Inc. Licensed to: LEGENDS
LIGHT 2985 4.998e-003
HEAVY 215.9 3.098e-002
1133
80.26
941.1
62.46
Aspen HYSYS Version 8.8 (34.0.0.8909)
3.388e+004 4.717e-003 1.674e+004 5.940e+006
Page 144 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 49 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
H2S
LIGHT
HEAVY
---
---
Hydrogen
5212
391.3
4.186e+004
14
Ethane
169.1
11.22
2.250e+008
15
Propane
---
---
---
16
CO2
61.28
5.841
188.3
17
Nitrogen
2030
191.7
6375
---
---
---
---
---
13
18
Air
19
Mercury
20
MEAmine
21
Ammonia
1.803e-003
4.287
---
---
UNIT OPERATIONS
23 24 25
---
1.197e-004
---
22
---
FEED TO
PRODUCT FROM
Separator:
D-9
Cooler:
LOGICAL CONNECTION E-101
26
UTILITIES
27 28
( No utilities reference this stream )
29
PROCESS UTILITY
30 31 32
DYNAMICS
33 34
Pressure Specification
(Inactive):
35
Flow Specification
(Inactive) Molar:
220.7 psia 1969 lbmole/hrMass:
36
2.365e+004 lb/hrStd Ideal Liq Volume:
4323 barrel/day
User Variables
37 38
NOTES
39 40 41
Description
42 43 44
Material Stream: 50
45 46 47
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
48 49
Overall
50
Vapour / Phase Fraction
51
Temperature:
52
Pressure:
53
Molar Flow
54
Mass Flow
55
Std Ideal Liq Vol Flow
(barrel/day)
56
Molar Enthalpy
(Btu/lbmole)
57
Molar Entropy
(Btu/lbmole-F)
58
Heat Flow
59
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
Aqueous Phase
0.0000
0.0000
0.0664
0.9336
(F)
100.0
100.0
100.0
100.0
(psia)
220.7
220.7
220.7
220.7
3.905
0.0000
0.2592
3.646
79.76
0.0000
14.07
65.69
5.458
0.0000
0.9507
(lbmole/hr) (lb/hr)
(Btu/hr)
-1.220e+005 13.12 -4.765e+005 5.457*
(barrel/day)
60
-3110 29.21 0.0000 0.0000
-1.136e+005 6.286 -2.944e+004 0.9716
4.508 -1.226e+005 13.60 -4.471e+005 4.433
PROPERTIES
61 62
Overall
63
Molecular Weight
64
Molar Density
65
Mass Density
66
Act. Volume Flow
67 68 69
Fluid Package:
Vapour Phase 20.42
(lbmole/ft3)
3.669e-002
Liquid Phase
Aqueous Phase
54.29
18.02
1.112
3.458
61.95
0.4400
60.36
62.31
(barrel/day)
5.503
0.0000
0.9964
4.507
Mass Enthalpy
(Btu/lb)
-5974
-259.3
-2093
-6805
Mass Entropy
(Btu/lb-F)
0.6423
2.435
0.1158
0.7551
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
3.033
11.99
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 145 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 50 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
Aqueous Phase
12
Heat Capacity
13
Mass Heat Capacity
14
LHV Molar Basis (Std)
(Btu/lbmole)
3.280e+004
8.475e+004
4.940e+005
15
HHV Molar Basis (Std)
(Btu/lbmole)
5.289e+004
9.765e+004
5.487e+005
16
HHV Mass Basis (Std)
17
CO2 Loading
18
CO2 App ML Con
19
CO2 App WT Con
20
LHV Mass Basis (Std)
21
Phase Fraction [Vol. Basis]
22
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
19.93
7.105
39.23
18.56
0.9758
0.5924
0.7226
1.030
2590
15.28 1.765e+004
8142
1.011e+004
1.774e-003
---
1.236e-003
(lbmole/ft3)
3.006e-004
---
1.156e-003
1.115e-004
(lbmol/lb)
4.852e-006
---
1.915e-005
1.789e-006
(Btu/lb)
979.4 1.373
1606
7066
9101
0.8482
---
---
0.1742
0.8258
Phase Fraction [Mass Basis]
0.0000
0.0000
0.1764
0.8236
23
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
0.1810
0.8190
24
Mass Exergy
(Btu/lb)
1.271
---
---
---
25
Partial Pressure of CO2
(psia)
0.0000
---
---
---
26
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
0.0000
27
Act. Gas Flow
28
Avg. Liq. Density
29
Specific Heat
(Btu/lbmole-F)
30
Std. Gas Flow
(MMSCFD)
31
Std. Ideal Liq. Mass Density
32
Act. Liq. Flow
33
Z Factor
34
Watson K
35
User Property
36
Partial Pressure of H2S
37
Cp/(Cp - R)
38
Cp/Cv
39
Heat of Vap.
40
Kinematic Viscosity
41
Liq. Mass Density (Std. Cond)
42
Liq. Vol. Flow (Std. Cond)
43
Liquid Fraction
44
Molar Volume
45
Mass Heat of Vap.
46
Phase Fraction [Molar Basis]
47
Surface Tension
48
Thermal Conductivity
49
Viscosity
50
Cv (Semi-Ideal)
51
Mass Cv (Semi-Ideal)
52
Cv
53
Mass Cv
54
Cv (Ent. Method)
55
Mass Cv (Ent. Method)
56
Cp/Cv (Ent. Method)
57
(ACFM)
---
---
---
---
(lbmole/ft3)
3.058
1.945
1.165
3.458
(lb/ft3)
19.93 3.550e-002 62.47
(USGPS)
2.675e-003
(psia)
(Btu/lbmole)
62.30
---
4.843e-004
2.191e-003
3.305e-002
1.063e-002
1.002 11.64
9.110
8.332
---
---
---
---
0.0000
---
---
---
1.111
1.388
1.053
1.120
1.202
1.406
1.751
1.154
---
---
---
1.728
10.21
0.6813
1.620e+004
(lb/ft3)
62.48
(Btu/lb)
63.26
18.56 3.314e-002
---
0.9833
(ft3/lbmole)
23.33
39.23 2.356e-003
9.109
(cSt) (barrel/day)
7.105 0.0000
61.90
63.35
5.457
3.167e-002 0.0000
0.9716
4.433
1.000
0.0000
1.000
1.000
0.3297
27.26
0.8994
0.2892
793.1
---
---
---
0.0000
0.0000
0.0664
0.9336
(dyne/cm)
---
50.63
69.87
(Btu/hr-ft-F)
0.3067
5.128e-002
0.1358
0.3633
0.9758
1.218e-002
9.875
0.6799
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
17.94
5.119
37.24
16.57
0.8786
0.4268
0.6860
0.9199
16.59
5.055
22.40
16.08
0.8122
0.4215
0.4125
0.8925
---
---
23.79
15.91
(Btu/lb-F)
---
---
0.4382
0.8829
---
---
1.649
1.167
Reid VP at 37.8 C
(psia)
11.08
---
9.275
3393
58
True VP at 37.8 C
(psia)
219.8
---
220.6
203.8
59
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
5.404
0.0000
0.9716
4.433
60
Viscosity Index
3.703
---
---
---
61
COMPOSITION
62 63
Overall Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
3.6852
0.9436
66.3895
0.8323
4.5550
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
LIQUID VOLUME FRACTION 0.0000 0.8345
Page 146 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 50 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
Oxygen
0.0002
0.0001
0.0073
0.0001
0.0004
0.0001
16
Methane
0.0002
0.0000
0.0027
0.0000
0.0006
0.0001
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0005
0.0001
0.0009
0.0000
0.0009
0.0002
19
Ethane
0.0003
0.0001
0.0083
0.0001
0.0016
0.0003
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0004
0.0001
0.0170
0.0002
0.0014
0.0003
22
Nitrogen
0.0005
0.0001
0.0140
0.0002
0.0012
0.0002
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.2181
0.0559
13.3235
0.1670
0.8971
0.1644
26
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Total
3.9053
1.0000
79.7632
1.0000
5.4583
1.0000
28
Vapour Phase
29 30
COMPONENTS
31
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
32
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
33
H2O
0.0000
0.0047
0.0000
0.0071
0.0000
0.0027
34
Oxygen
0.0000
0.0665
0.0000
0.1774
0.0000
0.0583
35
Methane
0.0000
0.0401
0.0000
0.0536
0.0000
0.0669
36
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Hydrogen
0.0000
0.6110
0.0000
0.1027
0.0000
0.5494
38
Ethane
0.0000
0.0119
0.0000
0.0298
0.0000
0.0313
39
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
CO2
0.0000
0.0061
0.0000
0.0223
0.0000
0.0101
41
Nitrogen
0.0000
0.2596
0.0000
0.6064
0.0000
0.2810
42
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
MEAmine
0.0000
0.0001
0.0000
0.0005
0.0000
0.0002
45
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
47
Liquid Phase
48 49
COMPONENTS
50
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
6.636e-002 LIQUID VOLUME FRACTION
51
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
H2O
0.0395
0.1522
0.7107
0.0505
0.0488
0.0513
53
Oxygen
0.0002
0.0008
0.0069
0.0005
0.0004
0.0004
54
Methane
0.0002
0.0006
0.0027
0.0002
0.0006
0.0006
55
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Hydrogen
0.0004
0.0016
0.0008
0.0001
0.0008
0.0008
57
Ethane
0.0003
0.0011
0.0083
0.0006
0.0016
0.0017
58
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
CO2
0.0003
0.0010
0.0119
0.0008
0.0010
0.0010
60
Nitrogen
0.0004
0.0014
0.0098
0.0007
0.0008
0.0009
61
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
MEAmine
0.2180
0.8413
13.3183
0.9466
0.8967
0.9432
64
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Total
0.2592
1.0000
14.0693
1.0000
0.9507
1.0000
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 147 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 50 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Aqueous Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9336 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
3.6458
0.9999
65.6787
0.9998
4.5063
0.9997
17
Oxygen
0.0000
0.0000
0.0005
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0001
0.0000
0.0001
0.0000
0.0001
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0001
0.0000
0.0052
0.0001
0.0004
0.0001
24
Nitrogen
0.0001
0.0000
0.0042
0.0001
0.0004
0.0001
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0001
0.0000
0.0052
0.0001
0.0004
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
3.6462
1.0000
65.6939
1.0000
4.5076
1.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
34
H2O
35
Oxygen
1133
80.26
1.674e+004
36
Methane
941.1
62.46
5.940e+006
---
---
Hydrogen
5212
391.3
4.186e+004
39
Ethane
169.1
11.22
2.250e+008
40
Propane
---
---
---
41
CO2
61.28
5.841
188.3
42
Nitrogen
2030
191.7
6375
---
---
---
---
---
37
2985 4.998e-003
H2S
38
43
Air
44
Mercury
45
MEAmine
46
Ammonia
215.9
1.803e-003
4.717e-003
---
---
1.197e-004
---
47
3.388e+004
3.098e-002
4.287
---
---
UNIT OPERATIONS
48 49
FEED TO
PRODUCT FROM
50
Separator:
51
LOGICAL CONNECTION D-9
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Inactive) Molar:
61
220.7 psia 3.905 lbmole/hrMass:
79.76 lb/hr Std Ideal Liq Volume:
5.458 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 148 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 51
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Vapour Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
18
Molar Enthalpy
(Btu/lbmole)
-3110
-3110
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Liquid Phase
1.0000
1.0000
0.0000
(F)
99.94
99.94
99.94
(psia)
214.7
214.7
214.7
1965
1965
0.0000
(lbmole/hr) (lb/hr)
2.357e+004
29.26
2.357e+004
29.26
0.0000 0.0000 -1.136e+005 6.272
(Btu/hr)
-6.111e+006
-6.111e+006
0.0000
(barrel/day)
* 3.181e+006
3.181e+006
0.0000
22
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-259.3
-259.3
-2092
30
Mass Entropy
(Btu/lb-F)
2.440
2.440
0.1155
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
4.944e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
5.491e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41 42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
11.99 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.570e-002 0.4281 2.353e+005
11.99 3.570e-002 0.4281 2.353e+005
54.31 0.7208 39.15 0.0000
7.103
7.103
39.24
0.5922
0.5922
0.7225
8142
8142
---
---
1.011e+004 ---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
7066
7066
9103
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
238.6
---
---
(psia)
1.304
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
917.4
917.4
---
(lbmole/ft3)
1.945
1.945
1.165
Specific Heat
(Btu/lbmole-F)
7.103
7.103
39.24
Std. Gas Flow
(MMSCFD)
17.86
17.86
0.0000
(lb/ft3)
23.33
23.33
63.26
(USGPS)
---
---
---
1.002
11.64
11.64
9.110
---
---
---
0.0000
---
---
1.388
1.388
1.053
1.405
1.405
1.753
4951
---
---
1.776
1.776
11.81
Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
--4.960e-002
3.167e-002
3.167e-002
61.90
3.181e+006
3.181e+006
0.0000
0.0000
0.0000
1.000
(ft3/lbmole)
28.01
28.01
1.387
(Btu/lb)
412.8
---
---
1.0000
1.0000
0.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
50.63
5.126e-002
5.126e-002
0.1358
1.218e-002
1.218e-002
7.409
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 149 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 51 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
5.117
5.117
37.25
0.4267
0.4267
0.6859
5.055
5.055
22.38
0.4215
0.4215
0.4121
---
---
---
---
---
---
---
---
---
---
---
9.211
---
---
3.181e+006 -23.72
23
3.181e+006 ---
219.0 0.0000 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
30
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
31
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
32
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
35
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
38
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
44
23565.9660
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
49
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
50
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
51
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
54
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
57
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
63
23565.9660
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
0.0000
0.1517
0.0000
0.0503
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000 LIQUID VOLUME FRACTION 0.0000 0.0511
Page 150 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 51 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
Oxygen
0.0000
0.0008
0.0000
0.0005
0.0000
0.0004
16
Methane
0.0000
0.0006
0.0000
0.0002
0.0000
0.0006
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0000
0.0016
0.0000
0.0001
0.0000
0.0008
19
Ethane
0.0000
0.0011
0.0000
0.0006
0.0000
0.0017
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0000
0.0010
0.0000
0.0008
0.0000
0.0010
22
Nitrogen
0.0000
0.0013
0.0000
0.0007
0.0000
0.0009
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0000
0.8419
0.0000
0.9468
0.0000
0.9434
26
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
80.76
80.76
---
34
Methane
62.79
62.79
---
---
---
---
35
217.3
217.3
3.109e-002
H2S
---
3.109e-002
---
36
Hydrogen
394.1
394.1
---
37
Ethane
11.26
11.26
---
38
Propane
---
---
---
39
CO2
5.873
5.873
---
40
Nitrogen
193.0
193.0
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
1.196e-004 ---
45
---
---
---
UNIT OPERATIONS
46 47 48
1.196e-004
FEED TO
PRODUCT FROM
Compressor:
K-100
49
Separator:
LOGICAL CONNECTION D-9
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
214.7 psia 1965 lbmole/hrMass:
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 151 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 52
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Vapour Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
18
Molar Enthalpy
(Btu/lbmole)
-693.7
-693.7
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
434.3
434.3
(psia)
814.7*
814.7
(lbmole/hr) (lb/hr)
1965 2.357e+004
29.97
1965 2.357e+004
29.97
(Btu/hr)
-1.363e+006
-1.363e+006
(barrel/day)
* 3.181e+006
3.181e+006
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-57.84
-57.84
30
Mass Entropy
(Btu/lb-F)
2.499
2.499
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
34
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41
11.99 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
8.353e-002 1.002 1.006e+005
11.99 8.353e-002 1.002 1.006e+005
7.444
7.444
0.6207
0.6207
8142
8142
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7066
7066
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
43
Mass Exergy
(Btu/lb)
408.4
---
44
Partial Pressure of CO2
(psia)
4.947
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48
(ACFM)
392.1
392.1
(lbmole/ft3)
1.945
1.945
Specific Heat
(Btu/lbmole-F)
7.444
7.444
49
Std. Gas Flow
(MMSCFD)
17.86
17.86
50
Std. Ideal Liq. Mass Density
(lb/ft3)
23.33
23.33
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
1.017
1.017
53
Watson K
11.64
11.64
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.364
1.364
1.381
1.381
5169
---
1.120
1.120
3.167e-002
3.167e-002
3.181e+006
3.181e+006
0.0000
0.0000
(ft3/lbmole)
11.97
11.97
(Btu/lb)
431.0
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
7.427e-002
7.427e-002
1.797e-002
1.797e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 152 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 52 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 5.458
5.458
0.4551
0.4551
5.390
5.390
0.4494
0.4494
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.181e+006
3.181e+006
-23.19
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
30
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
31
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
32
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
35
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
38
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
44
23565.9660
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
49
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
50
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
51
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
54
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
57
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
63
K VALUE
64 65
23565.9660
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 153 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 52 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Cooler:
E-103
Compressor:
27
LOGICAL CONNECTION K-100
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Inactive) Molar:
* 814.7 psia
1965 lbmole/hrMass:
37
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 53
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
Vapour Phase
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
57
Molar Enthalpy
(Btu/lbmole)
-1687
-1687
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
300.0*
300.0
(psia)
814.7
814.7
(lbmole/hr) (lb/hr)
1965 2.357e+004
28.77
1965 2.357e+004
28.77
(Btu/hr)
-3.315e+006
-3.315e+006
(barrel/day)
* 3.181e+006
3.181e+006
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 11.99
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
9.837e-002 1.180 8.538e+004 -140.7
11.99 9.837e-002 1.180 8.538e+004 -140.7
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 154 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 53 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
16
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22 23
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.399
2.399
7.350
7.350
0.6128
0.6128
8142
8142
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7066
7066
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
24
Phase Fraction [Act. Vol. Basis]
1.000
1.000
25
Mass Exergy
(Btu/lb)
379.5
---
26
Partial Pressure of CO2
(psia)
4.947
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30
(ACFM)
332.9
332.9
(lbmole/ft3)
1.945
1.945
Specific Heat
(Btu/lbmole-F)
7.350
7.350
31
Std. Gas Flow
(MMSCFD)
17.86
17.86
32
Std. Ideal Liq. Mass Density
(lb/ft3)
23.33
23.33
33
Act. Liq. Flow
(USGPS)
---
---
34
Z Factor
1.016
1.016
35
Watson K
11.64
11.64
36
User Property
---
---
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.370
1.370
1.397
1.397
5169
---
0.8293
0.8293
3.167e-002
3.167e-002
3.181e+006
3.181e+006
0.0000
0.0000
(ft3/lbmole)
10.17
10.17
(Btu/lb)
431.0
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
6.586e-002
6.586e-002
1.567e-002
1.567e-002
5.364
5.364
0.4473
0.4473
5.261
5.261
0.4386
0.4386
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.181e+006 -31.06
62
3.181e+006 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.1895
MOLE FRACTION 0.0001
MASS FLOW (lb/hr) 5.3071
Vapour Fraction MASS FRACTION 0.0002
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.4546
1.0000
LIQUID VOLUME FRACTION 0.0001
Page 155 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 53 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
16
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
17
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
20
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
23
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
29
23565.9660
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
33
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
34
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
35
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
36
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
39
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
42
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
23565.9660
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
---
---
---
52
H2O
---
---
---
53
Oxygen
---
---
---
54
Methane
---
---
---
---
---
---
55
H2S
56
Hydrogen
---
---
---
57
Ethane
---
---
---
58
Propane
---
---
---
59
CO2
---
---
---
60
Nitrogen
---
---
---
---
---
---
61
Air
62
Mercury
---
---
---
63
MEAmine
---
---
---
64
Ammonia
---
---
---
65
UNIT OPERATIONS
66 67 68 69
FEED TO Compressor:
Aspen Technology Inc. Licensed to: LEGENDS
PRODUCT FROM K-101
Cooler:
LOGICAL CONNECTION E-103
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 156 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 53 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Inactive):
18
Flow Specification
(Inactive) Molar:
814.7 psia 1965 lbmole/hrMass:
19
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: 54
28 29 30
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
Vapour Phase
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
39
Molar Enthalpy
(Btu/lbmole)
-295.3
-295.3
40
Molar Entropy
(Btu/lbmole-F)
41
Heat Flow
42
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
487.1
487.1
(psia)
1515*
1515
(lbmole/hr) (lb/hr)
1965 2.357e+004
29.14
1965 2.357e+004
29.14
(Btu/hr)
-5.803e+005
-5.803e+005
(barrel/day)
* 3.181e+006
3.181e+006
43
PROPERTIES
44 45
Overall
Vapour Phase
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Mass Enthalpy
(Btu/lb)
-24.62
-24.62
51
Mass Entropy
(Btu/lb-F)
2.430
2.430
52
Heat Capacity
53
Mass Heat Capacity
54
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
55
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
56
HHV Mass Basis (Std)
57
CO2 Loading
58
CO2 App ML Con
59
CO2 App WT Con
60
LHV Mass Basis (Std)
61 62
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
11.99
0.1445
0.1445
1.733 5.812e+004
1.733 5.812e+004
7.547
7.547
0.6292
0.6292
8142
8142
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7066
7066
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
63
Phase Fraction [Act. Vol. Basis]
1.000
1.000
64
Mass Exergy
(Btu/lb)
478.7
---
65
Partial Pressure of CO2
(psia)
9.198
---
66
Cost Based on Flow
(Cost/s)
0.0000
0.0000
67
Act. Gas Flow
(ACFM)
226.6
226.6
68
Avg. Liq. Density
(lbmole/ft3)
1.945
1.945
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
11.99
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 157 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 54 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Specific Heat
(Btu/lbmole-F)
7.547
7.547
13
Std. Gas Flow
(MMSCFD)
17.86
17.86
14
Std. Ideal Liq. Mass Density
(lb/ft3)
23.33
23.33
15
Act. Liq. Flow
(USGPS)
---
---
16
Z Factor
1.031
1.031
17
Watson K
11.64
11.64
18
User Property
---
---
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
41
True VP at 37.8 C
42
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
43
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.357
1.357
1.382
1.382
5226
---
0.6870
0.6870
3.167e-002
3.167e-002
3.181e+006
3.181e+006
0.0000
0.0000
(ft3/lbmole)
6.919
6.919
(Btu/lb)
435.8
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
7.818e-002
7.818e-002
1.908e-002
1.908e-002
5.561
5.561
0.4637
0.4637
5.459
5.459
0.4552
0.4552
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.181e+006 -31.26
44
3.181e+006 ---
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
50
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
51
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
52
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
53
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
54
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
56
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
57
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
59
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
60
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
63
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
23565.9660
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 158 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 54 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
16
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
17
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
18
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
21
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
24
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
23565.9660
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Cooler:
E-104
51
Compressor:
LOGICAL CONNECTION K-101
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Active):
60
Flow Specification
(Inactive) Molar:
61
1965 lbmole/hrMass:
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
62 63
NOTES
64 65
* 1515 psia
29285
66 67 68 69
(Last modified Mon Dec 17, 2018, 15:08)
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 159 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 54 (continued)
7 8
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
9 10
Description
11 12 13
Material Stream: 55
14 15 16
CONDITIONS
17 18
Overall
Vapour Phase
19
Vapour / Phase Fraction
20
Temperature:
21
Pressure:
22
Molar Flow
23
Mass Flow
24
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
25
Molar Enthalpy
(Btu/lbmole)
-2441
-2441
26
Molar Entropy
(Btu/lbmole-F)
27
Heat Flow
28
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
200.0*
200.0
(psia)
1515
1515
(lbmole/hr) (lb/hr)
1965 2.357e+004
26.45
1965 2.357e+004
26.45
(Btu/hr)
-4.796e+006
-4.796e+006
(barrel/day)
* 3.181e+006
3.181e+006
29
PROPERTIES
30 31
Overall
Vapour Phase
32
Molecular Weight
33
Molar Density
34
Mass Density
35
Act. Volume Flow
36
Mass Enthalpy
(Btu/lb)
-203.5
-203.5
37
Mass Entropy
(Btu/lb-F)
2.205
2.205
38
Heat Capacity
39
Mass Heat Capacity
40
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
41
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
42
HHV Mass Basis (Std)
43
CO2 Loading
44
CO2 App ML Con
45
CO2 App WT Con
46
LHV Mass Basis (Std)
47 48
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
11.99
11.99
0.2080
0.2080
2.494 4.038e+004
2.494 4.038e+004
7.433
7.433
0.6198
0.6198
8142
8142
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7066
7066
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
49
Phase Fraction [Act. Vol. Basis]
1.000
1.000
50
Mass Exergy
(Btu/lb)
420.5
---
51
Partial Pressure of CO2
(psia)
9.198
---
52
Cost Based on Flow
(Cost/s)
0.0000
0.0000
53
Act. Gas Flow
54
Avg. Liq. Density
55
(ACFM)
157.5
157.5
(lbmole/ft3)
1.945
1.945
Specific Heat
(Btu/lbmole-F)
7.433
7.433
56
Std. Gas Flow
(MMSCFD)
17.86
17.86
57
Std. Ideal Liq. Mass Density
(lb/ft3)
23.33
23.33
58
Act. Liq. Flow
(USGPS)
---
---
59
Z Factor
1.029
1.029
60
Watson K
11.64
11.64
61
User Property
---
---
62
Partial Pressure of H2S
63
Cp/(Cp - R)
64
Cp/Cv
65
Heat of Vap.
66
Kinematic Viscosity
67
Liq. Mass Density (Std. Cond)
68
Liq. Vol. Flow (Std. Cond)
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.365
1.365
1.430
1.430
5226
---
0.3585
0.3585
3.167e-002
3.167e-002
3.181e+006
3.181e+006
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 160 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 55 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Liquid Fraction
13
Molar Volume
14
Mass Heat of Vap.
15
Phase Fraction [Molar Basis]
16
Surface Tension
17
Thermal Conductivity
18
Viscosity
19
Cv (Semi-Ideal)
20
Mass Cv (Semi-Ideal)
21
Cv
22
Mass Cv
23
Cv (Ent. Method)
24
Mass Cv (Ent. Method)
25
Cp/Cv (Ent. Method)
26
Reid VP at 37.8 C
27
True VP at 37.8 C
28
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
29
Viscosity Index
Vapour Phase 0.0000
0.0000
(ft3/lbmole)
4.808
4.808
(Btu/lb)
435.8
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
6.036e-002
6.036e-002
1.433e-002
1.433e-002
5.447
5.447
0.4542
0.4542
5.199
5.199
0.4335
0.4335
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.181e+006 ---
3.181e+006 ---
30
COMPOSITION
31 32
Overall Phase
33 34
COMPONENTS
35
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
36
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
37
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
38
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
39
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
40
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
42
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
43
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
45
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
46
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
49
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
51
23565.9660
Vapour Phase
52 53
COMPONENTS
54
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
55
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
56
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
57
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
58
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
59
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
61
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
62
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
64
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
65
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
68
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 161 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 55 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
Fluid Package:
Total
1964.9702
1.0000
Phase Fraction
23565.9660
14
1.0000
1.000
4317.6702
1.0000
K VALUE
15 16
COMPONENTS
MIXED
LIGHT
HEAVY
17
CO
---
---
---
18
H2O
---
---
---
19
Oxygen
---
---
---
20
Methane
---
---
---
---
---
---
21
H2S
22
Hydrogen
---
---
---
23
Ethane
---
---
---
24
Propane
---
---
---
25
CO2
---
---
---
26
Nitrogen
---
---
---
---
---
---
27
Air
28
Mercury
---
---
---
29
MEAmine
---
---
---
30
Ammonia
---
---
---
31
UNIT OPERATIONS
32 33 34
FEED TO
PRODUCT FROM
Compressor:
K-102
Cooler:
LOGICAL CONNECTION E-104
35
UTILITIES
36 37
( No utilities reference this stream )
38
PROCESS UTILITY
39 40 41
DYNAMICS
42 43
Pressure Specification
(Inactive):
44
Flow Specification
(Inactive) Molar:
1515 psia 1965 lbmole/hrMass:
45
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
46 47
NOTES
48 49 50
Description
51 52 53
Material Stream: 56
54 55 56
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
57 58
Overall
Vapour Phase
59
Vapour / Phase Fraction
60
Temperature:
61
Pressure:
62
Molar Flow
63
Mass Flow
64
Std Ideal Liq Vol Flow
(barrel/day)
4318
4318
65
Molar Enthalpy
(Btu/lbmole)
169.3
169.3
66
Molar Entropy
(Btu/lbmole-F)
67
Heat Flow
68
Liq Vol Flow @Std Cond
69
Aspen Technology Inc. Licensed to: LEGENDS
1.0000
1.0000
(F)
539.9
539.9
(psia)
4940*
4940
(lbmole/hr) (lb/hr)
1965 2.357e+004
27.13
1965 2.357e+004
27.13
(Btu/hr)
3.327e+005
3.327e+005
(barrel/day)
* 3.181e+006
3.181e+006
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 162 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 56 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Molecular Weight
13
Molar Density
14
Mass Density
15
Act. Volume Flow
16
Mass Enthalpy
(Btu/lb)
14.12
14.12
17
Mass Entropy
(Btu/lb-F)
2.262
2.262
18
Heat Capacity
19
Mass Heat Capacity
20
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.475e+004
21
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.765e+004
22
HHV Mass Basis (Std)
23
CO2 Loading
24
CO2 App ML Con
25
CO2 App WT Con
26
LHV Mass Basis (Std)
27 28
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
11.99
11.99
0.4152
0.4152
4.980 2.023e+004
4.980 2.023e+004
7.770
7.770
0.6479
0.6479
8142
8142
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7066
7066
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
29
Phase Fraction [Act. Vol. Basis]
1.000
1.000
30
Mass Exergy
(Btu/lb)
607.6
---
31
Partial Pressure of CO2
(psia)
29.99
---
32
Cost Based on Flow
(Cost/s)
0.0000
0.0000
33
Act. Gas Flow
34
Avg. Liq. Density
35
(ACFM)
78.87
78.87
(lbmole/ft3)
1.945
1.945
Specific Heat
(Btu/lbmole-F)
7.770
7.770
36
Std. Gas Flow
(MMSCFD)
17.86
17.86
37
Std. Ideal Liq. Mass Density
(lb/ft3)
23.33
23.33
38
Act. Liq. Flow
(USGPS)
---
---
39
Z Factor
1.109
1.109
40
Watson K
11.64
11.64
41
User Property
---
---
42
Partial Pressure of H2S
43
Cp/(Cp - R)
44
Cp/Cv
45
Heat of Vap.
46
Kinematic Viscosity
47
Liq. Mass Density (Std. Cond)
48
Liq. Vol. Flow (Std. Cond)
49
Liquid Fraction
50
Molar Volume
51
Mass Heat of Vap.
52
Phase Fraction [Molar Basis]
53
Surface Tension
54
Thermal Conductivity
55
Viscosity
56
Cv (Semi-Ideal)
57
Mass Cv (Semi-Ideal)
58
Cv
59
Mass Cv
60
Cv (Ent. Method)
61
Mass Cv (Ent. Method)
62
Cp/Cv (Ent. Method)
63
Reid VP at 37.8 C
(psia)
64
True VP at 37.8 C
(psia)
---
65
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
66
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.343
1.343
1.394
1.394
5157
---
0.2638
0.2638
3.167e-002
3.167e-002
3.181e+006
3.181e+006
0.0000
0.0000
(ft3/lbmole)
2.408
2.408
(Btu/lb)
430.0
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
---
8.469e-002
8.469e-002
2.105e-002
2.105e-002
5.784
5.784
0.4823
0.4823
5.576
5.576
0.4649
0.4649
5.632
5.632
0.4696
0.4696
1.380
1.380
---
-----
3.181e+006 ---
3.181e+006 ---
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 163 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 56 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
16
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
17
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
18
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
21
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
24
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
30
23565.9660
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
35
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
36
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
37
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
40
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
43
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
1964.9702
1.0000
1.0000
4317.6702
1.0000
49
K VALUE
50 51
23565.9660
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 164 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 56 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Cooler:
E-105
Compressor:
13
LOGICAL CONNECTION K-102
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 4940 psia
1965 lbmole/hrMass:
23
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 57
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
4318
4308
43
Molar Enthalpy
(Btu/lbmole)
-3348
-2899
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Liquid Phase
Aqueous Phase
0.9962
0.9962
0.0000
0.0037
(F)
95.00*
95.00
95.00
95.00
(psia)
4940
4940
4940
1965
1958
(lbmole/hr) (lb/hr)
2.357e+004
22.45
2.343e+004
22.48
6.076e-002 3.135 0.2197 -1.047e+005 7.744
(Btu/hr)
-6.579e+006
-5.674e+006
-6361
(barrel/day)
* 3.181e+006
3.169e+006
0.2259
47
4940 7.345 132.4 9.093 -1.224e+005 13.36 -8.988e+005 8.942
PROPERTIES
48 49
Overall
Vapour Phase
Liquid Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-279.2
-242.2
-2029
-6787
55
Mass Entropy
(Btu/lb-F)
1.872
1.878
0.1501
0.7410
56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
8.475e+004
8.505e+004
4.659e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
9.765e+004
9.794e+004
5.173e+005
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
(lbmole/ft3)
63
CO2 App WT Con
(lbmol/lb)
64
LHV Mass Basis (Std)
(Btu/lb)
65
Phase Fraction [Vol. Basis]
0.9978
0.9978
5.088e-005
2.106e-003
66
Phase Fraction [Mass Basis]
0.9942
0.9942
1.330e-004
5.619e-003
67
Phase Fraction [Act. Vol. Basis]
0.9992
0.9992
1.995e-005
7.839e-004
68
Mass Exergy
523.9
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
11.99
11.97
51.60
18.03
0.7328
0.7306
1.136
3.495
8.789
8.745
58.61
63.00
0.2286
8.985
1.146e+004
1.145e+004
7.990
7.951
36.26
18.39
0.6663
0.6642
0.7028
1.020 39.33 1.765e+004
8142
8183
1.003e+004
---
---
1.465e-002
---
---
1.286e-002
1.261e-003
---
---
2.195e-004
2.002e-005
7066
7106
9030
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
979.1 20.21
2.182
---
Page 165 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 57 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Liquid Phase
Aqueous Phase
(psia)
30.10
---
---
---
(Cost/s)
0.0000
0.0000
0.0000
0.0000
(ACFM)
44.65
44.65
---
---
(lbmole/ft3)
1.945
1.942
1.182
3.453
Specific Heat
(Btu/lbmole-F)
7.990
7.951
Std. Gas Flow
(MMSCFD)
17.86
17.79
23.33
23.25
(lb/ft3) (USGPS)
4.479e-003
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
(Btu/lb)
61.00 1.111e-004
18.39 6.677e-002 62.25 4.367e-003
---
1.136
0.7305
0.2375
11.64
11.64
9.183
7.895
---
---
---
---
0.0000
---
---
---
1.331
1.333
1.058
1.121
1.503
1.510
1.717
1.147
5157
---
---
---
---
0.1099
8.555
0.7502
3.167e-002
3.160e-002
59.32
63.31
3.181e+006
3.169e+006
0.2259
8.942
3.769e-003 (ft3/lbmole)
---
36.26 5.523e-004
1.365
0.0000
1.000
1.000
1.369
0.8803
0.2861
430.0
---
---
---
0.9962
0.9962
0.0000
0.0037
(dyne/cm)
70.27
46.22
70.27
(Btu/hr-ft-F)
---
6.120e-002
0.1213
0.3603
---
1.539e-002
8.032
0.7571
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
6.005
5.965
34.27
16.41
0.5007
0.4983
0.6643
0.9101
5.316
5.267
21.12
16.04
0.4432
0.4400
0.4094
0.8898
---
5.250
24.58
15.89
---
0.4387
0.4764
0.8814
---
1.514
1.475
---
---
159.7
---
---
3.169e+006 ---
3.169e+006 ---
48
1.158 2.883e+004
4820
4516
0.2259
8.942
---
---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9962
LIQUID VOLUME FRACTION
54
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
55
H2O
9.2668
0.0047
166.9423
0.0071
11.4541
0.0027
56
Oxygen
130.6354
0.0665
4180.3321
0.1774
251.5990
0.0583
57
Methane
78.7303
0.0401
1263.0621
0.0536
288.8683
0.0669
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1200.5227
0.6110
2420.2538
0.1027
2372.2267
0.5494
60
Ethane
23.3592
0.0119
702.4097
0.0298
135.2215
0.0313
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
11.9317
0.0061
525.1126
0.0223
43.5653
0.0101
63
Nitrogen
510.1368
0.2596
14290.4625
0.6064
1213.4672
0.2810
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.1978
0.0001
12.0839
0.0005
0.8136
0.0002
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
1964.9702
1.0000
1.0000
4317.6702
69
Aspen Technology Inc. Licensed to: LEGENDS
23565.9660
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 166 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 57 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9962 LIQUID VOLUME FRACTION
15
CO
0.1895
0.0001
5.3071
0.0002
0.4546
0.0001
16
H2O
1.9239
0.0010
34.6590
0.0015
2.3780
0.0006
17
Oxygen
130.6342
0.0667
4180.2936
0.1784
251.5967
0.0584
18
Methane
78.7297
0.0402
1263.0531
0.0539
288.8662
0.0670
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1200.5187
0.6133
2420.2458
0.1033
2372.2189
0.5506
21
Ethane
23.3586
0.0119
702.3901
0.0300
135.2177
0.0314
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
11.9284
0.0061
524.9657
0.0224
43.5531
0.0101
24
Nitrogen
510.1305
0.2606
14290.2853
0.6099
1213.4521
0.2817
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1507
0.0001
9.2079
0.0004
0.6200
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
1957.5642
1.0000
1.0000
4308.3572
1.0000
23430.4075
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
3.092e-005 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0078
0.1291
0.1413
0.0451
0.0097
0.0441
36
Oxygen
0.0008
0.0129
0.0250
0.0080
0.0015
0.0069
37
Methane
0.0006
0.0092
0.0090
0.0029
0.0021
0.0094
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0019
0.0318
0.0039
0.0012
0.0038
0.0174
40
Ethane
0.0007
0.0107
0.0196
0.0063
0.0038
0.0172
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0007
0.0113
0.0303
0.0097
0.0025
0.0114
43
Nitrogen
0.0013
0.0222
0.0378
0.0120
0.0032
0.0146
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0470
0.7727
2.8680
0.9148
0.1931
0.8790
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0608
1.0000
3.1349
1.0000
0.2197
1.0000
49
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
3.738e-003 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
7.3351
0.9986
132.1420
0.9979
9.0664
0.9970
55
Oxygen
0.0004
0.0001
0.0134
0.0001
0.0008
0.0001
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0020
0.0003
0.0041
0.0000
0.0040
0.0004
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0027
0.0004
0.1167
0.0009
0.0097
0.0011
62
Nitrogen
0.0050
0.0007
0.1394
0.0011
0.0118
0.0013
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0001
0.0000
0.0080
0.0001
0.0005
0.0001
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
7.3453
1.0000
132.4236
1.0000
9.0933
1.0000
68 69
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Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 167 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 57 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
CO
13
H2O
LIGHT
HEAVY
928.8
13.01
9.912e-004
14
Oxygen
410.8
5.180
15
Methane
530.4
4.356
16
H2S
2224
7.612e-003
9.842e-004 1167 5.141e+005
---
---
---
Hydrogen
1145
19.30
2213
18
Ethane
135.5
1.112
19
Propane
---
---
---
20
CO2
13.52
0.5381
16.89
21
Nitrogen
305.2
11.74
384.8
---
---
---
---
---
17
22
Air
23
Mercury
24
MEAmine
25
Ammonia
1.211e-002
4.312
---
---
UNIT OPERATIONS
27 28 29
---
9.965e-005
---
26
3.122e+007
FEED TO
PRODUCT FROM
Mixer:
MIX-102 Cooler:
LOGICAL CONNECTION E-105
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
4940 psia 1965 lbmole/hrMass:
40
2.357e+004 lb/hrStd Ideal Liq Volume:
4318 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 58
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
7276
7246
60
Molar Enthalpy
(Btu/lbmole)
-5210
-4829
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Liquid Phase
0.9943
0.9943
0.0057
(F)
94.55
94.55
94.55
(psia)
4820
4820
4820
3256
3238
18.71
(lbmole/hr) (lb/hr)
4.521e+004
23.85
4.488e+004
23.89
(Btu/hr)
-1.697e+007
-1.563e+007
(barrel/day)
* 5.270e+006
5.240e+006
64
328.2 30.09 -7.123e+004 16.91 -1.332e+006 29.42
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Vapour Phase
Liquid Phase
13.88
13.86
17.55
0.7417
0.7386
2.706
Aspen HYSYS Version 8.8 (34.0.0.8909)
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1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 58 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-375.2
-348.3
-4059
15
Mass Entropy
(Btu/lb-F)
1.718
1.723
0.9639
16
Heat Capacity
8.581
8.522
18.78
17
Mass Heat Capacity
0.6180
0.6147
18
LHV Molar Basis (Std)
(Btu/lbmole)
8.968e+004
8.976e+004
7.589e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
1.030e+005
1.030e+005
9.836e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
10.30 1.877e+004
10.24 1.874e+004
47.48 29.55
1.070
7418
7431
5606
---
---
1.455
(lbmole/ft3)
---
---
3.955e-003
(lbmol/lb)
---
---
8.331e-005
(Btu/lb)
6459
6475
Phase Fraction [Vol. Basis]
0.9959
0.9959
4.135e-003
26
Phase Fraction [Mass Basis]
0.9927
0.9927
7.260e-003
27
Phase Fraction [Act. Vol. Basis]
0.9984
0.9984
1.575e-003
28
Mass Exergy
(Btu/lb)
445.7
---
29
Partial Pressure of CO2
(psia)
34.78
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
4325
---
(ACFM)
73.05
73.05
---
(lbmole/ft3)
1.913
1.910
2.658
Specific Heat
(Btu/lbmole-F)
8.581
8.522
18.78
Std. Gas Flow
(MMSCFD)
29.60
29.43
0.1700
26.56
26.48
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
1.437e-002
(Btu/lb)
46.64 1.437e-002
---
1.097
0.2995
11.10
11.09
12.17
---
---
---
0.0000
---
---
1.301
1.304
1.118
1.543
1.553
1.275
4826
---
---
---
0.1039
0.3464
3.667e-002
3.661e-002
47.69
5.270e+006
5.240e+006
29.42
5.745e-003 (ft3/lbmole)
---
1.348
0.0000
1.000
1.354
0.3696
347.6
---
---
0.9943
0.9943
0.0057
(dyne/cm)
44.24
(Btu/hr-ft-F)
---
5.552e-002
0.3014
---
1.704e-002
0.2634
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
44.24
6.595
6.536
16.79
0.4750
0.4715
0.9570
5.562
5.489
14.73
0.4006
0.3959
0.8393
6.093
5.459
15.20
0.4389
0.3938
0.8662
1.408
1.561
1.235
---
---
239.1
---
---
5.240e+006 ---
5.240e+006 ---
4505 29.42 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 169 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 58 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9943
LIQUID VOLUME FRACTION
15
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
16
H2O
9.2845
0.0029
167.2607
0.0037
11.4759
0.0016
17
Oxygen
311.9685
0.0958
9982.9913
0.2208
600.8400
0.0826
18
Methane
186.2348
0.0572
2987.7458
0.0661
683.3116
0.0939
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1675.5884
0.5146
3377.9863
0.0747
3310.9542
0.4550
21
Ethane
49.3871
0.0152
1485.0654
0.0328
285.8912
0.0393
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
23.3883
0.0072
1029.3111
0.0228
85.3954
0.0117
24
Nitrogen
831.2466
0.2553
23285.7121
0.5150
1977.2941
0.2718
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1983
0.0001
12.1117
0.0003
0.8155
0.0001
28
Ammonia
168.5154
0.0518
2869.8180
0.0635
318.9647
0.0438
29
Total
3256.2735
1.0000
45210.9342
1.0000
7276.0502
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9943 LIQUID VOLUME FRACTION
34
CO
0.4617
0.0001
12.9315
0.0003
1.1077
0.0002
35
H2O
1.0154
0.0003
18.2934
0.0004
1.2551
0.0002
36
Oxygen
311.9482
0.0964
9982.3432
0.2224
600.8010
0.0829
37
Methane
186.2335
0.0575
2987.7259
0.0666
683.3071
0.0943
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1675.5476
0.5175
3377.9041
0.0753
3310.8736
0.4569
40
Ethane
49.3870
0.0153
1485.0617
0.0331
285.8904
0.0395
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
23.3609
0.0072
1028.1076
0.0229
85.2956
0.0118
43
Nitrogen
831.2237
0.2567
23285.0686
0.5188
1977.2395
0.2729
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.1795
0.0001
10.9640
0.0002
0.7382
0.0001
47
Ammonia
158.2086
0.0489
2694.2933
0.0600
299.4560
0.0413
48
Total
3237.5662
1.0000
44882.6933
1.0000
7245.9642
1.0000
49
Liquid Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
5.745e-003 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0003
0.0000
0.0000
0.0000
54
H2O
8.2690
0.4420
148.9673
0.4538
10.2208
0.3397
55
Oxygen
0.0203
0.0011
0.6481
0.0020
0.0390
0.0013
56
Methane
0.0012
0.0001
0.0198
0.0001
0.0045
0.0002
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0408
0.0022
0.0822
0.0003
0.0806
0.0027
59
Ethane
0.0001
0.0000
0.0038
0.0000
0.0007
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0273
0.0015
1.2035
0.0037
0.0998
0.0033
62
Nitrogen
0.0230
0.0012
0.6435
0.0020
0.0546
0.0018
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0188
0.0010
1.1476
0.0035
0.0773
0.0026
66
Ammonia
10.3068
0.5509
175.5248
0.5347
19.5086
0.6484
67
Total
18.7073
1.0000
328.2408
1.0000
30.0861
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 170 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 58 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
13
H2O
14
Oxygen
89.00
89.00
---
15
Methane
871.8
871.8
---
---
---
---
16
257.1
257.1
7.096e-004
H2S
---
7.096e-004
---
17
Hydrogen
237.4
237.4
---
18
Ethane
2286
2286
---
19
Propane
---
---
---
20
CO2
4.936
4.936
---
21
Nitrogen
209.1
209.1
---
---
---
---
---
---
---
22
Air
23
Mercury
24
MEAmine
5.520e-002
5.520e-002
---
25
Ammonia
8.870e-002
8.870e-002
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Component Splitter:
D-12
LOGICAL CONNECTION
Mixer:
MIX-102
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
4820 psia 3256 lbmole/hrMass:
40
4.521e+004 lb/hrStd Ideal Liq Volume:
7276 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 59
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
6957
6950
60
Molar Enthalpy
(Btu/lbmole)
-4239
-4012
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Aqueous Phase
0.9981
0.9981
0.0019
(F)
97.00*
97.00
97.00
(psia)
4940*
4940
4940
3088
3082
5.921
(lbmole/hr) (lb/hr)
4.234e+004
23.32
4.223e+004
23.34
(Btu/hr)
-1.309e+007
-1.236e+007
(barrel/day)
* 4.999e+006
4.989e+006
64
106.8 7.331 -1.223e+005 13.43 -7.242e+005 7.208
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Vapour Phase
Aqueous Phase
13.71
13.70
18.03
0.7351
0.7340
3.492
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 171 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 59 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-309.1
-292.7
-6784
15
Mass Entropy
(Btu/lb-F)
1.701
1.703
0.7447
16
Heat Capacity
8.210
8.190
18.39
17
Mass Heat Capacity
0.5987
0.5976
1.020
18
LHV Molar Basis (Std)
(Btu/lbmole)
8.714e+004
8.731e+004
19
HHV Molar Basis (Std)
(Btu/lbmole)
9.974e+004
9.989e+004
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
23
CO2 App WT Con
(lbmol/lb)
24
LHV Mass Basis (Std)
(Btu/lb)
25
Phase Fraction [Vol. Basis]
0.9989
0.9989
1.054e-003
26
Phase Fraction [Mass Basis]
0.9975
0.9975
2.521e-003
27
Phase Fraction [Act. Vol. Basis]
0.9996
0.9996
4.037e-004
28
Mass Exergy
(Btu/lb)
457.1
---
29
Partial Pressure of CO2
(psia)
37.48
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
10.08 1.796e+004
10.06 1.795e+004
62.96 7.248
33.42 1.764e+004
7273
7289
---
---
978.6
---
---
1.467e-003
---
---
2.331e-005
6355
6371
37.00
1.853
---
(ACFM)
69.98
69.98
---
(lbmole/ft3)
1.897
1.896
3.453
Specific Heat
(Btu/lbmole-F)
8.210
8.190
Std. Gas Flow
(MMSCFD)
28.07
28.01
26.02
25.98
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
3.523e-003
(Btu/lb)
62.25 3.523e-003
---
1.127
0.2368
10.85
10.85
7.791
---
---
---
0.0000
---
---
1.319
1.320
1.121
1.521
1.524
1.147
5131
---
---
---
0.1045
0.7357
3.621e-002
3.619e-002
63.31
4.999e+006
4.989e+006
7.208
1.917e-003 (ft3/lbmole)
---
18.39 5.382e-002
1.360
0.0000
1.000
1.362
0.2864
374.2
---
---
0.9981
0.9981
0.0019
(dyne/cm)
70.07
(Btu/hr-ft-F)
---
5.611e-002
0.3611
---
1.684e-002
0.7420
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
70.07
6.224
6.204
16.41
0.4539
0.4527
0.9099
5.399
5.375
16.04
0.3937
0.3922
0.8894
5.732
5.359
15.88
0.4180
0.3911
0.8806
1.432
1.528
1.158
---
---
---
---
---
4560
4.989e+006 ---
4.989e+006 ---
7.208 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 172 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 59 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9981
LIQUID VOLUME FRACTION
15
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
16
H2O
9.2845
0.0030
167.2607
0.0040
11.4759
0.0016
17
Oxygen
311.9685
0.1010
9982.9913
0.2358
600.8400
0.0864
18
Methane
186.2348
0.0603
2987.7458
0.0706
683.3116
0.0982
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1675.5884
0.5427
3377.9863
0.0798
3310.9542
0.4759
21
Ethane
49.3871
0.0160
1485.0654
0.0351
285.8912
0.0411
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
23.3883
0.0076
1029.3111
0.0243
85.3954
0.0123
24
Nitrogen
831.2466
0.2692
23285.7121
0.5500
1977.2941
0.2842
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1983
0.0001
12.1117
0.0003
0.8155
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
3087.7581
1.0000
1.0000
6957.0856
1.0000
42341.1161
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9981 LIQUID VOLUME FRACTION
34
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
35
H2O
3.3724
0.0011
60.7549
0.0014
4.1685
0.0006
36
Oxygen
311.9680
0.1012
9982.9747
0.2364
600.8390
0.0865
37
Methane
186.2348
0.0604
2987.7457
0.0707
683.3116
0.0983
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1675.5869
0.5437
3377.9832
0.0800
3310.9512
0.4764
40
Ethane
49.3871
0.0160
1485.0654
0.0352
285.8912
0.0411
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
23.3858
0.0076
1029.2016
0.0244
85.3863
0.0123
43
Nitrogen
831.2426
0.2697
23285.5981
0.5513
1977.2844
0.2845
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.1982
0.0001
12.1075
0.0003
0.8152
0.0001
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
3081.8374
1.0000
1.0000
6949.7550
1.0000
49
42234.3631
Aqueous Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.917e-003 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
5.9120
0.9985
106.5058
0.9977
7.3075
0.9969
55
Oxygen
0.0005
0.0001
0.0166
0.0002
0.0010
0.0001
56
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0015
0.0003
0.0031
0.0000
0.0030
0.0004
59
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
0.0025
0.0004
0.1095
0.0010
0.0091
0.0012
62
Nitrogen
0.0041
0.0007
0.1140
0.0011
0.0097
0.0013
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
0.0001
0.0000
0.0041
0.0000
0.0003
0.0000
66
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Total
5.9207
1.0000
106.7531
1.0000
7.3305
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 173 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 59 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
CO
13
H2O Oxygen
15
Methane
1154
Hydrogen
2188
---
1.096e-003
---
4.979e+005
H2S
17
HEAVY ---
1.096e-003
14
16
LIGHT 2188
1154
---
4.979e+005
---
---
---
2117
---
2117
18
Ethane
19
Propane
---
---
---
20
CO2
18.06
---
18.06
21
Nitrogen
392.4
---
392.4
---
---
---
22
3.073e+007
Air
---
3.073e+007
23
Mercury
---
---
---
24
MEAmine
5.662
---
5.662
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Valve:
VLV-101 Component Splitter:
30
LOGICAL CONNECTION D-12
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 4940 psia
3088 lbmole/hrMass:
40
4.234e+004 lb/hrStd Ideal Liq Volume:
6957 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 60
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
333.5
333.5
(psia)
4940*
4940
168.5
168.5
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
2870
2870
319.0
319.0
-2.301e+004 27.30 -3.877e+006 320.9*
(barrel/day)
64
-2.301e+004 27.30 -3.877e+006 320.9
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Liquid Phase 17.03
17.03
1.216
1.216
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 174 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 60 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Density
13
Act. Volume Flow
14
(lb/ft3)
Liquid Phase 20.70
20.70
(barrel/day)
592.6
592.6
Mass Enthalpy
(Btu/lb)
-1351
-1351
15
Mass Entropy
(Btu/lb-F)
1.603
1.603
16
Heat Capacity
26.30
26.30
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
1.362e+005
1.362e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
1.627e+005
1.627e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.544
9551
1.544
9551
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
7998
7998
Phase Fraction [Vol. Basis]
0.0000
1.000
26
Phase Fraction [Mass Basis]
0.0000
1.000
27
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
28
Mass Exergy
(Btu/lb)
227.3
---
29
Partial Pressure of CO2
(psia)
0.0000
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
2.258
2.258
Specific Heat
(Btu/lbmole-F)
26.30
26.30
Std. Gas Flow
(MMSCFD)
1.532
1.532
(lb/ft3)
38.46
38.46
(USGPS)
0.2881
0.2881
0.4774
0.4774
12.24
12.24
---
---
(psia)
(Btu/lbmole)
0.0000
---
1.082
1.082
2.648
2.648
---
---
(cSt)
0.1228
0.1228
(lb/ft3)
38.22
38.22
320.9
320.9
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.8227
0.8227
-827.2
---
0.0000
1.0000
(dyne/cm)
---
---
(Btu/hr-ft-F)
0.1332
0.1332
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
4.071e-002
4.071e-002
24.31
24.31
1.427
1.427
9.929
9.929
0.5830
0.5830
17.77
17.77
1.043
1.043
1.480
1.480
(psia)
210.5
210.5
(psia)
210.5
210.5
320.9
320.9
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 175 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 60 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
29
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
48
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
0.0000
0.0000
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 176 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 60 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Cooler:
E-106
LOGICAL CONNECTION
Component Splitter:
13
D-12
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 4940 psia
168.5 lbmole/hrMass:
23
2870 lb/hr Std Ideal Liq Volume:
319.0 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 61
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
6957
6950
43
Molar Enthalpy
(Btu/lbmole)
-4239
-4011
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Aqueous Phase
0.9981
0.9981
0.0019
(F)
96.93
96.93
96.93
(psia)
4820*
4820
4820
3088
3082
5.951
(lbmole/hr) (lb/hr)
4.234e+004
23.38
4.223e+004
23.40
(Btu/hr)
-1.309e+007
-1.236e+007
(barrel/day)
* 4.999e+006
4.989e+006
47
107.3 7.367 -1.223e+005 13.43 -7.279e+005 7.244
PROPERTIES
48 49
Overall
Vapour Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-309.1
-292.7
-6785
55
Mass Entropy
(Btu/lb-F)
1.705
1.707
0.7447
56
Heat Capacity
8.199
8.180
18.40
57
Mass Heat Capacity
0.5980
0.5969
1.020
58
LHV Molar Basis (Std)
(Btu/lbmole)
8.714e+004
8.731e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
9.974e+004
9.989e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
(lbmole/ft3)
63
CO2 App WT Con
(lbmol/lb)
64
LHV Mass Basis (Std)
(Btu/lb)
65
Phase Fraction [Vol. Basis]
0.9989
0.9989
1.059e-003
66
Phase Fraction [Mass Basis]
0.9975
0.9975
2.534e-003
67
Phase Fraction [Act. Vol. Basis]
0.9996
0.9996
3.977e-004
68
Mass Exergy
455.0
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
13.71
13.70
18.03
0.7204
0.7193
3.491
9.879
9.858
62.94
1.832e+004
1.831e+004
7.286
33.04 1.764e+004
7273
7289
---
---
978.6
---
---
1.454e-003
---
---
2.309e-005
6355
6371
35.37
1.832
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 177 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 61 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Aqueous Phase
(psia)
36.57
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
71.41
71.41
---
(lbmole/ft3)
1.897
1.896
3.453
Specific Heat
(Btu/lbmole-F)
8.199
8.180
Std. Gas Flow
(MMSCFD)
28.07
28.01
26.02
25.98
(lb/ft3) (USGPS)
3.542e-003
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
(Btu/lb)
62.25 3.542e-003
---
1.122
0.2311
10.85
10.85
7.792
---
---
---
0.0000
---
---
1.320
1.321
1.121
1.520
1.523
1.147
5139
---
---
---
0.1058
0.7363
3.621e-002
3.619e-002
63.31
4.999e+006
4.989e+006
7.244
1.927e-003 (ft3/lbmole)
---
18.40 5.409e-002
1.388
0.0000
1.000
1.390
0.2864
374.7
---
---
0.9981
0.9981
0.0019
(dyne/cm)
70.08
(Btu/hr-ft-F)
---
5.579e-002
0.3611
---
1.671e-002
0.7424
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
70.08
6.214
6.194
16.41
0.4531
0.4520
0.9101
5.395
5.370
16.04
0.3934
0.3919
0.8895
5.714
5.342
15.84
0.4167
0.3898
0.8786
1.435
1.531
1.161
---
---
---
---
---
4446
4.989e+006 ---
4.989e+006 ---
48
7.244 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9981
LIQUID VOLUME FRACTION
54
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
55
H2O
9.2845
0.0030
167.2607
0.0040
11.4759
0.0016
56
Oxygen
311.9685
0.1010
9982.9913
0.2358
600.8400
0.0864
57
Methane
186.2348
0.0603
2987.7458
0.0706
683.3116
0.0982
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1675.5884
0.5427
3377.9863
0.0798
3310.9542
0.4759
60
Ethane
49.3871
0.0160
1485.0654
0.0351
285.8912
0.0411
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
23.3883
0.0076
1029.3111
0.0243
85.3954
0.0123
63
Nitrogen
831.2466
0.2692
23285.7121
0.5500
1977.2941
0.2842
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.1983
0.0001
12.1117
0.0003
0.8155
0.0001
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
3087.7581
1.0000
1.0000
6957.0856
69
Aspen Technology Inc. Licensed to: LEGENDS
42341.1161
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 178 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 61 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9981 LIQUID VOLUME FRACTION
15
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
16
H2O
3.3425
0.0011
60.2148
0.0014
4.1314
0.0006
17
Oxygen
311.9680
0.1012
9982.9749
0.2364
600.8390
0.0865
18
Methane
186.2348
0.0604
2987.7457
0.0707
683.3116
0.0983
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1675.5869
0.5437
3377.9833
0.0800
3310.9512
0.4764
21
Ethane
49.3871
0.0160
1485.0654
0.0352
285.8912
0.0411
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
23.3858
0.0076
1029.2020
0.0244
85.3864
0.0123
24
Nitrogen
831.2426
0.2697
23285.5995
0.5513
1977.2845
0.2845
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
3081.8075
1.0000
1.0000
6949.7182
1.0000
30
42233.8250
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.927e-003 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
5.9420
0.9986
107.0458
0.9977
7.3445
0.9969
36
Oxygen
0.0005
0.0001
0.0164
0.0002
0.0010
0.0001
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0015
0.0003
0.0030
0.0000
0.0029
0.0004
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0025
0.0004
0.1090
0.0010
0.0090
0.0012
43
Nitrogen
0.0040
0.0007
0.1126
0.0010
0.0096
0.0013
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0001
0.0000
0.0043
0.0000
0.0003
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
5.9506
1.0000
107.2912
1.0000
7.3674
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
52
CO
53
H2O
54
Oxygen
55
Methane
56
H2S
57
Hydrogen
LIGHT 2230 1.086e-003 1174 5.063e+005
HEAVY ---------
2230 1.086e-003 1174 5.063e+005
---
---
---
2168
---
2168
58
Ethane
59
Propane
---
---
---
60
CO2
18.22
---
18.22
61
Nitrogen
399.4
---
399.4
---
---
---
62
Air
3.104e+007
---
3.104e+007
63
Mercury
---
---
---
64
MEAmine
5.463
---
5.463
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 179 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 61 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO Separator:
PRODUCT FROM
LOGICAL CONNECTION
S-2 SEPARADOR SECUNDARIOValve: CARGA
VLV-101
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 4820 psia
3088 lbmole/hrMass:
23
4.234e+004 lb/hrStd Ideal Liq Volume:
6957 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 62
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.0000
0.0000
1.0000
(F)
96.93
96.93
96.93
(psia)
4820
4820
4820
5.951
0.0000
5.951
107.3
0.0000
107.3
7.367
0.0000
(lbmole/hr) (lb/hr)
(Btu/hr)
-1.223e+005 13.43 -7.279e+005 7.244*
(barrel/day)
47
-4011 23.40 0.0000 0.0000
7.367 -1.223e+005 13.43 -7.279e+005 7.244
PROPERTIES
48 49
Overall
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Vapour Phase
Aqueous Phase
18.03
13.70
18.03
3.491
0.7193
3.491
62.94
9.858
62.94
(barrel/day)
7.286
0.0000
7.286
Mass Enthalpy
(Btu/lb)
-6785
-292.7
-6785
55
Mass Entropy
(Btu/lb-F)
0.7447
1.707
0.7447
56
Heat Capacity
57
Mass Heat Capacity
58
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F)
18.40
8.180
18.40
(Btu/lb-F)
1.020
0.5969
1.020
LHV Molar Basis (Std)
(Btu/lbmole)
33.04
59
HHV Molar Basis (Std)
(Btu/lbmole)
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
(lbmole/ft3)
1.454e-003
63
CO2 App WT Con
(lbmol/lb)
2.309e-005
64
LHV Mass Basis (Std)
65
Phase Fraction [Vol. Basis]
66
(Btu/lb)
9.989e+004
978.6
7289
35.37
---
33.04 1.764e+004 978.6 35.37
---
1.454e-003
---
2.309e-005
1.832
6371
1.832
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
67
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
68
Mass Exergy
17.40
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
1.764e+004
8.731e+004
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 180 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 62 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Specific Heat
(Btu/lbmole-F)
17
Std. Gas Flow
(MMSCFD)
18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46 47
Vapour Phase
Aqueous Phase
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
3.453
1.896
3.453
(lb/ft3)
18.40 5.409e-002 62.25
(USGPS)
3.542e-003
8.180 0.0000 25.98 ---
18.40 5.409e-002 62.25 3.542e-003
---
1.122
0.2311
7.792
10.85
7.792
---
---
---
0.0000
---
---
1.121
1.321
1.121
1.147
1.523
1.147
---
---
---
(cSt)
0.7363
0.1058
0.7363
(lb/ft3)
63.31
(psia)
(Btu/lbmole)
(barrel/day) (ft3/lbmole) (Btu/lb)
3.619e-002
63.31
7.244
0.0000
1.000
0.0000
7.244 1.000
0.2864
1.390
0.2864
-781.3
---
---
0.0000
0.0000
1.0000
(dyne/cm)
70.08
(Btu/hr-ft-F)
0.3611
5.579e-002
0.3611
0.7424
1.671e-002
0.7424
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
70.08
16.41
6.194
16.41
0.9101
0.4520
0.9101
16.04
5.370
16.04
0.8895
0.3919
0.8895
15.84
5.342
15.84
0.8786
0.3898
0.8786
1.161
1.531
1.161
---
---
---
4446
---
4446
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
7.244
0.0000
7.244
Viscosity Index
-1.313
---
---
(Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
H2O
5.9420
0.9986
107.0458
0.9977
7.3445
0.9969
56
Oxygen
0.0005
0.0001
0.0164
0.0002
0.0010
0.0001
57
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0015
0.0003
0.0030
0.0000
0.0029
0.0004
60
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0025
0.0004
0.1090
0.0010
0.0090
0.0012
63
Nitrogen
0.0040
0.0007
0.1126
0.0010
0.0096
0.0013
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0001
0.0000
0.0043
0.0000
0.0003
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
5.9506
1.0000
107.2912
1.0000
7.3674
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 181 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 62 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0001
0.0000
0.0003
0.0000
0.0002
16
H2O
0.0000
0.0011
0.0000
0.0014
0.0000
0.0006
17
Oxygen
0.0000
0.1012
0.0000
0.2364
0.0000
0.0865
18
Methane
0.0000
0.0604
0.0000
0.0707
0.0000
0.0983
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.5437
0.0000
0.0800
0.0000
0.4764
21
Ethane
0.0000
0.0160
0.0000
0.0352
0.0000
0.0411
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0076
0.0000
0.0244
0.0000
0.0123
24
Nitrogen
0.0000
0.2697
0.0000
0.5513
0.0000
0.2845
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0001
0.0000
0.0003
0.0000
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
5.9420
0.9986
107.0458
0.9977
7.3445
0.9969
36
Oxygen
0.0005
0.0001
0.0164
0.0002
0.0010
0.0001
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0015
0.0003
0.0030
0.0000
0.0029
0.0004
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0025
0.0004
0.1090
0.0010
0.0090
0.0012
43
Nitrogen
0.0040
0.0007
0.1126
0.0010
0.0096
0.0013
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0001
0.0000
0.0043
0.0000
0.0003
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
5.9506
1.0000
107.2912
1.0000
7.3674
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
52
CO
53
H2O
54
Oxygen
55
Methane
56
H2S
57
Hydrogen
LIGHT 2230 1.086e-003 1174 5.063e+005
HEAVY ---------
2230 1.086e-003 1174 5.063e+005
---
---
---
2168
---
2168
58
Ethane
59
Propane
---
---
---
60
CO2
18.22
---
18.22
61
Nitrogen
399.4
---
399.4
---
---
---
62
Air
3.104e+007
---
3.104e+007
63
Mercury
---
---
---
64
MEAmine
5.463
---
5.463
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 182 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 62 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Separator:
LOGICAL CONNECTION
S-2 SEPARADOR SECUNDARIO CARGA
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
4820 psia 5.951 lbmole/hrMass:
23
107.3 lb/hr Std Ideal Liq Volume:
7.367 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 63
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
6950
6950
43
Molar Enthalpy
(Btu/lbmole)
-4011
-4011
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Aqueous Phase
1.0000
1.0000
0.0000
(F)
96.93
96.93
96.93
(psia)
4820
4820
4820
3082
3082
0.0000
(lbmole/hr) (lb/hr)
4.223e+004
23.40
4.223e+004
23.40
0.0000 0.0000 -1.223e+005 13.43
(Btu/hr)
-1.236e+007
-1.236e+007
0.0000
(barrel/day)
* 4.989e+006
4.989e+006
0.0000
47
PROPERTIES
48 49
Overall
Vapour Phase
Aqueous Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-292.7
-292.7
-6785
55
Mass Entropy
(Btu/lb-F)
1.707
1.707
0.7447
56
Heat Capacity
8.180
8.180
18.40
57
Mass Heat Capacity
0.5969
0.5969
1.020
58
LHV Molar Basis (Std)
(Btu/lbmole)
8.731e+004
8.731e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
9.989e+004
9.989e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66 67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
13.70
18.03
0.7193
0.7193
3.491
9.858
9.858
1.831e+004
1.831e+004
62.94 0.0000
33.04 1.764e+004
7289
7289
978.6
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
6371
6371
1.832
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
455.7
---
---
Licensed to: LEGENDS
(Btu/lb)
13.70
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 183 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 63 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Aqueous Phase
(psia)
36.57
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
71.41
71.41
---
(lbmole/ft3)
1.896
1.896
3.453
Specific Heat
(Btu/lbmole-F)
8.180
8.180
18.40
Std. Gas Flow
(MMSCFD)
28.01
28.01
0.0000
(lb/ft3)
25.98
25.98
62.25
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.122
0.2311
10.85
10.85
7.792
---
---
---
0.0000
---
---
1.321
1.321
1.121
1.523
1.523
1.147
4625
---
---
0.1058
0.1058
0.7363
3.619e-002
3.619e-002
63.31
4.989e+006
4.989e+006
0.0000
0.0000
0.0000
1.000
1.390
1.390
0.2864
337.5
---
---
1.0000
1.0000
0.0000
---
---
70.08
5.579e-002
5.579e-002
0.3611
1.671e-002
1.671e-002
0.7424
6.194
6.194
16.41
0.4520
0.4520
0.9101
5.370
5.370
16.04
0.3919
0.3919
0.8895
5.342
5.342
15.84
0.3898
0.3898
0.8786
1.531
1.531
1.161
---
---
---
---
---
4446
4.989e+006 ---
4.989e+006 ---
48
0.0000 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
54
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
55
H2O
3.3425
0.0011
60.2148
0.0014
4.1314
0.0006
56
Oxygen
311.9680
0.1012
9982.9749
0.2364
600.8390
0.0865
57
Methane
186.2348
0.0604
2987.7457
0.0707
683.3116
0.0983
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
1675.5869
0.5437
3377.9833
0.0800
3310.9512
0.4764
60
Ethane
49.3871
0.0160
1485.0654
0.0352
285.8912
0.0411
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
23.3858
0.0076
1029.2020
0.0244
85.3864
0.0123
63
Nitrogen
831.2426
0.2697
23285.5995
0.5513
1977.2845
0.2845
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
3081.8075
1.0000
1.0000
6949.7182
69
Aspen Technology Inc. Licensed to: LEGENDS
42233.8250
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 184 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 63 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.4617
0.0001
12.9318
0.0003
1.1077
0.0002
16
H2O
3.3425
0.0011
60.2148
0.0014
4.1314
0.0006
17
Oxygen
311.9680
0.1012
9982.9749
0.2364
600.8390
0.0865
18
Methane
186.2348
0.0604
2987.7457
0.0707
683.3116
0.0983
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1675.5869
0.5437
3377.9833
0.0800
3310.9512
0.4764
21
Ethane
49.3871
0.0160
1485.0654
0.0352
285.8912
0.0411
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
23.3858
0.0076
1029.2020
0.0244
85.3864
0.0123
24
Nitrogen
831.2426
0.2697
23285.5995
0.5513
1977.2845
0.2845
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
3081.8075
1.0000
1.0000
6949.7182
1.0000
30
42233.8250
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.9986
0.0000
0.9977
0.0000
0.9969
36
Oxygen
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0003
0.0000
0.0000
0.0000
0.0004
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0004
0.0000
0.0010
0.0000
0.0012
43
Nitrogen
0.0000
0.0007
0.0000
0.0010
0.0000
0.0013
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
52
CO
53
H2O
54
Oxygen
55
Methane
56
H2S
57
Hydrogen
LIGHT 2230 1.086e-003 1174 5.063e+005
HEAVY ---------
2230 1.086e-003 1174 5.063e+005
---
---
---
2168
---
2168
58
Ethane
59
Propane
---
---
---
60
CO2
18.22
---
18.22
61
Nitrogen
399.4
---
399.4
---
---
---
62
Air
3.104e+007
---
3.104e+007
63
Mercury
---
---
---
64
MEAmine
5.463
---
5.463
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 185 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 63 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Conversion Reactor:
T-3 CONVERTIDOR Separator:
13
LOGICAL CONNECTION
S-2 SEPARADOR SECUNDARIO CARGA
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
4820 psia 3082 lbmole/hrMass:
23
4.223e+004 lb/hrStd Ideal Liq Volume:
6950 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 64
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
44
Molar Entropy
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
652.0
652.0
652.0
(psia)
4820
4820
4820
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(Btu/lbmole)
-4658
-4944
-4658
(Btu/lbmole-F)
32.68
32.81
32.68
(Btu/hr)
0.0000
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
47
PROPERTIES
48 49
Overall
Vapour Phase
Liquid Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54 55 56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
1.017e+005
1.030e+005
1.017e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
1.170e+005
1.185e+005
1.170e+005
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
Phase Fraction [Vol. Basis]
66
Phase Fraction [Mass Basis]
67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
(lbmole/ft3)
16.89
16.84
0.3748
0.3753
0.3748
6.313
6.341
6.313
(barrel/day)
0.0000
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-276.6
-292.7
-276.6
Mass Entropy
(Btu/lb-F)
1.940
1.942
1.940
9.485
9.560
9.485
0.5631
0.5659
0.5631
Licensed to: LEGENDS
(lb/ft3)
16.84
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
6948
7016
6948
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
6039
6098
6039
(Btu/lb)
---
---
1.000
0.0000
0.0000
1.000
---
---
---
455.6
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 186 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 64 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Vapour Phase
Liquid Phase
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000 ---
(ACFM)
---
---
(lbmole/ft3)
---
---
---
Specific Heat
(Btu/lbmole-F)
9.485
9.560
9.485
17
Std. Gas Flow
(MMSCFD)
0.0000
18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
0.0000
0.0000
(lb/ft3)
31.97
32.04
31.97
(USGPS)
0.0000
---
0.0000
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
---
1.076
1.078
10.75
10.79
10.75
---
---
---
0.0000
---
---
1.265
1.262
1.265
1.358
1.358
1.358
7709
---
---
0.1787
0.2397
0.1787
4.454e-002
(barrel/day)
4.467e-002
4.454e-002
0.0000
0.0000
0.0000
1.000
0.0000
1.000
(ft3/lbmole)
2.668
2.664
2.668
(Btu/lb)
457.7
---
---
0.0000
0.0000
1.0000
(dyne/cm)
5.316e-003
(Btu/hr-ft-F)
5.156e-002
6.495e-002
5.156e-002
1.807e-002
2.435e-002
1.807e-002
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
5.316e-003
7.499
7.574
7.499
0.4452
0.4483
0.4452
6.985
7.041
6.985
0.4147
0.4168
0.4147
---
7.039
---
---
0.4167
---
---
1.358
---
(psia)
---
---
---
(psia)
---
---
---
0.0000
0.0000
0.0000
---
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0002
0.0000
0.0003
0.0000
0.0002
55
H2O
0.0000
0.0011
0.0000
0.0012
0.0000
0.0006
56
Oxygen
0.0000
0.1253
0.0000
0.2381
0.0000
0.1072
57
Methane
0.0000
0.0739
0.0000
0.0704
0.0000
0.1204
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0000
0.3273
0.0000
0.0392
0.0000
0.2871
60
Ethane
0.0000
0.0190
0.0000
0.0340
0.0000
0.0490
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0000
0.0091
0.0000
0.0239
0.0000
0.0148
63
Nitrogen
0.0000
0.2207
0.0000
0.3670
0.0000
0.2330
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
67
Ammonia
0.0000
0.2232
0.0000
0.2257
0.0000
0.1875
68
Total
0.0000
1.0000
0.0000
1.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 187 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 64 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0002
0.0000
0.0003
0.0000
0.0002
16
H2O
0.0000
0.0013
0.0000
0.0014
0.0000
0.0007
17
Oxygen
0.0000
0.1248
0.0000
0.2364
0.0000
0.1066
18
Methane
0.0000
0.0745
0.0000
0.0707
0.0000
0.1213
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.3211
0.0000
0.0383
0.0000
0.2815
21
Ethane
0.0000
0.0198
0.0000
0.0352
0.0000
0.0507
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0094
0.0000
0.0244
0.0000
0.0152
24
Nitrogen
0.0000
0.2161
0.0000
0.3584
0.0000
0.2281
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0001
0.0000
0.0003
0.0000
0.0001
28
Ammonia
0.0000
0.2328
0.0000
0.2346
0.0000
0.1955
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0002
0.0000
0.0003
0.0000
0.0002
35
H2O
0.0000
0.0011
0.0000
0.0012
0.0000
0.0006
36
Oxygen
0.0000
0.1253
0.0000
0.2381
0.0000
0.1072
37
Methane
0.0000
0.0739
0.0000
0.0704
0.0000
0.1204
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.3273
0.0000
0.0392
0.0000
0.2871
40
Ethane
0.0000
0.0190
0.0000
0.0340
0.0000
0.0490
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0091
0.0000
0.0239
0.0000
0.0148
43
Nitrogen
0.0000
0.2207
0.0000
0.3670
0.0000
0.2330
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
47
Ammonia
0.0000
0.2232
0.0000
0.2257
0.0000
0.1875
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
0.9867
0.9867
---
53
H2O
1.179
1.179
---
54
Oxygen
0.9957
0.9957
---
55
Methane
1.008
1.008
---
---
---
---
56
H2S
57
Hydrogen
0.9811
0.9811
---
58
Ethane
1.037
1.037
---
59
Propane
---
---
---
60
CO2
1.024
1.024
---
61
Nitrogen
0.9794
0.9794
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
1.160
1.160
---
65
Ammonia
1.043
1.043
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 188 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 64 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Conversion Reactor:
13
LOGICAL CONNECTION
T-3 CONVERTIDOR
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
4820 psia 0.0000 lbmole/hrMass:
23
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 65
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
Liquid Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
5634
5634
0.0000
43
Molar Enthalpy
(Btu/lbmole)
-4944
-4944
-4658
44
Molar Entropy
(Btu/lbmole-F)
32.81
32.81
45
Heat Flow
46
Liq Vol Flow @Std Cond
1.0000
1.0000
0.0000
(F)
652.0
652.0
652.0
(psia)
4820
4820
4820
2500
2500
0.0000
(lbmole/hr) (lb/hr)
4.223e+004
4.223e+004
0.0000
32.68
(Btu/hr)
-1.236e+007
-1.236e+007
0.0000
(barrel/day)
* 4.041e+006
4.041e+006
0.0000
47
PROPERTIES
48 49
Overall
Vapour Phase
Liquid Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-292.7
-292.7
-276.6
55
Mass Entropy
(Btu/lb-F)
1.942
1.942
1.940
56
Heat Capacity
9.560
9.560
9.485
57
Mass Heat Capacity
0.5659
0.5659
0.5631
58
LHV Molar Basis (Std)
(Btu/lbmole)
1.030e+005
1.030e+005
1.017e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
1.185e+005
1.185e+005
1.170e+005
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66 67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
16.89
16.84
0.3753
0.3753
0.3748
6.341 2.847e+004
6.341 2.847e+004
6.313 0.0000
7016
7016
6948
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
6098
6098
6039
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
454.1
---
---
Licensed to: LEGENDS
(Btu/lb)
16.89
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 189 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 65 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Liquid Phase
(psia)
45.09
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
111.0
111.0
---
(lbmole/ft3)
1.897
1.897
1.898
Specific Heat
(Btu/lbmole-F)
9.560
9.560
9.485
Std. Gas Flow
(MMSCFD)
22.72
22.72
0.0000
(lb/ft3)
32.04
32.04
31.97
(USGPS)
---
---
---
---
1.076
1.078
10.79
10.79
10.75
---
---
---
0.0000
---
---
1.262
1.262
1.265
1.358
1.358
1.358
7865
---
---
0.2397
0.2397
0.1787
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
4.467e-002
4.467e-002
4.041e+006
4.041e+006
4.454e-002 0.0000
0.0000
0.0000
1.000
(ft3/lbmole)
2.664
2.664
2.668
(Btu/lb)
465.5
---
---
1.0000
1.0000
0.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
5.316e-003
6.495e-002
6.495e-002
5.156e-002
2.435e-002
2.435e-002
1.807e-002
7.574
7.574
7.499
0.4483
0.4483
0.4452
7.041
7.041
6.985
0.4168
0.4168
0.4147
7.039
7.039
---
0.4167
0.4167
---
1.358
1.358
---
(psia)
---
---
---
(psia)
---
---
(Btu/lb-F)
4.041e+006 ---
4.041e+006 ---
48
--0.0000 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
54
CO
0.4617
0.0002
12.9318
0.0003
1.1077
0.0002
55
H2O
3.3425
0.0013
60.2148
0.0014
4.1314
0.0007
56
Oxygen
311.9680
0.1248
9982.9749
0.2364
600.8390
0.1066
57
Methane
186.2348
0.0745
2987.7457
0.0707
683.3116
0.1213
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
802.7822
0.3211
1618.4089
0.0383
1586.2935
0.2815
60
Ethane
49.3871
0.0198
1485.0654
0.0352
285.8912
0.0507
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
23.3858
0.0094
1029.2020
0.0244
85.3864
0.0152
63
Nitrogen
540.3077
0.2161
15135.6397
0.3584
1285.2349
0.2281
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
67
Ammonia
581.8698
0.2328
9909.2435
0.2346
1101.3585
0.1955
68
Total
2499.9377
1.0000
42233.5343
1.0000
5634.3694
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 190 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 65 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.4617
0.0002
12.9318
0.0003
1.1077
0.0002
16
H2O
3.3425
0.0013
60.2148
0.0014
4.1314
0.0007
17
Oxygen
311.9680
0.1248
9982.9749
0.2364
600.8390
0.1066
18
Methane
186.2348
0.0745
2987.7457
0.0707
683.3116
0.1213
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
802.7822
0.3211
1618.4089
0.0383
1586.2935
0.2815
21
Ethane
49.3871
0.0198
1485.0654
0.0352
285.8912
0.0507
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
23.3858
0.0094
1029.2020
0.0244
85.3864
0.0152
24
Nitrogen
540.3077
0.2161
15135.6397
0.3584
1285.2349
0.2281
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
28
Ammonia
581.8698
0.2328
9909.2435
0.2346
1101.3585
0.1955
29
Total
2499.9377
1.0000
42233.5343
1.0000
5634.3694
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0002
0.0000
0.0003
0.0000
0.0002
35
H2O
0.0000
0.0011
0.0000
0.0012
0.0000
0.0006
36
Oxygen
0.0000
0.1253
0.0000
0.2381
0.0000
0.1072
37
Methane
0.0000
0.0739
0.0000
0.0704
0.0000
0.1204
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.3273
0.0000
0.0392
0.0000
0.2871
40
Ethane
0.0000
0.0190
0.0000
0.0340
0.0000
0.0490
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0091
0.0000
0.0239
0.0000
0.0148
43
Nitrogen
0.0000
0.2207
0.0000
0.3670
0.0000
0.2330
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
47
Ammonia
0.0000
0.2232
0.0000
0.2257
0.0000
0.1875
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
0.9867
0.9867
---
53
H2O
1.179
1.179
---
54
Oxygen
0.9957
0.9957
---
55
Methane
1.008
1.008
---
---
---
---
56
H2S
57
Hydrogen
0.9811
0.9811
---
58
Ethane
1.037
1.037
---
59
Propane
---
---
---
60
CO2
1.024
1.024
---
61
Nitrogen
0.9794
0.9794
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
1.160
1.160
---
65
Ammonia
1.043
1.043
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 191 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 65 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO Cooler:
PRODUCT FROM E-21 CONDENSADOR Conversion Reactor:
13
LOGICAL CONNECTION
T-3 CONVERTIDOR
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
4820 psia 2500 lbmole/hrMass:
23
4.223e+004 lb/hrStd Ideal Liq Volume:
5634 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 66
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.8626
0.8626
0.1374
(F)
87.00*
87.00
87.00
(psia)
4565*
4565
4565
2500
2156
343.5
(lbmole/hr) (lb/hr)
4.223e+004
(barrel/day)
5634 -1.104e+004 24.93
3.613e+004 4942 -8118 25.54
(Btu/hr)
-2.761e+007
-1.751e+007
(barrel/day)
* 4.041e+006
3.488e+006
47
6104 692.5 -2.941e+004 21.07 -1.010e+007 721.7
PROPERTIES
48 49
Overall
Vapour Phase
Liquid Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-653.7
-484.6
-1655
55
Mass Entropy
(Btu/lb-F)
1.476
1.525
1.186
56
Heat Capacity
11.04
9.827
18.65
57
Mass Heat Capacity
0.6535
0.5866
58
LHV Molar Basis (Std)
(Btu/lbmole)
1.030e+005
9.722e+004
1.394e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
1.185e+005
1.112e+005
1.649e+005
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
16.75
17.77
0.8445
0.7725
2.039
14.27
12.94
36.24
1.265e+004
1.193e+004
719.9
1.049
7016
6635
9277
---
---
20.97
(lbmole/ft3)
---
---
2.459e-002
(lbmol/lb)
---
---
6.786e-004
(Btu/lb)
6098
5803
7845
Phase Fraction [Vol. Basis]
0.8771
0.8771
0.1229
66
Phase Fraction [Mass Basis]
0.8555
0.8555
67
Phase Fraction [Act. Vol. Basis]
0.9431
0.9431
68
Mass Exergy
343.4
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
16.89
(Btu/lb)
0.1445 5.690e-002 ---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 192 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 66 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
(psia)
45
True VP at 37.8 C
(psia)
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
Liquid Phase
(psia)
40.73
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
46.53
46.53
---
(lbmole/ft3)
1.897
1.865
2.120
Specific Heat
(Btu/lbmole-F)
11.04
9.827
18.65
Std. Gas Flow
(MMSCFD)
22.72
19.60
3.122
(lb/ft3)
32.04
31.25
37.68
(USGPS)
0.3500
---
0.3500
(psia)
(Btu/lbmole) (cSt)
---
1.007
0.3816
10.79
10.42
12.17
---
---
---
0.0000
---
---
1.219
1.253
1.119
1.491
1.673
1.907
7911
---
---
(lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb)
0.1651
4.467e-002
4.428e-002
36.15
4.041e+006
3.488e+006
721.7
0.1374
0.0000
1.000
1.184
1.295
0.4904
468.3
---
---
0.8626
0.8626
0.1374
(dyne/cm)
22.44
(Btu/hr-ft-F)
---
4.891e-002
---
2.006e-002
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
9.675e-002
---
22.44 0.2277 9.584e-002
9.054
7.841
16.66
0.5359
0.4680
0.9377
7.405
5.874
9.781
0.4383
0.3506
0.5504
15.84
5.850
9.126
0.9377
0.3492
0.5135
0.6968
1.680
2.044
---
---
511.5
---
---
3.489e+006 ---
3.488e+006 ---
48
4059 721.7 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.8626
LIQUID VOLUME FRACTION
54
CO
0.4617
0.0002
12.9318
0.0003
1.1077
0.0002
55
H2O
3.3425
0.0013
60.2148
0.0014
4.1314
0.0007
56
Oxygen
311.9680
0.1248
9982.9749
0.2364
600.8390
0.1066
57
Methane
186.2348
0.0745
2987.7457
0.0707
683.3116
0.1213
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
802.7822
0.3211
1618.4089
0.0383
1586.2935
0.2815
60
Ethane
49.3871
0.0198
1485.0654
0.0352
285.8912
0.0507
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
23.3858
0.0094
1029.2020
0.0244
85.3864
0.0152
63
Nitrogen
540.3077
0.2161
15135.6397
0.3584
1285.2349
0.2281
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.1982
0.0001
12.1074
0.0003
0.8152
0.0001
67
Ammonia
581.8698
0.2328
9909.2435
0.2346
1101.3585
0.1955
68
Total
2499.9377
1.0000
42233.5343
1.0000
5634.3694
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 193 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 66 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.8626 LIQUID VOLUME FRACTION
15
CO
0.4558
0.0002
12.7670
0.0004
1.0936
0.0002
16
H2O
0.0276
0.0000
0.4979
0.0000
0.0342
0.0000
17
Oxygen
302.4065
0.1402
9677.0083
0.2678
582.4240
0.1179
18
Methane
179.2695
0.0831
2876.0034
0.0796
657.7556
0.1331
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
794.8027
0.3686
1602.3222
0.0443
1570.5260
0.3178
21
Ethane
43.8254
0.0203
1317.8243
0.0365
253.6954
0.0513
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
19.2440
0.0089
846.9214
0.0234
70.2637
0.0142
24
Nitrogen
536.4766
0.2488
15028.3201
0.4160
1276.1220
0.2582
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0007
0.0000
0.0400
0.0000
0.0027
0.0000
28
Ammonia
279.9713
0.1298
4767.9118
0.1320
529.9275
0.1072
29
Total
2156.4801
1.0000
36129.6164
1.0000
4941.8446
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.1374 LIQUID VOLUME FRACTION
34
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
35
H2O
3.3148
0.0097
59.7169
0.0098
4.0972
0.0059
36
Oxygen
9.5615
0.0278
305.9667
0.0501
18.4150
0.0266
37
Methane
6.9652
0.0203
111.7423
0.0183
25.5560
0.0369
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
7.9795
0.0232
16.0867
0.0026
15.7675
0.0228
40
Ethane
5.5617
0.0162
167.2411
0.0274
32.1957
0.0465
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
4.1418
0.0121
182.2807
0.0299
15.1227
0.0218
43
Nitrogen
3.8311
0.0112
107.3196
0.0176
9.1130
0.0132
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.1976
0.0006
12.0674
0.0020
0.8125
0.0012
47
Ammonia
301.8985
0.8790
5141.3317
0.8423
571.4310
0.8251
48
Total
343.4576
1.0000
6103.9179
1.0000
692.5248
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
53
H2O
54
Oxygen
5.037
5.037
---
55
Methane
4.099
4.099
---
---
---
---
56
H2S
12.33 1.328e-003
12.33 1.328e-003
-----
57
Hydrogen
15.86
15.86
---
58
Ethane
1.255
1.255
---
59
Propane
---
---
---
60
CO2
0.7400
0.7400
---
61
Nitrogen
22.30
22.30
---
---
---
---
---
---
---
62
Air
63
Mercury
64
MEAmine
65
Ammonia
5.275e-004 0.1477
5.275e-004 0.1477
-----
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 194 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 66 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO Separator:
PRODUCT FROM
S-1 SEPARADOR PRIMARIO Cooler:
LOGICAL CONNECTION
E-21 CONDENSADOR
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 4565 psia
2500 lbmole/hrMass:
23
5634 barrel/day
User Variables
24 25
NOTES
26 27
4.223e+004 lb/hrStd Ideal Liq Volume:
29285
28 29 30
(Last modified Mon Dec 17, 2018, 15:22)
31 32
Description
33 34 35
Material Stream: 67
36 37 38
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
39 40
Overall
Vapour Phase
41
Vapour / Phase Fraction
42
Temperature:
43
Pressure:
44
Molar Flow
45
Mass Flow
46
Std Ideal Liq Vol Flow
(barrel/day)
4942
4942
47
Molar Enthalpy
(Btu/lbmole)
-8118
-8118
48
Molar Entropy
(Btu/lbmole-F)
49
Heat Flow
50
Liq Vol Flow @Std Cond
Liquid Phase
1.0000
1.0000
0.0000
(F)
87.00
87.00
87.00
(psia)
4565
4565
4565
2156
2156
0.0000
(lbmole/hr) (lb/hr)
3.613e+004
25.54
3.613e+004
25.54
0.0000 0.0000 -2.941e+004 21.07
(Btu/hr)
-1.751e+007
-1.751e+007
0.0000
(barrel/day)
* 3.488e+006
3.488e+006
0.0000
51
PROPERTIES
52 53
Overall
Vapour Phase
Liquid Phase
54
Molecular Weight
55
Molar Density
56
Mass Density
57
Act. Volume Flow
58
Mass Enthalpy
(Btu/lb)
-484.6
-484.6
-1655
59
Mass Entropy
(Btu/lb-F)
1.525
1.525
1.186
60
Heat Capacity
9.827
9.827
18.65
61
Mass Heat Capacity
0.5866
0.5866
62
LHV Molar Basis (Std)
(Btu/lbmole)
9.722e+004
9.722e+004
1.394e+005
63
HHV Molar Basis (Std)
(Btu/lbmole)
1.112e+005
1.112e+005
1.649e+005
64
HHV Mass Basis (Std)
65
CO2 Loading
66
CO2 App ML Con
67
CO2 App WT Con
68
LHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
16.75
16.75
17.77
0.7725
0.7725
2.039
12.94
12.94
1.193e+004
1.193e+004
36.24 0.0000
1.049
6635
6635
9277
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
5803
5803
7845
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 195 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 67 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Phase Fraction [Vol. Basis]
1.000
1.000
---
13
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
14
Phase Fraction [Act. Vol. Basis]
15
Mass Exergy
16
Partial Pressure of CO2
17
Cost Based on Flow
18
Act. Gas Flow
19
Avg. Liq. Density
20 21 22
Std. Ideal Liq. Mass Density
23
Act. Liq. Flow
24
Z Factor
25
Watson K
26
User Property
27
Partial Pressure of H2S
28
Cp/(Cp - R)
29
Cp/Cv
30
Heat of Vap.
31
Kinematic Viscosity
32
Liq. Mass Density (Std. Cond)
33
Liq. Vol. Flow (Std. Cond)
34
Liquid Fraction
35
Molar Volume
36
Mass Heat of Vap.
37
Phase Fraction [Molar Basis]
38
Surface Tension
39
Thermal Conductivity
40
Viscosity
41
Cv (Semi-Ideal)
42
Mass Cv (Semi-Ideal)
43
Cv
44
Mass Cv
45
Cv (Ent. Method)
46
Mass Cv (Ent. Method)
47
Cp/Cv (Ent. Method)
48
Reid VP at 37.8 C
(psia)
49
True VP at 37.8 C
(psia)
50
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
51
Viscosity Index
1.000
1.000
0.0000
(Btu/lb)
358.1
---
---
(psia)
40.73
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
46.53
46.53
---
(lbmole/ft3)
1.865
1.865
2.120
Specific Heat
(Btu/lbmole-F)
9.827
9.827
18.65
Std. Gas Flow
(MMSCFD)
19.60
19.60
0.0000
(lb/ft3)
31.25
31.25
37.68
(USGPS)
---
---
---
---
1.007
0.3816
10.42
10.42
12.17
---
---
---
0.0000
---
---
1.253
1.253
1.119
1.673
1.673
1.907
6063
---
(psia)
(Btu/lbmole) (cSt)
9.675e-002
(lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
9.675e-002
--0.1651
4.428e-002
4.428e-002
36.15
3.488e+006
3.488e+006
0.0000
0.0000
0.0000
1.000
1.295
1.295
0.4904
361.9
---
---
1.0000
1.0000
0.0000
---
---
4.891e-002
4.891e-002
2.006e-002
2.006e-002
22.44 0.2277 9.584e-002
7.841
7.841
16.66
0.4680
0.4680
0.9377
5.874
5.874
9.781
0.3506
0.3506
0.5504
5.850
5.850
9.126
0.3492
0.3492
0.5135
1.680
1.680
2.044
---
---
511.5
---
---
3.488e+006 ---
3.488e+006 ---
52
4059 0.0000 ---
COMPOSITION
53 54
Overall Phase
55 56
COMPONENTS
57
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
58
CO
0.4558
0.0002
12.7670
0.0004
1.0936
0.0002
59
H2O
0.0276
0.0000
0.4979
0.0000
0.0342
0.0000
60
Oxygen
302.4065
0.1402
9677.0083
0.2678
582.4240
0.1179
61
Methane
179.2695
0.0831
2876.0034
0.0796
657.7556
0.1331
62
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Hydrogen
794.8027
0.3686
1602.3222
0.0443
1570.5260
0.3178
64
Ethane
43.8254
0.0203
1317.8243
0.0365
253.6954
0.0513
65
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
CO2
19.2440
0.0089
846.9214
0.0234
70.2637
0.0142
67
Nitrogen
536.4766
0.2488
15028.3201
0.4160
1276.1220
0.2582
68
Air
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 196 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 67 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
MEAmine
0.0007
0.0000
0.0400
0.0000
0.0027
0.0000
17
Ammonia
279.9713
0.1298
4767.9118
0.1320
529.9275
0.1072
18
Total
2156.4801
1.0000
36129.6164
1.0000
4941.8446
1.0000
19
Vapour Phase
20 21
COMPONENTS
22
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
23
CO
0.4558
0.0002
12.7670
0.0004
1.0936
0.0002
24
H2O
0.0276
0.0000
0.4979
0.0000
0.0342
0.0000
25
Oxygen
302.4065
0.1402
9677.0083
0.2678
582.4240
0.1179
26
Methane
179.2695
0.0831
2876.0034
0.0796
657.7556
0.1331
27
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Hydrogen
794.8027
0.3686
1602.3222
0.0443
1570.5260
0.3178
29
Ethane
43.8254
0.0203
1317.8243
0.0365
253.6954
0.0513
30
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
CO2
19.2440
0.0089
846.9214
0.0234
70.2637
0.0142
32
Nitrogen
536.4766
0.2488
15028.3201
0.4160
1276.1220
0.2582
33
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
MEAmine
0.0007
0.0000
0.0400
0.0000
0.0027
0.0000
36
Ammonia
279.9713
0.1298
4767.9118
0.1320
529.9275
0.1072
37
Total
2156.4801
1.0000
36129.6164
1.0000
4941.8446
1.0000
38
Liquid Phase
39 40
COMPONENTS
41
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
42
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
H2O
0.0000
0.0097
0.0000
0.0098
0.0000
0.0059
44
Oxygen
0.0000
0.0278
0.0000
0.0501
0.0000
0.0266
45
Methane
0.0000
0.0203
0.0000
0.0183
0.0000
0.0369
46
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Hydrogen
0.0000
0.0232
0.0000
0.0026
0.0000
0.0228
48
Ethane
0.0000
0.0162
0.0000
0.0274
0.0000
0.0465
49
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
CO2
0.0000
0.0121
0.0000
0.0299
0.0000
0.0218
51
Nitrogen
0.0000
0.0112
0.0000
0.0176
0.0000
0.0132
52
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
MEAmine
0.0000
0.0006
0.0000
0.0020
0.0000
0.0012
55
Ammonia
0.0000
0.8790
0.0000
0.8423
0.0000
0.8251
56
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
57
K VALUE
58 59
COMPONENTS
MIXED
LIGHT
HEAVY
60
CO
61
H2O
62
Oxygen
5.037
5.037
---
63
Methane
4.099
4.099
---
---
---
---
64
H2S
12.33 1.328e-003
12.33 1.328e-003
-----
65
Hydrogen
15.86
15.86
---
66
Ethane
1.255
1.255
---
67
Propane
---
---
---
68
CO2
0.7400
0.7400
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 197 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 67 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Nitrogen
13
Air
14
Mercury
15
MEAmine
16
Ammonia
LIGHT
HEAVY
22.30
22.30
---
---
---
---
---
---
---
5.275e-004
5.275e-004
0.1477
17
---
0.1477
---
UNIT OPERATIONS
18 19 20
Fluid Package:
FEED TO
PRODUCT FROM
Tee:
TEE-104 Separator:
21
LOGICAL CONNECTION
S-1 SEPARADOR PRIMARIO
UTILITIES
22 23
( No utilities reference this stream )
24
PROCESS UTILITY
25 26 27
DYNAMICS
28 29
Pressure Specification
(Inactive):
30
Flow Specification
(Inactive) Molar:
4565 psia 2156 lbmole/hrMass:
31
3.613e+004 lb/hrStd Ideal Liq Volume:
4942 barrel/day
User Variables
32 33
NOTES
34 35 36
Description
37 38 39
Material Stream: 68
40 41 42
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
43 44
Overall
45
Vapour / Phase Fraction
46
Temperature:
47
Pressure:
48
Molar Flow
49
Mass Flow
50
Std Ideal Liq Vol Flow
51
Molar Enthalpy
(Btu/lbmole)
52
Molar Entropy
(Btu/lbmole-F)
53
Heat Flow
54
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
87.00
87.00
87.00
(psia)
4565
4565
4565
343.5
0.0000
343.5
6104
0.0000
6104
692.5
0.0000
692.5
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-2.941e+004 21.07 -1.010e+007 721.7*
(barrel/day)
55
-8118 25.54 0.0000 0.0000
-2.941e+004 21.07 -1.010e+007 721.7
PROPERTIES
56 57
Overall
58
Molecular Weight
59
Molar Density
60
Mass Density
61
Act. Volume Flow
62
Vapour Phase
Liquid Phase
17.77
16.75
17.77
2.039
0.7725
2.039
36.24
12.94
36.24
(barrel/day)
719.9
0.0000
719.9
Mass Enthalpy
(Btu/lb)
-1655
-484.6
-1655
63
Mass Entropy
(Btu/lb-F)
1.186
1.525
1.186
64
Heat Capacity
18.65
9.827
18.65
65
Mass Heat Capacity
1.049
0.5866
66
LHV Molar Basis (Std)
(Btu/lbmole)
1.394e+005
9.722e+004
1.394e+005
67
HHV Molar Basis (Std)
(Btu/lbmole)
1.649e+005
1.112e+005
1.649e+005
68
HHV Mass Basis (Std)
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
9277
6635
1.049
9277
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 198 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 68 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
CO2 Loading
13
CO2 App ML Con
(lbmole/ft3)
2.459e-002
14
CO2 App WT Con
(lbmol/lb)
6.786e-004
15
LHV Mass Basis (Std)
16
Phase Fraction [Vol. Basis]
17 18 19
Mass Exergy
20
Partial Pressure of CO2
21
Cost Based on Flow
22
Act. Gas Flow
23
Avg. Liq. Density
24 25 26
Std. Ideal Liq. Mass Density
27
Act. Liq. Flow
28
Z Factor
29
Watson K
30
User Property
31
Partial Pressure of H2S
32
Cp/(Cp - R)
33
Cp/Cv
34
Heat of Vap.
35
Kinematic Viscosity
36
Liq. Mass Density (Std. Cond)
37
Liq. Vol. Flow (Std. Cond)
38
Liquid Fraction
39
Molar Volume
40
Mass Heat of Vap.
41
Phase Fraction [Molar Basis]
42
Surface Tension
43
Thermal Conductivity
44
Viscosity
45
Cv (Semi-Ideal)
46
Mass Cv (Semi-Ideal)
47
Cv
48
Mass Cv
49
Cv (Ent. Method)
50
Mass Cv (Ent. Method)
51
Cp/Cv (Ent. Method)
52
Reid VP at 37.8 C
(psia)
53
True VP at 37.8 C
(psia)
54
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
55
Viscosity Index
20.97
(Btu/lb)
Liquid Phase
---
20.97
---
2.459e-002
---
6.786e-004
7845
5803
7845
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
(Btu/lb)
182.1
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.120
1.865
2.120
Specific Heat
(Btu/lbmole-F)
18.65
9.827
18.65
Std. Gas Flow
(MMSCFD)
3.122
0.0000
3.122
(lb/ft3)
37.68
31.25
37.68
(USGPS)
0.3500
---
0.3500
(psia)
(Btu/lbmole)
---
1.007
0.3816
12.17
10.42
12.17
---
---
---
0.0000
---
---
1.119
1.253
1.119
1.907
1.673
1.907
---
---
---
(cSt)
0.1651
9.675e-002
0.1651
(lb/ft3)
36.15
4.428e-002
36.15
(barrel/day) (ft3/lbmole) (Btu/lb)
721.7
0.0000
1.000
0.0000
1.000
0.4904
1.295
0.4904
-792.7
---
---
0.0000
0.0000
1.0000
(dyne/cm)
22.44
(Btu/hr-ft-F)
0.2277
(cP)
9.584e-002
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
721.7
--4.891e-002 2.006e-002
22.44 0.2277 9.584e-002
16.66
7.841
16.66
0.9377
0.4680
0.9377
9.781
5.874
9.781
0.5504
0.3506
0.5504
9.126
5.850
9.126
0.5135
0.3492
0.5135
2.044
1.680
2.044
511.5
---
511.5
4059
---
4059
721.7
0.0000
721.7
---
---
---
56
COMPOSITION
57 58
Overall Phase
59 60
COMPONENTS
61
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
62
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
63
H2O
3.3148
0.0097
59.7169
0.0098
4.0972
0.0059
64
Oxygen
9.5615
0.0278
305.9667
0.0501
18.4150
0.0266
65
Methane
6.9652
0.0203
111.7423
0.0183
25.5560
0.0369
66
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Hydrogen
7.9795
0.0232
16.0867
0.0026
15.7675
0.0228
68
Ethane
5.5617
0.0162
167.2411
0.0274
32.1957
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0465
Page 199 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 68 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
CO2
4.1418
0.0121
182.2807
0.0299
15.1227
0.0218
17
Nitrogen
3.8311
0.0112
107.3196
0.0176
9.1130
0.0132
18
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
MEAmine
0.1976
0.0006
12.0674
0.0020
0.8125
0.0012
21
Ammonia
301.8985
0.8790
5141.3317
0.8423
571.4310
0.8251
22
Total
343.4576
1.0000
6103.9179
1.0000
692.5248
1.0000
23
Vapour Phase
24 25
COMPONENTS
26
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
27
CO
0.0000
0.0002
0.0000
0.0004
0.0000
0.0002
28
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Oxygen
0.0000
0.1402
0.0000
0.2678
0.0000
0.1179
30
Methane
0.0000
0.0831
0.0000
0.0796
0.0000
0.1331
31
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Hydrogen
0.0000
0.3686
0.0000
0.0443
0.0000
0.3178
33
Ethane
0.0000
0.0203
0.0000
0.0365
0.0000
0.0513
34
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
CO2
0.0000
0.0089
0.0000
0.0234
0.0000
0.0142
36
Nitrogen
0.0000
0.2488
0.0000
0.4160
0.0000
0.2582
37
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ammonia
0.0000
0.1298
0.0000
0.1320
0.0000
0.1072
41
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
42
Liquid Phase
43 44
COMPONENTS
45
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
46
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
47
H2O
3.3148
0.0097
59.7169
0.0098
4.0972
0.0059
48
Oxygen
9.5615
0.0278
305.9667
0.0501
18.4150
0.0266
49
Methane
6.9652
0.0203
111.7423
0.0183
25.5560
0.0369
50
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Hydrogen
7.9795
0.0232
16.0867
0.0026
15.7675
0.0228
52
Ethane
5.5617
0.0162
167.2411
0.0274
32.1957
0.0465
53
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
CO2
4.1418
0.0121
182.2807
0.0299
15.1227
0.0218
55
Nitrogen
3.8311
0.0112
107.3196
0.0176
9.1130
0.0132
56
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
MEAmine
0.1976
0.0006
12.0674
0.0020
0.8125
0.0012
59
Ammonia
301.8985
0.8790
5141.3317
0.8423
571.4310
0.8251
60
Total
343.4576
1.0000
6103.9179
1.0000
692.5248
1.0000
61
K VALUE
62 63
COMPONENTS
MIXED
LIGHT
HEAVY
64
CO
65
H2O
66
Oxygen
5.037
5.037
---
67
Methane
4.099
4.099
---
---
---
68 69
H2S
Aspen Technology Inc. Licensed to: LEGENDS
12.33 1.328e-003
Aspen HYSYS Version 8.8 (34.0.0.8909)
12.33 1.328e-003
-----
---
Page 200 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 68 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
Hydrogen
15.86
15.86
---
13
Ethane
1.255
1.255
---
14
Propane
---
---
---
15
CO2
0.7400
0.7400
---
16
Nitrogen
22.30
22.30
---
---
---
---
---
---
---
17
Air
18
Mercury
19
MEAmine
20
Ammonia
5.275e-004 0.1477
21
---
0.1477
---
UNIT OPERATIONS
22 23 24
5.275e-004
FEED TO
PRODUCT FROM
Mixer:
MIX-103 Separator:
LOGICAL CONNECTION
S-1 SEPARADOR PRIMARIO
25
UTILITIES
26 27
( No utilities reference this stream )
28
PROCESS UTILITY
29 30 31
DYNAMICS
32 33
Pressure Specification
(Inactive):
34
Flow Specification
(Inactive) Molar:
4565 psia 343.5 lbmole/hrMass:
35
6104 lb/hr Std Ideal Liq Volume:
692.5 barrel/day
User Variables
36 37
NOTES
38 39 40
Description
41 42 43
Material Stream: 69
44 45 46
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
47 48
Overall
Vapour Phase
49
Vapour / Phase Fraction
50
Temperature:
51
Pressure:
52
Molar Flow
53
Mass Flow
54
Std Ideal Liq Vol Flow
(barrel/day)
2959
2959
55
Molar Enthalpy
(Btu/lbmole)
-8118
-8118
56
Molar Entropy
(Btu/lbmole-F)
57
Heat Flow
58
Liq Vol Flow @Std Cond
Liquid Phase
1.0000
1.0000
0.0000
(F)
87.00
87.00
87.00
(psia)
4565
4565
4565
1291*
1291
0.0000
(lbmole/hr) (lb/hr)
2.163e+004
25.54
2.163e+004
25.54
0.0000 0.0000 -2.941e+004 21.07
(Btu/hr)
-1.048e+007
-1.048e+007
0.0000
(barrel/day)
* 2.089e+006
2.089e+006
0.0000
59
PROPERTIES
60 61
Overall
62
Molecular Weight
63
Molar Density
64
Mass Density
65
Act. Volume Flow
66 67 68
Heat Capacity
69
Aspen Technology Inc.
Vapour Phase
Liquid Phase
16.75
16.75
17.77
0.7725
0.7725
2.039
12.94
12.94
36.24
(barrel/day)
7146
7146
0.0000
Mass Enthalpy
(Btu/lb)
-484.6
-484.6
-1655
Mass Entropy
(Btu/lb-F)
1.525
1.525
1.186
9.827
9.827
18.65
Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 201 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 69 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Heat Capacity
13
LHV Molar Basis (Std)
(Btu/lbmole)
9.722e+004
9.722e+004
1.394e+005
14
HHV Molar Basis (Std)
(Btu/lbmole)
1.112e+005
1.112e+005
1.649e+005
15
HHV Mass Basis (Std)
16
CO2 Loading
17
CO2 App ML Con
18
CO2 App WT Con
19
LHV Mass Basis (Std)
20 21 22
Phase Fraction [Act. Vol. Basis]
23
Mass Exergy
24
Partial Pressure of CO2
25
Cost Based on Flow
26
Act. Gas Flow
27
Avg. Liq. Density
28 29 30
Std. Ideal Liq. Mass Density
31
Act. Liq. Flow
32
Z Factor
33
Watson K
34
User Property
35
Partial Pressure of H2S
36
Cp/(Cp - R)
37
Cp/Cv
38
Heat of Vap.
39
Kinematic Viscosity
40
Liq. Mass Density (Std. Cond)
41
Liq. Vol. Flow (Std. Cond)
42
Liquid Fraction
43
Molar Volume
44
Mass Heat of Vap.
45
Phase Fraction [Molar Basis]
46
Surface Tension
47
Thermal Conductivity
48
Viscosity
49
Cv (Semi-Ideal)
50
Mass Cv (Semi-Ideal)
51
Cv
52
Mass Cv
53
Cv (Ent. Method)
54
Mass Cv (Ent. Method)
55
Cp/Cv (Ent. Method)
56
Reid VP at 37.8 C
(psia)
57
True VP at 37.8 C
(psia)
58
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
59
Viscosity Index
(Btu/lb-F)
(Btu/lb)
0.5866
0.5866
1.049
6635
6635
9277
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
5803
5803
7845
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
1.000
1.000
0.0000
(Btu/lb)
358.1
---
---
(psia)
40.73
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
27.86
27.86
---
(lbmole/ft3)
1.865
1.865
2.120
Specific Heat
(Btu/lbmole-F)
9.827
9.827
18.65
Std. Gas Flow
(MMSCFD)
11.74
11.74
0.0000
(lb/ft3)
31.25
31.25
37.68
(USGPS)
---
---
---
---
1.007
0.3816
10.42
10.42
12.17
---
---
---
0.0000
---
---
1.253
1.253
1.119
1.673
1.673
1.907
6063
---
(psia)
(Btu/lbmole) (cSt)
9.675e-002
(lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
9.675e-002
--0.1651
4.428e-002
4.428e-002
36.15
2.089e+006
2.089e+006
0.0000
0.0000
0.0000
1.000
1.295
1.295
0.4904
361.9
---
---
1.0000
1.0000
0.0000
---
---
4.891e-002
4.891e-002
2.006e-002
2.006e-002
22.44 0.2277 9.584e-002
7.841
7.841
16.66
0.4680
0.4680
0.9377
5.874
5.874
9.781
0.3506
0.3506
0.5504
5.850
5.850
9.126
0.3492
0.3492
0.5135
1.680
1.680
2.044
---
---
511.5
---
---
2.089e+006 ---
2.089e+006 ---
60
4059 0.0000 ---
COMPOSITION
61 62
Overall Phase
63 64
COMPONENTS
65
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
66
CO
0.2729
0.0002
7.6449
0.0004
0.6548
0.0002
67
H2O
0.0165
0.0000
0.2981
0.0000
0.0205
0.0000
68
Oxygen
181.0814
0.1402
5794.6062
0.2678
348.7563
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.1179
Page 202 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 69 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14 15
Methane
16
H2S
17
Hydrogen
18
Ethane
19
Propane
20
CO2
21
Nitrogen
22
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
107.3469
0.0831
1722.1549
0.0796
393.8650
0.1331
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
475.9290
0.3686
959.4728
0.0443
940.4332
0.3178
26.2427
0.0203
789.1151
0.0365
151.9132
0.0513
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
11.5233
0.0089
507.1377
0.0234
42.0740
0.0142
321.2430
0.2488
8998.9793
0.4160
764.1436
0.2582
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
MEAmine
0.0004
0.0000
0.0239
0.0000
0.0016
0.0000
25
Ammonia
167.6472
0.1298
2855.0323
0.1320
317.3213
0.1072
26
Total
1291.3033
1.0000
21634.4653
1.0000
2959.1835
1.0000
27
Vapour Phase
28 29
COMPONENTS
30
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
31
CO
0.2729
0.0002
7.6449
0.0004
0.6548
0.0002
32
H2O
0.0165
0.0000
0.2981
0.0000
0.0205
0.0000
33
Oxygen
181.0814
0.1402
5794.6062
0.2678
348.7563
0.1179
34
Methane
107.3469
0.0831
1722.1549
0.0796
393.8650
0.1331
35
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Hydrogen
475.9290
0.3686
959.4728
0.0443
940.4332
0.3178
37
Ethane
26.2427
0.0203
789.1151
0.0365
151.9132
0.0513
38
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
CO2
11.5233
0.0089
507.1377
0.0234
42.0740
0.0142
40
Nitrogen
321.2430
0.2488
8998.9793
0.4160
764.1436
0.2582
41
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
MEAmine
0.0004
0.0000
0.0239
0.0000
0.0016
0.0000
44
Ammonia
167.6472
0.1298
2855.0323
0.1320
317.3213
0.1072
45
Total
1291.3033
1.0000
21634.4653
1.0000
2959.1835
1.0000
46
Liquid Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
50
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
H2O
0.0000
0.0097
0.0000
0.0098
0.0000
0.0059
52
Oxygen
0.0000
0.0278
0.0000
0.0501
0.0000
0.0266
53
Methane
0.0000
0.0203
0.0000
0.0183
0.0000
0.0369
54
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Hydrogen
0.0000
0.0232
0.0000
0.0026
0.0000
0.0228
56
Ethane
0.0000
0.0162
0.0000
0.0274
0.0000
0.0465
57
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
CO2
0.0000
0.0121
0.0000
0.0299
0.0000
0.0218
59
Nitrogen
0.0000
0.0112
0.0000
0.0176
0.0000
0.0132
60
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
MEAmine
0.0000
0.0006
0.0000
0.0020
0.0000
0.0012
63
Ammonia
0.0000
0.8790
0.0000
0.8423
0.0000
0.8251
64
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
65
K VALUE
66 67
COMPONENTS
68 69
MIXED CO
Aspen Technology Inc. Licensed to: LEGENDS
LIGHT 12.33
Aspen HYSYS Version 8.8 (34.0.0.8909)
HEAVY 12.33
---
Page 203 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 69 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
H2O
13
Oxygen
5.037
5.037
---
14
Methane
4.099
4.099
---
---
---
---
15
1.328e-003
H2S
1.328e-003
---
16
Hydrogen
15.86
15.86
---
17
Ethane
1.255
1.255
---
18
Propane
---
---
---
19
CO2
0.7400
0.7400
---
20
Nitrogen
22.30
22.30
---
---
---
---
---
---
---
21
Air
22
Mercury
23
MEAmine
24
Ammonia
5.275e-004 0.1477
25
---
0.1477
---
UNIT OPERATIONS
26 27 28
5.275e-004
FEED TO
PRODUCT FROM
Compressor:
K-103
Tee:
LOGICAL CONNECTION TEE-104
29
UTILITIES
30 31
( No utilities reference this stream )
32
PROCESS UTILITY
33 34 35
DYNAMICS
36 37
Pressure Specification
(Inactive):
38
Flow Specification
(Active)
4565 psia * Mass: 1291 lbmole/hr
Molar:
39
2.163e+004 lb/hrStd Ideal Liq Volume:
2959 barrel/day
User Variables
40 41
NOTES
42 43 44
Description
45 46 47
Material Stream: 70
48 49 50
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
51 52
Overall
Vapour Phase
53
Vapour / Phase Fraction
54
Temperature:
55
Pressure:
56
Molar Flow
57
Mass Flow
58
Std Ideal Liq Vol Flow
(barrel/day)
2959
2959
59
Molar Enthalpy
(Btu/lbmole)
-8038
-8038
60
Molar Entropy
(Btu/lbmole-F)
61
Heat Flow
62
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
96.88
96.88
(psia)
4820*
4820
(lbmole/hr) (lb/hr)
1291 2.163e+004
25.58
1291 2.163e+004
25.58
(Btu/hr)
-1.038e+007
-1.038e+007
(barrel/day)
* 2.089e+006
2.089e+006
63
PROPERTIES
64 65
Overall
66
Molecular Weight
67
Molar Density
68
Mass Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
Vapour Phase 16.75
16.75
0.7898
0.7898
13.23
13.23
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 204 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 70 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Act. Volume Flow
13
Mass Enthalpy
14
Mass Entropy
15
Heat Capacity
16
Mass Heat Capacity
17
LHV Molar Basis (Std)
(Btu/lbmole)
9.722e+004
9.722e+004
18
HHV Molar Basis (Std)
(Btu/lbmole)
1.112e+005
1.112e+005
19
HHV Mass Basis (Std)
20
CO2 Loading
21
CO2 App ML Con
22
CO2 App WT Con
23
LHV Mass Basis (Std)
24 25
(barrel/day)
6989
6989
(Btu/lb)
-479.8
-479.8
(Btu/lb-F)
1.527
1.527
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
9.786
9.786
0.5841
0.5841
6635
6635
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
5803
5803
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
26
Phase Fraction [Act. Vol. Basis]
1.000
1.000
27
Mass Exergy
(Btu/lb)
361.7
---
28
Partial Pressure of CO2
(psia)
43.01
29
Cost Based on Flow
30
Act. Gas Flow
31
Avg. Liq. Density
32
(Cost/s)
1.050e+004
--1.050e+004
(ACFM)
27.25
27.25
(lbmole/ft3)
1.865
1.865
Specific Heat
(Btu/lbmole-F)
9.786
9.786
33
Std. Gas Flow
(MMSCFD)
11.74
11.74
34
Std. Ideal Liq. Mass Density
(lb/ft3)
31.25
31.25
35
Act. Liq. Flow
(USGPS)
---
---
36
Z Factor
1.022
1.022
37
Watson K
10.42
10.42
38
User Property
---
---
39
Partial Pressure of H2S
40
Cp/(Cp - R)
41
Cp/Cv
42
Heat of Vap.
43
Kinematic Viscosity
44
Liq. Mass Density (Std. Cond)
45
Liq. Vol. Flow (Std. Cond)
46
Liquid Fraction
47
Molar Volume
48
Mass Heat of Vap.
49
Phase Fraction [Molar Basis]
50
Surface Tension
51
Thermal Conductivity
52
Viscosity
53
Cv (Semi-Ideal)
54
Mass Cv (Semi-Ideal)
55
Cv
56
Mass Cv
57
Cv (Ent. Method)
58
Mass Cv (Ent. Method)
59
Cp/Cv (Ent. Method)
60
Reid VP at 37.8 C
(psia)
61
True VP at 37.8 C
(psia)
---
62
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
63
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.255
1.255
1.660
1.660
6030 9.662e-002
--9.662e-002
4.428e-002
4.428e-002
2.089e+006
2.089e+006
0.0000
0.0000
(ft3/lbmole)
1.266
1.266
(Btu/lb)
359.9
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
---
4.995e-002
4.995e-002
2.048e-002
2.048e-002
7.800
7.800
0.4656
0.4656
5.894
5.894
0.3518
0.3518
5.846
5.846
0.3489
0.3489
1.674
1.674
---
-----
2.089e+006 ---
2.089e+006 ---
64 65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 205 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 70 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
CO
0.2729
0.0002
7.6449
0.0004
0.6548
0.0002
16
H2O
0.0165
0.0000
0.2981
0.0000
0.0205
0.0000
17
Oxygen
181.0814
0.1402
5794.6062
0.2678
348.7563
0.1179
18
Methane
107.3469
0.0831
1722.1549
0.0796
393.8650
0.1331
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
475.9290
0.3686
959.4728
0.0443
940.4332
0.3178
21
Ethane
26.2427
0.0203
789.1151
0.0365
151.9132
0.0513
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
11.5233
0.0089
507.1377
0.0234
42.0740
0.0142
24
Nitrogen
321.2430
0.2488
8998.9793
0.4160
764.1436
0.2582
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0004
0.0000
0.0239
0.0000
0.0016
0.0000
28
Ammonia
167.6472
0.1298
2855.0323
0.1320
317.3213
0.1072
29
Total
1291.3033
1.0000
21634.4653
1.0000
2959.1835
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.2729
0.0002
7.6449
0.0004
0.6548
0.0002
35
H2O
0.0165
0.0000
0.2981
0.0000
0.0205
0.0000
36
Oxygen
181.0814
0.1402
5794.6062
0.2678
348.7563
0.1179
37
Methane
107.3469
0.0831
1722.1549
0.0796
393.8650
0.1331
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
475.9290
0.3686
959.4728
0.0443
940.4332
0.3178
40
Ethane
26.2427
0.0203
789.1151
0.0365
151.9132
0.0513
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
11.5233
0.0089
507.1377
0.0234
42.0740
0.0142
43
Nitrogen
321.2430
0.2488
8998.9793
0.4160
764.1436
0.2582
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0004
0.0000
0.0239
0.0000
0.0016
0.0000
47
Ammonia
167.6472
0.1298
2855.0323
0.1320
317.3213
0.1072
48
Total
1291.3033
1.0000
21634.4653
1.0000
2959.1835
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
---
---
---
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 206 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 70 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Recycle:
RCY-2
Compressor:
13
LOGICAL CONNECTION K-103
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 4820 psia
1291 lbmole/hrMass:
23
2959 barrel/day
User Variables
24 25
NOTES
26 27
2.163e+004 lb/hrStd Ideal Liq Volume:
29285
28 29 30
(Last modified Mon Dec 17, 2018, 15:08)
31 32
Description
33 34 35
Material Stream: 71
36 37 38
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
39 40
Overall
Vapour Phase
41
Vapour / Phase Fraction
42
Temperature:
43
Pressure:
44
Molar Flow
45
Mass Flow
46
Std Ideal Liq Vol Flow
(barrel/day)
2958
2958
47
Molar Enthalpy
(Btu/lbmole)
-8043
-8043
48
Molar Entropy
(Btu/lbmole-F)
49
Heat Flow
50
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
96.86*
96.86
(psia)
4820*
4820
1291*
(lbmole/hr) (lb/hr)
2.164e+004
25.58
1291 2.164e+004
25.58
(Btu/hr)
-1.039e+007
-1.039e+007
(barrel/day)
* 2.089e+006
2.089e+006
51
PROPERTIES
52 53
Overall
Vapour Phase
54
Molecular Weight
55
Molar Density
56
Mass Density
57
Act. Volume Flow
58
Mass Enthalpy
59
Mass Entropy
60
Heat Capacity
61
Mass Heat Capacity
62
LHV Molar Basis (Std)
(Btu/lbmole)
9.718e+004
9.718e+004
63
HHV Molar Basis (Std)
(Btu/lbmole)
1.111e+005
1.111e+005
64
HHV Mass Basis (Std)
65
CO2 Loading
66
CO2 App ML Con
67
CO2 App WT Con
68
LHV Mass Basis (Std)
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
16.76
16.76
0.7902
0.7902
13.25
13.25
(barrel/day)
6985
6985
(Btu/lb)
-479.8
-479.8
(Btu/lb-F)
1.526
1.526
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
9.794
9.794
0.5843
0.5843
6629
6629
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
5797
5797
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 207 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 71 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Phase Fraction [Vol. Basis]
1.000
1.000
13
Phase Fraction [Mass Basis]
1.000
1.000
14
Phase Fraction [Act. Vol. Basis]
1.000
1.000
15
Mass Exergy
(Btu/lb)
361.5
---
16
Partial Pressure of CO2
(psia)
42.76
---
17
Cost Based on Flow
(Cost/s)
0.0000
0.0000
18
Act. Gas Flow
19
Avg. Liq. Density
20
(ACFM)
27.24
27.24
(lbmole/ft3)
1.866
1.866
Specific Heat
(Btu/lbmole-F)
9.794
9.794
21
Std. Gas Flow
(MMSCFD)
11.74
11.74
22
Std. Ideal Liq. Mass Density
(lb/ft3)
31.28
31.28
23
Act. Liq. Flow
(USGPS)
---
---
24
Z Factor
1.021
1.021
25
Watson K
10.41
10.41
26
User Property
---
---
27
Partial Pressure of H2S
28
Cp/(Cp - R)
29
Cp/Cv
30
Heat of Vap.
31
Kinematic Viscosity
32
Liq. Mass Density (Std. Cond)
33
Liq. Vol. Flow (Std. Cond)
34
Liquid Fraction
35
Molar Volume
36
Mass Heat of Vap.
37
Phase Fraction [Molar Basis]
38
Surface Tension
39
Thermal Conductivity
40
Viscosity
41
Cv (Semi-Ideal)
42
Mass Cv (Semi-Ideal)
43
Cv
44
Mass Cv
45
Cv (Ent. Method)
46
Mass Cv (Ent. Method)
47
Cp/Cv (Ent. Method)
48
Reid VP at 37.8 C
(psia)
49
True VP at 37.8 C
(psia)
---
50
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
51
Viscosity Index
(psia)
(Btu/lbmole) (cSt)
0.0000
---
1.254
1.254
1.661
1.661
6041 9.659e-002
(lb/ft3) (barrel/day)
--9.659e-002
4.430e-002
4.430e-002
2.089e+006
2.089e+006
0.0000
0.0000
(ft3/lbmole)
1.266
1.266
(Btu/lb)
360.4
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
---
4.994e-002
4.994e-002
2.049e-002
2.049e-002
7.808
7.808
0.4658
0.4658
5.898
5.898
0.3519
0.3519
5.872
5.872
0.3503
0.3503
1.668
1.668
---
-----
2.089e+006 ---
2.089e+006 ---
52
COMPOSITION
53 54
Overall Phase
55 56
COMPONENTS
57
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
58
CO
* 0.2722
* 0.0002
* 7.6247
* 0.0004
* 0.6531
* 0.0002
59
H2O
* 0.0177
* 0.0000
* 0.3184
* 0.0000
* 0.0218
* 0.0000
60
Oxygen
* 181.3331
* 0.1404
* 5802.6593
* 0.2681
* 349.2410
* 0.1181
61
Methane
* 107.5045
* 0.0833
* 1724.6836
* 0.0797
* 394.4433
* 0.1333
62
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
63
Hydrogen
* 475.0657
* 0.3679
* 957.7325
* 0.0442
* 938.7275
* 0.3173
64
Ethane
* 26.0279
* 0.0202
* 782.6557
* 0.0362
* 150.6697
* 0.0509
65
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
66
CO2
* 11.4565
* 0.0089
* 504.1985
* 0.0233
* 41.8302
* 0.0141
67
Nitrogen
* 321.1098
* 0.2487
* 8995.2496
* 0.4156
* 763.8269
* 0.2582
68
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
* 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
* 0.0000
Page 208 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 71 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
16
MEAmine
* 0.0005
* 0.0000
* 0.0277
* 0.0000
* 0.0019
* 0.0000
17
Ammonia
* 168.5154
* 0.1305
* 2869.8180
* 0.1326
* 318.9647
* 0.1078
18
Total
1291.3033
1.0000
21644.9682
1.0000
2958.3801
1.0000
19
Vapour Phase
20 21
COMPONENTS
MOLAR FLOW (lbmole/hr)
22
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
23
CO
0.2722
0.0002
7.6247
0.0004
0.6531
0.0002
24
H2O
0.0177
0.0000
0.3184
0.0000
0.0218
0.0000
25
Oxygen
181.3331
0.1404
5802.6593
0.2681
349.2410
0.1181
26
Methane
107.5045
0.0833
1724.6836
0.0797
394.4433
0.1333
27
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Hydrogen
475.0657
0.3679
957.7325
0.0442
938.7275
0.3173
29
Ethane
26.0279
0.0202
782.6557
0.0362
150.6697
0.0509
30
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
CO2
11.4565
0.0089
504.1985
0.0233
41.8302
0.0141
32
Nitrogen
321.1098
0.2487
8995.2496
0.4156
763.8269
0.2582
33
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
MEAmine
0.0005
0.0000
0.0277
0.0000
0.0019
0.0000
36
Ammonia
168.5154
0.1305
2869.8180
0.1326
318.9647
0.1078
37
Total
1291.3033
1.0000
21644.9682
1.0000
2958.3801
1.0000
38
K VALUE
39 40
COMPONENTS
MIXED
LIGHT
HEAVY
41
CO
---
---
---
42
H2O
---
---
---
43
Oxygen
---
---
---
44
Methane
---
---
---
---
---
---
45
H2S
46
Hydrogen
---
---
---
47
Ethane
---
---
---
48
Propane
---
---
---
49
CO2
---
---
---
50
Nitrogen
---
---
---
---
---
---
51
Air
52
Mercury
---
---
---
53
MEAmine
---
---
---
54
Ammonia
---
---
---
55
UNIT OPERATIONS
56 57 58
FEED TO
PRODUCT FROM
Mixer:
MIX-102 Recycle:
59
LOGICAL CONNECTION RCY-2
UTILITIES
60 61
( No utilities reference this stream )
62
PROCESS UTILITY
63 64 65
DYNAMICS
66 67
Pressure Specification
(Inactive):
68
Flow Specification
(Inactive) Molar:
69
Aspen Technology Inc. Licensed to: LEGENDS
* 4820 psia * Mass: 1291 lbmole/hr
2.164e+004 lb/hrStd Ideal Liq Volume:
Aspen HYSYS Version 8.8 (34.0.0.8909)
2958 barrel/day
Page 209 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 71 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
User Variables
10 11
NOTES
12 13 14
Description
15 16 17
Material Stream: 72
18 19 20
CONDITIONS
21 22
Overall
23
Vapour / Phase Fraction
24
Temperature:
25
Pressure:
26
Molar Flow
27
Mass Flow
28
Std Ideal Liq Vol Flow
29
Molar Enthalpy
(Btu/lbmole)
30
Molar Entropy
(Btu/lbmole-F)
31
Heat Flow
32
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
99.00*
99.00
(psia)
4820*
4820
168.5
168.5
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
2870
2870
319.0
319.0
-2.821e+004 19.63 -4.753e+006 320.9*
(barrel/day)
33
-2.821e+004 19.63 -4.753e+006 320.9
PROPERTIES
34 35
Overall
36
Molecular Weight
37
Molar Density
38
Mass Density
39
Act. Volume Flow
40
Liquid Phase 17.03
17.03
2.201
2.201
37.48
37.48
(barrel/day)
327.3
327.3
Mass Enthalpy
(Btu/lb)
-1656
-1656
41
Mass Entropy
(Btu/lb-F)
1.152
1.152
42
Heat Capacity
18.93
18.93
43
Mass Heat Capacity
44
LHV Molar Basis (Std)
(Btu/lbmole)
1.362e+005
1.362e+005
45
HHV Molar Basis (Std)
(Btu/lbmole)
1.627e+005
1.627e+005
46
HHV Mass Basis (Std)
47
CO2 Loading
48
CO2 App ML Con
49
CO2 App WT Con
50
LHV Mass Basis (Std)
51
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.112
9551
1.112
9551
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
7998
7998
Phase Fraction [Vol. Basis]
0.0000
1.000
52
Phase Fraction [Mass Basis]
0.0000
1.000
53
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
54
Mass Exergy
(Btu/lb)
163.9
---
55
Partial Pressure of CO2
(psia)
0.0000
---
56
Cost Based on Flow
(Cost/s)
0.0000
0.0000
57
Act. Gas Flow
58
Avg. Liq. Density
59 60 61
Std. Ideal Liq. Mass Density
62
Act. Liq. Flow
63
Z Factor
64
Watson K
65
User Property
66
Partial Pressure of H2S
67
(ACFM)
---
---
(lbmole/ft3)
2.258
2.258
Specific Heat
(Btu/lbmole-F)
18.93
18.93
Std. Gas Flow
(MMSCFD)
1.532
1.532
(lb/ft3)
38.46
38.46
(USGPS)
0.1591
0.1591
0.3653
0.3653
12.24
12.24
---
---
0.0000
---
Cp/(Cp - R)
1.117
1.117
68
Cp/Cv
2.169
2.169
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 210 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 72 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Heat of Vap.
13
Kinematic Viscosity
14
Liq. Mass Density (Std. Cond)
15
Liq. Vol. Flow (Std. Cond)
16
Liquid Fraction
17
Molar Volume
18
Mass Heat of Vap.
19
Phase Fraction [Molar Basis]
20
Surface Tension
21
Thermal Conductivity
22
Viscosity
23
Cv (Semi-Ideal)
24
Mass Cv (Semi-Ideal)
25
Cv
26
Mass Cv
27
Cv (Ent. Method)
28
Mass Cv (Ent. Method)
29
Cp/Cv (Ent. Method)
30
Reid VP at 37.8 C
31
True VP at 37.8 C
32
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
33
Viscosity Index
(Btu/lbmole)
Liquid Phase ---
---
(cSt)
0.1866
0.1866
(lb/ft3)
38.22
38.22
320.9
320.9
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4544
0.4544
-827.2
---
0.0000
1.0000
(dyne/cm)
23.13
23.13
(Btu/hr-ft-F)
0.2605
0.2605
0.1120
0.1120
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.94
16.94
0.9950
0.9950
8.726
8.726
0.5124
0.5124
---
---
---
---
---
---
(psia)
210.5
210.5
(psia)
210.5
210.5
320.9
320.9
---
---
34
COMPOSITION
35 36
Overall Phase
37 38
COMPONENTS
39
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
40
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
54
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
55
Liquid Phase
56 57
COMPONENTS
58
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
59
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 211 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 72 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
19
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
20
K VALUE
21 22
COMPONENTS
MIXED
LIGHT
HEAVY
23
CO
---
---
---
24
H2O
---
---
---
25
Oxygen
---
---
---
26
Methane
---
---
---
---
---
---
27
H2S
28
Hydrogen
---
---
---
29
Ethane
---
---
---
30
Propane
---
---
---
31
CO2
---
---
---
32
Nitrogen
---
---
---
---
---
---
33
Air
34
Mercury
---
---
---
35
MEAmine
---
---
---
36
Ammonia
0.0000
0.0000
---
37
UNIT OPERATIONS
38 39 40
FEED TO
PRODUCT FROM
Component Splitter:
X-101
Cooler:
LOGICAL CONNECTION E-106
41
UTILITIES
42 43
( No utilities reference this stream )
44
PROCESS UTILITY
45 46 47
DYNAMICS
48 49
Pressure Specification
(Active):
50
Flow Specification
(Inactive) Molar:
* 4820 psia
168.5 lbmole/hrMass:
51
2870 lb/hr Std Ideal Liq Volume:
319.0 barrel/day
User Variables
52 53
NOTES
54 55 56
Description
57 58 59
Material Stream: 73
60 61 62
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
63 64
Overall
65
Vapour / Phase Fraction
66
Temperature:
67
Pressure:
68
Molar Flow
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Liquid Phase 0.0000
1.0000
(F)
99.00
99.00
(psia)
4820*
4820
168.5
168.5
(lbmole/hr)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 212 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 73 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Mass Flow
13
Std Ideal Liq Vol Flow
14
Molar Enthalpy
(Btu/lbmole)
15
Molar Entropy
(Btu/lbmole-F)
16
Heat Flow
17
Liq Vol Flow @Std Cond
(lb/hr) (barrel/day)
(Btu/hr)
Liquid Phase 2870
2870
319.0
319.0
-2.821e+004 19.63 -4.753e+006 320.9*
(barrel/day)
18
-2.821e+004 19.63 -4.753e+006 320.9
PROPERTIES
19 20
Overall
21
Molecular Weight
22
Molar Density
23
Mass Density
24
Act. Volume Flow
25
Liquid Phase 17.03
17.03
2.201
2.201
37.48
37.48
(barrel/day)
327.3
327.3
Mass Enthalpy
(Btu/lb)
-1656
-1656
26
Mass Entropy
(Btu/lb-F)
1.152
1.152
27
Heat Capacity
18.93
18.93
28
Mass Heat Capacity
29
LHV Molar Basis (Std)
(Btu/lbmole)
1.362e+005
1.362e+005
30
HHV Molar Basis (Std)
(Btu/lbmole)
1.627e+005
1.627e+005
31
HHV Mass Basis (Std)
32
CO2 Loading
33
CO2 App ML Con
34
CO2 App WT Con
35
LHV Mass Basis (Std)
36
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.112
9551
1.112
9551
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
7998
7998
Phase Fraction [Vol. Basis]
0.0000
1.000
37
Phase Fraction [Mass Basis]
0.0000
1.000
38
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
39
Mass Exergy
(Btu/lb)
163.9
---
40
Partial Pressure of CO2
(psia)
0.0000
---
41
Cost Based on Flow
(Cost/s)
0.0000
0.0000
42
Act. Gas Flow
43
Avg. Liq. Density
44 45 46
Std. Ideal Liq. Mass Density
47
Act. Liq. Flow
48
Z Factor
49
Watson K
50
User Property
51
Partial Pressure of H2S
52
Cp/(Cp - R)
53
Cp/Cv
54
Heat of Vap.
55
Kinematic Viscosity
56
Liq. Mass Density (Std. Cond)
57
Liq. Vol. Flow (Std. Cond)
58
Liquid Fraction
59
Molar Volume
60
Mass Heat of Vap.
61
Phase Fraction [Molar Basis]
62
Surface Tension
63
Thermal Conductivity
64
Viscosity
65
Cv (Semi-Ideal)
66
Mass Cv (Semi-Ideal)
67
Cv
68
Mass Cv
69
Fluid Package:
(ACFM)
---
---
(lbmole/ft3)
2.258
2.258
Specific Heat
(Btu/lbmole-F)
18.93
18.93
Std. Gas Flow
(MMSCFD)
1.532
1.532
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
38.46
38.46
(USGPS)
0.1591
0.1591
0.3653
0.3653
12.24
12.24
---
---
(psia)
(Btu/lbmole)
0.0000
---
1.117
1.117
2.169
2.169
---
---
(cSt)
0.1866
0.1866
(lb/ft3)
38.22
38.22
320.9
320.9
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4544
0.4544
-827.2
---
0.0000
1.0000
(dyne/cm)
23.13
23.13
(Btu/hr-ft-F)
0.2605
0.2605
0.1120
0.1120
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.94
16.94
0.9950
0.9950
8.726
8.726
0.5124
0.5124
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 213 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 73 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Ent. Method)
13
Mass Cv (Ent. Method)
14
Cp/Cv (Ent. Method)
15
Reid VP at 37.8 C
16
True VP at 37.8 C
17
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
18
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F)
Liquid Phase ---
---
---
---
---
---
(psia)
210.5
210.5
(psia)
210.5
210.5
320.9
320.9
---
---
19
COMPOSITION
20 21
Overall Phase
22 23
COMPONENTS
24
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
25
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
39
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
40
Liquid Phase
41 42
COMPONENTS
43
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
44
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Ammonia
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
58
Total
168.5154
1.0000
2869.8180
1.0000
318.9647
1.0000
59
K VALUE
60 61
COMPONENTS
MIXED
LIGHT
HEAVY
62
CO
---
---
---
63
H2O
---
---
---
64
Oxygen
---
---
---
65
Methane
---
---
---
---
---
-----
66
H2S
67
Hydrogen
---
---
68
Ethane
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 214 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 73 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
Propane
---
---
---
13
CO2
---
---
---
14
Nitrogen
---
---
---
---
---
---
15
Air
16
Mercury
---
---
---
17
MEAmine
---
---
---
18
Ammonia
0.0000
0.0000
---
19
UNIT OPERATIONS
20 21 22
FEED TO
PRODUCT FROM
Mixer:
MIX-103 Component Splitter:
23
LOGICAL CONNECTION X-101
UTILITIES
24 25
( No utilities reference this stream )
26
PROCESS UTILITY
27 28 29
DYNAMICS
30 31
Pressure Specification
(Active):
32
Flow Specification
(Inactive) Molar:
* 4820 psia
168.5 lbmole/hrMass:
33
2870 lb/hr Std Ideal Liq Volume:
319.0 barrel/day
User Variables
34 35
NOTES
36 37 38
Description
39 40 41
Material Stream: 74
42 43 44
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
45 46
Overall
47
Vapour / Phase Fraction
48
Temperature:
49
Pressure:
50
Molar Flow
51
Mass Flow
52
Std Ideal Liq Vol Flow
(barrel/day)
53
Molar Enthalpy
(Btu/lbmole)
54
Molar Entropy
(Btu/lbmole-F)
55
Heat Flow
56
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
99.00*
99.00
(psia)
4820*
4820
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
0.0000 -2.821e+004
0.0000 -2.821e+004
19.63
19.63
(Btu/hr)
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
57
PROPERTIES
58 59
Overall
60
Molecular Weight
61
Molar Density
62
Mass Density
63
Act. Volume Flow
64 65 66
Heat Capacity
67
Mass Heat Capacity
68
LHV Molar Basis (Std)
69
Fluid Package:
(lbmole/ft3)
17.03
2.201
2.201
37.48
37.48
(barrel/day)
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-1656
-1656
Mass Entropy
(Btu/lb-F)
1.152
1.152
18.93
18.93
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
Liquid Phase 17.03
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole)
1.112 1.362e+005
1.112 1.362e+005
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 215 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 74 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
HHV Molar Basis (Std)
13
HHV Mass Basis (Std)
14
CO2 Loading
15
CO2 App ML Con
16
CO2 App WT Con
17
LHV Mass Basis (Std)
18 19
(Btu/lbmole) (Btu/lb)
Liquid Phase
1.627e+005
1.627e+005
9551
9551
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
7998
7998
Phase Fraction [Vol. Basis]
0.0000
1.000
Phase Fraction [Mass Basis]
0.0000
1.000
20
Phase Fraction [Act. Vol. Basis]
0.0000
---
21
Mass Exergy
(Btu/lb)
163.9
---
22
Partial Pressure of CO2
(psia)
0.0000
---
23
Cost Based on Flow
(Cost/s)
0.0000
0.0000
24
Act. Gas Flow
---
25
Avg. Liq. Density
26
(ACFM)
---
(lbmole/ft3)
---
---
Specific Heat
(Btu/lbmole-F)
18.93
18.93
27
Std. Gas Flow
(MMSCFD)
0.0000
0.0000
28
Std. Ideal Liq. Mass Density
29
Act. Liq. Flow
30
Z Factor
31
Watson K
32
User Property
33
Partial Pressure of H2S
34
Cp/(Cp - R)
35
Cp/Cv
36
Heat of Vap.
37
Kinematic Viscosity
38
Liq. Mass Density (Std. Cond)
39
Liq. Vol. Flow (Std. Cond)
40
Liquid Fraction
41
Molar Volume
42
Mass Heat of Vap.
43
Phase Fraction [Molar Basis]
44
Surface Tension
45
Thermal Conductivity
46
Viscosity
47
Cv (Semi-Ideal)
48
Mass Cv (Semi-Ideal)
49
Cv
50
Mass Cv
51
Cv (Ent. Method)
52
Mass Cv (Ent. Method)
53
Cp/Cv (Ent. Method)
54
Reid VP at 37.8 C
(psia)
55
True VP at 37.8 C
(psia)
56
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
57
Viscosity Index
(lb/ft3)
38.46
38.46
(USGPS)
0.0000
0.0000
0.3653
0.3653
12.24
12.24
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
0.0000
---
1.117
1.117
2.169
2.169
---
---
0.1866
0.1866
38.22
38.22
(barrel/day)
0.0000
0.0000
1.000
1.000
(ft3/lbmole)
0.4544
0.4544
(Btu/lb)
-827.2
---
0.0000
1.0000
(dyne/cm)
23.13
23.13
(Btu/hr-ft-F)
0.2605
0.2605
0.1120
0.1120
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.94
16.94
0.9950
0.9950
8.726
8.726
0.5124
0.5124
---
---
---
---
---
---
210.5
210.5
210.5
210.5
0.0000
0.0000
---
---
58
COMPOSITION
59 60
Overall Phase
61 62
COMPONENTS
63
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
64
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 216 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 74 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Ammonia
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
24
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
25
Liquid Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
43
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
44
K VALUE
45 46
COMPONENTS
MIXED
LIGHT
HEAVY
47
CO
---
---
---
48
H2O
---
---
---
49
Oxygen
---
---
---
50
Methane
---
---
---
---
---
---
51
H2S
52
Hydrogen
---
---
---
53
Ethane
---
---
---
54
Propane
---
---
---
55
CO2
---
---
---
56
Nitrogen
---
---
---
---
---
---
57
Air
58
Mercury
---
---
---
59
MEAmine
---
---
---
60
Ammonia
0.0000
0.0000
---
61
UNIT OPERATIONS
62 63
FEED TO
64
PRODUCT FROM Component Splitter:
65
LOGICAL CONNECTION X-101
UTILITIES
66 67
( No utilities reference this stream )
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 217 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 74 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROCESS UTILITY
10 11 12
DYNAMICS
13 14
Pressure Specification
(Active):
15
Flow Specification
(Inactive) Molar:
* 4820 psia
0.0000 lbmole/hrMass:
16
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
17 18
NOTES
19 20 21
Description
22 23 24
Material Stream: 75
25 26 27
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
28 29
Overall
30
Vapour / Phase Fraction
31
Temperature:
32
Pressure:
33
Molar Flow
34
Mass Flow
35
Std Ideal Liq Vol Flow
(barrel/day)
36
Molar Enthalpy
(Btu/lbmole)
37
Molar Entropy
(Btu/lbmole-F)
38
Heat Flow
39
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
90.98
90.98
(psia)
4565
4565
512.0
512.0
8974
8974
(lbmole/hr) (lb/hr)
(Btu/hr)
1011 -2.901e+004 20.67 -1.485e+007 1040*
(barrel/day)
40
1011 -2.901e+004 20.67 -1.485e+007 1040
PROPERTIES
41 42
Overall
Liquid Phase
43
Molecular Weight
44
Molar Density
45
Mass Density
46
Act. Volume Flow
47
Mass Enthalpy
48
Mass Entropy
49
Heat Capacity
50
Mass Heat Capacity
51
LHV Molar Basis (Std)
(Btu/lbmole)
1.384e+005
1.384e+005
52
HHV Molar Basis (Std)
(Btu/lbmole)
1.641e+005
1.641e+005
53
HHV Mass Basis (Std)
54
CO2 Loading
55
CO2 App ML Con
(lbmole/ft3)
1.691e-002
1.691e-002
56
CO2 App WT Con
(lbmol/lb)
4.616e-004
4.616e-004
57
LHV Mass Basis (Std)
58
(lbmole/ft3) (lb/ft3)
17.53
17.53
2.090
2.090
36.64
36.64
(barrel/day)
1047
1047
(Btu/lb)
-1655
-1655
(Btu/lb-F)
1.179
1.179
18.77
18.77
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.071
1.071
9364
9364
20.97
20.97
7894
7894
Phase Fraction [Vol. Basis]
0.0000
1.000
59
Phase Fraction [Mass Basis]
0.0000
1.000
60
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
61
Mass Exergy
(Btu/lb)
176.0
---
62
Partial Pressure of CO2
(psia)
0.0000
---
63
Cost Based on Flow
(Cost/s)
0.0000
0.0000
64
Act. Gas Flow
65
Avg. Liq. Density
66 67 68
Std. Ideal Liq. Mass Density
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
2.164
2.164
Specific Heat
(Btu/lbmole-F)
18.77
18.77
Std. Gas Flow
(MMSCFD)
4.654
4.654
37.92
37.92
Licensed to: LEGENDS
(lb/ft3)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 218 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 75 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Act. Liq. Flow
13
Z Factor
14
Watson K
15
User Property
16
Partial Pressure of H2S
17
Cp/(Cp - R)
18
Cp/Cv
19
Heat of Vap.
20
Kinematic Viscosity
21
Liq. Mass Density (Std. Cond)
22
Liq. Vol. Flow (Std. Cond)
23
Liquid Fraction
24
Molar Volume
25
Mass Heat of Vap.
26
Phase Fraction [Molar Basis]
27
Surface Tension
28
Thermal Conductivity
29
Viscosity
30
Cv (Semi-Ideal)
31
Mass Cv (Semi-Ideal)
32
Cv
33
Mass Cv
34
Cv (Ent. Method)
35
Mass Cv (Ent. Method)
36
Cp/Cv (Ent. Method)
37
Reid VP at 37.8 C
(psia)
38
True VP at 37.8 C
(psia)
39
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
40
Viscosity Index
(USGPS)
(psia)
(Btu/lbmole)
Liquid Phase 0.5089
0.5089
0.3695
0.3695
12.20
12.20
---
---
0.0000
---
1.118
1.118
2.009
2.009
---
---
(cSt)
0.1720
0.1720
(lb/ft3)
36.90
36.90
(barrel/day)
1040
1040
1.000
1.000
(ft3/lbmole)
0.4784
0.4784
(Btu/lb)
-803.7
---
0.0000
1.0000
(dyne/cm)
22.70
22.70
(Btu/hr-ft-F)
0.2383
0.2383
0.1010
0.1010
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.78
16.78
0.9574
0.9574
9.343
9.343
0.5331
0.5331
8.428
8.428
0.4808
0.4808
2.227
2.227
407.7
407.7
2750
2750
1040
1040
---
---
41
COMPOSITION
42 43
Overall Phase
44 45
COMPONENTS
46
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
47
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
48
H2O
3.3148
0.0065
59.7169
0.0067
4.0972
0.0041
49
Oxygen
9.5615
0.0187
305.9667
0.0341
18.4150
0.0182
50
Methane
6.9652
0.0136
111.7423
0.0125
25.5560
0.0253
51
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
Hydrogen
7.9795
0.0156
16.0867
0.0018
15.7675
0.0156
53
Ethane
5.5617
0.0109
167.2411
0.0186
32.1957
0.0318
54
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
CO2
4.1418
0.0081
182.2807
0.0203
15.1227
0.0150
56
Nitrogen
3.8311
0.0075
107.3196
0.0120
9.1130
0.0090
57
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
MEAmine
0.1976
0.0004
12.0674
0.0013
0.8125
0.0008
60
Ammonia
470.4139
0.9188
8011.1497
0.8927
890.3957
0.8803
61
Total
511.9730
1.0000
8973.7359
1.0000
1011.4894
1.0000
62
Liquid Phase
63 64
COMPONENTS
65
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
66
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
67
H2O
3.3148
0.0065
59.7169
0.0067
4.0972
0.0041
68
Oxygen
9.5615
0.0187
305.9667
0.0341
18.4150
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0182
Page 219 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 75 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Methane
6.9652
0.0136
111.7423
0.0125
25.5560
0.0253
16
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Hydrogen
7.9795
0.0156
16.0867
0.0018
15.7675
0.0156
18
Ethane
5.5617
0.0109
167.2411
0.0186
32.1957
0.0318
19
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
CO2
4.1418
0.0081
182.2807
0.0203
15.1227
0.0150
21
Nitrogen
3.8311
0.0075
107.3196
0.0120
9.1130
0.0090
22
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
MEAmine
0.1976
0.0004
12.0674
0.0013
0.8125
0.0008
25
Ammonia
470.4139
0.9188
8011.1497
0.8927
890.3957
0.8803
26
Total
511.9730
1.0000
8973.7359
1.0000
1011.4894
1.0000
27
K VALUE
28 29
COMPONENTS
MIXED
LIGHT
HEAVY
30
CO
0.0000
0.0000
---
31
H2O
0.0000
0.0000
---
32
Oxygen
0.0000
0.0000
---
33
Methane
0.0000
0.0000
---
---
---
---
34
H2S
35
Hydrogen
0.0000
0.0000
---
36
Ethane
0.0000
0.0000
---
37
Propane
---
---
---
38
CO2
0.0000
0.0000
---
39
Nitrogen
0.0000
0.0000
---
---
---
---
40
Air
41
Mercury
---
---
---
42
MEAmine
0.0000
0.0000
---
43
Ammonia
0.0000
0.0000
---
44
UNIT OPERATIONS
45 46 47
FEED TO
PRODUCT FROM
Valve:
VLV-102 Mixer:
48
LOGICAL CONNECTION MIX-103
UTILITIES
49 50
( No utilities reference this stream )
51
PROCESS UTILITY
52 53 54
DYNAMICS
55 56
Pressure Specification
(Inactive):
57
Flow Specification
(Inactive) Molar:
58
4565 psia 512.0 lbmole/hrMass:
8974 lb/hr Std Ideal Liq Volume:
1011 barrel/day
User Variables
59 60
NOTES
61 62 63
Description
64 65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 220 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 76
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0728
0.0728
0.9272
(F)
90.84
90.84
90.84
(psia)
579.7*
579.7
579.7
512.0
37.26
474.7
8974
693.0
8281
1011
86.59
924.9
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-2.901e+004 21.45 -1.485e+007 1040*
(barrel/day)
22
-1.541e+004 33.22 -5.744e+005 6.015e+004
-3.008e+004 20.53 -1.428e+007 926.0
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase
Liquid Phase
17.53
18.60
17.44
0.9015
0.1088
2.104
15.80
2.024
36.71
(barrel/day)
2428
1463
964.3
Mass Enthalpy
(Btu/lb)
-1655
-828.9
-1724
30
Mass Entropy
(Btu/lb-F)
1.224
1.786
1.177
31
Heat Capacity
19.92
9.204
20.76
32
Mass Heat Capacity
1.136
0.4949
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.384e+005
1.301e+005
1.390e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.641e+005
1.491e+005
1.653e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
8.560e-002
8.560e-002
0.9144
41
Phase Fraction [Mass Basis]
7.722e-002
7.722e-002
0.9228
42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.190
9364
8017
9477
---
---
17.58
(lbmole/ft3)
---
---
1.540e-002
(lbmol/lb)
---
---
4.195e-004
(Btu/lb)
7894
6997
7969
0.6028
0.6028
0.3972
(Btu/lb)
152.0
---
---
(psia)
10.40
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
5.706
5.706
---
(lbmole/ft3)
2.164
1.840
2.194
Specific Heat
(Btu/lbmole-F)
19.92
9.204
20.76
Std. Gas Flow
(MMSCFD)
4.654
0.3387
4.315
(lb/ft3)
37.92
34.21
38.27
(USGPS)
0.4687
---
0.4687
Licensed to: LEGENDS
(psia)
(Btu/lbmole)
---
0.9015
12.20
11.15
12.26
---
---
---
0.0000
---
---
1.111
1.275
1.106
1.022
1.505
2.315
1.592e+004
4.663e-002
---
---
0.4047
0.1900
(cSt)
---
(lb/ft3)
36.90
4.925e-002
38.23
1040
6.015e+004
926.0
(barrel/day) (ft3/lbmole) (Btu/lb)
0.9272
0.0000
1.000
1.109
9.187
0.4752
908.5
---
---
0.0728
0.0728
0.9272
(dyne/cm)
23.80
(Btu/hr-ft-F)
---
(cP)
---
---
23.80
2.664e-002
0.2547
1.312e-002
0.1117
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 221 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 76 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Liquid Phase
17.93
7.218
18.78
1.023
0.3881
1.076
19.49
6.114
8.970
1.112
0.3288
0.5142
---
---
5.381
(Btu/lb-F)
---
---
0.3085
---
---
3.859
Reid VP at 37.8 C
(psia)
407.7
---
269.3
20
True VP at 37.8 C
(psia)
2750
---
590.3
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
6.107e+004 ---
6.015e+004 ---
23
926.0 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0728
LIQUID VOLUME FRACTION
29
CO
0.0059
0.0000
0.1649
0.0000
0.0141
0.0000
30
H2O
3.3148
0.0065
59.7169
0.0067
4.0972
0.0041
31
Oxygen
9.5615
0.0187
305.9667
0.0341
18.4150
0.0182
32
Methane
6.9652
0.0136
111.7423
0.0125
25.5560
0.0253
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
7.9795
0.0156
16.0867
0.0018
15.7675
0.0156
35
Ethane
5.5617
0.0109
167.2411
0.0186
32.1957
0.0318
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
4.1418
0.0081
182.2807
0.0203
15.1227
0.0150
38
Nitrogen
3.8311
0.0075
107.3196
0.0120
9.1130
0.0090
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1976
0.0004
12.0674
0.0013
0.8125
0.0008
42
Ammonia
470.4139
0.9188
8011.1497
0.8927
890.3957
0.8803
43
Total
511.9730
1.0000
8973.7359
1.0000
1011.4894
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
7.278e-002 LIQUID VOLUME FRACTION
48
CO
0.0051
0.0001
0.1420
0.0002
0.0122
0.0001
49
H2O
0.0003
0.0000
0.0046
0.0000
0.0003
0.0000
50
Oxygen
6.5747
0.1764
210.3910
0.3036
12.6627
0.1462
51
Methane
4.2266
0.1134
67.8069
0.0978
15.5078
0.1791
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
7.2567
0.1947
14.6295
0.0211
14.3392
0.1656
54
Ethane
1.2394
0.0333
37.2682
0.0538
7.1745
0.0829
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6684
0.0179
29.4143
0.0424
2.4403
0.0282
57
Nitrogen
3.5360
0.0949
99.0533
0.1429
8.4111
0.0971
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
61
Ammonia
13.7564
0.3692
234.2714
0.3381
26.0380
0.3007
62
Total
37.2635
1.0000
692.9812
1.0000
86.5860
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0008
0.0000
0.0228
0.0000
0.0020
68
H2O
3.3146
0.0070
59.7123
0.0072
4.0969
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.9272 LIQUID VOLUME FRACTION 0.0000 0.0044
Page 222 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 76 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9272 LIQUID VOLUME FRACTION
15
Oxygen
2.9867
0.0063
95.5757
0.0115
5.7524
0.0062
16
Methane
2.7386
0.0058
43.9354
0.0053
10.0482
0.0109
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.7228
0.0015
1.4572
0.0002
1.4283
0.0015
19
Ethane
4.3224
0.0091
129.9730
0.0157
25.0212
0.0271
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
3.4735
0.0073
152.8664
0.0185
12.6824
0.0137
22
Nitrogen
0.2951
0.0006
8.2663
0.0010
0.7019
0.0008
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
26
Ammonia
456.6575
0.9620
7776.8783
0.9392
864.3577
0.9345
27
Total
474.7096
1.0000
8280.7547
1.0000
924.9034
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
28.04
28.04
---
34
Methane
19.66
19.66
---
---
---
---
35
79.22
79.22
9.790e-004
H2S
---
9.790e-004
---
36
Hydrogen
127.9
127.9
---
37
Ethane
3.653
3.653
---
38
Propane
---
---
---
39
CO2
2.451
2.451
---
40
Nitrogen
152.7
152.7
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
1.015e-004 0.3838
45
---
0.3838
---
UNIT OPERATIONS
46 47 48
1.015e-004
FEED TO
PRODUCT FROM
Separator:
D-6
49
Valve:
LOGICAL CONNECTION VLV-102
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Active):
58
Flow Specification
(Inactive) Molar:
59
* 579.7 psia
512.0 lbmole/hrMass:
8974 lb/hr Std Ideal Liq Volume:
1011 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 223 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 77
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
1.0000
1.0000
0.0000
(F)
90.84
90.84
90.84
(psia)
579.7
579.7
579.7
37.26
37.26
0.0000
693.0
693.0
0.0000
86.59
86.59
(lbmole/hr) (lb/hr)
-1.541e+004 33.22
-1.541e+004 33.22
0.0000 -3.008e+004 20.53
(Btu/hr)
-5.744e+005
-5.744e+005
0.0000
(barrel/day)
* 6.015e+004
6.015e+004
0.0000
22
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29 30 31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.301e+005
1.301e+005
1.390e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.491e+005
1.491e+005
1.653e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41 42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48
Specific Heat
(Btu/lbmole-F)
9.204
9.204
20.76
49
Std. Gas Flow
(MMSCFD)
0.3387
0.3387
0.0000
50
Std. Ideal Liq. Mass Density
(lb/ft3)
34.21
34.21
38.27
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
---
0.9015
53
Watson K
11.15
11.15
12.26
54
User Property
---
---
---
55
Partial Pressure of H2S
0.0000
---
---
56
Cp/(Cp - R)
1.275
1.275
1.106
57
Cp/Cv
1.505
1.505
2.315
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
18.60
18.60
17.44
0.1088
0.1088
2.104
2.024
2.024
36.71
(barrel/day)
1463
1463
0.0000
Mass Enthalpy
(Btu/lb)
-828.9
-828.9
-1724
Mass Entropy
(Btu/lb-F)
1.786
1.786
1.177
9.204
9.204
20.76
0.4949
0.4949
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
8017
8017
9477
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
6997
6997
7969
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
Licensed to: LEGENDS
(Btu/lb)
1.190
1.000
1.000
0.0000
(Btu/lb)
204.7
---
---
(psia)
10.40
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
5.706
5.706
---
(lbmole/ft3)
1.840
1.840
2.194
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP)
1.027e+004 0.4047
--4.663e-002
---
---
0.4047
0.1900
4.925e-002
4.925e-002
38.23
6.015e+004
6.015e+004
0.0000
0.0000
0.0000
1.000
9.187
9.187
0.4752
552.4
---
---
1.0000
1.0000
0.0000
---
---
23.80
2.664e-002
2.664e-002
0.2547
1.312e-002
1.312e-002
0.1117
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 224 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 77 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
7.218
7.218
18.78
0.3881
0.3881
1.076
6.114
6.114
8.970
0.3288
0.3288
0.5142
---
---
5.381
---
---
0.3085
---
---
3.859
---
---
269.3
---
---
6.015e+004 ---
6.015e+004 ---
23
590.3 0.0000 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.0051
0.0001
0.1420
0.0002
0.0122
0.0001
30
H2O
0.0003
0.0000
0.0046
0.0000
0.0003
0.0000
31
Oxygen
6.5747
0.1764
210.3910
0.3036
12.6627
0.1462
32
Methane
4.2266
0.1134
67.8069
0.0978
15.5078
0.1791
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
7.2567
0.1947
14.6295
0.0211
14.3392
0.1656
35
Ethane
1.2394
0.0333
37.2682
0.0538
7.1745
0.0829
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.6684
0.0179
29.4143
0.0424
2.4403
0.0282
38
Nitrogen
3.5360
0.0949
99.0533
0.1429
8.4111
0.0971
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
42
Ammonia
13.7564
0.3692
234.2714
0.3381
26.0380
0.3007
43
Total
37.2635
1.0000
692.9812
1.0000
86.5860
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0051
0.0001
0.1420
0.0002
0.0122
0.0001
49
H2O
0.0003
0.0000
0.0046
0.0000
0.0003
0.0000
50
Oxygen
6.5747
0.1764
210.3910
0.3036
12.6627
0.1462
51
Methane
4.2266
0.1134
67.8069
0.0978
15.5078
0.1791
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
7.2567
0.1947
14.6295
0.0211
14.3392
0.1656
54
Ethane
1.2394
0.0333
37.2682
0.0538
7.1745
0.0829
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6684
0.0179
29.4143
0.0424
2.4403
0.0282
57
Nitrogen
3.5360
0.0949
99.0533
0.1429
8.4111
0.0971
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
61
Ammonia
13.7564
0.3692
234.2714
0.3381
26.0380
0.3007
62
Total
37.2635
1.0000
692.9812
1.0000
86.5860
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
0.0000
0.0070
0.0000
0.0072
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000 LIQUID VOLUME FRACTION 0.0000 0.0044
Page 225 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 77 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
Oxygen
0.0000
0.0063
0.0000
0.0115
0.0000
0.0062
16
Methane
0.0000
0.0058
0.0000
0.0053
0.0000
0.0109
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0000
0.0015
0.0000
0.0002
0.0000
0.0015
19
Ethane
0.0000
0.0091
0.0000
0.0157
0.0000
0.0271
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0000
0.0073
0.0000
0.0185
0.0000
0.0137
22
Nitrogen
0.0000
0.0006
0.0000
0.0010
0.0000
0.0008
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0000
0.0004
0.0000
0.0015
0.0000
0.0009
26
Ammonia
0.0000
0.9620
0.0000
0.9392
0.0000
0.9345
27
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
28.04
28.04
---
34
Methane
19.66
19.66
---
---
---
---
35
79.22
79.22
9.790e-004
H2S
---
9.790e-004
---
36
Hydrogen
127.9
127.9
---
37
Ethane
3.653
3.653
---
38
Propane
---
---
---
39
CO2
2.451
2.451
---
40
Nitrogen
152.7
152.7
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
1.015e-004 0.3838
45
---
0.3838
---
UNIT OPERATIONS
46 47 48
1.015e-004
FEED TO
PRODUCT FROM
Mixer:
MIX-104 Separator:
49
LOGICAL CONNECTION D-6
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
579.7 psia 37.26 lbmole/hrMass:
693.0 lb/hr Std Ideal Liq Volume:
86.59 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 226 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 78
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
90.84
90.84
90.84
(psia)
579.7
579.7
579.7
474.7
0.0000
474.7
8281
0.0000
8281
924.9
0.0000
924.9
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-3.008e+004 20.53 -1.428e+007 926.0*
(barrel/day)
22
-1.541e+004 33.22 0.0000 0.0000
-3.008e+004 20.53 -1.428e+007 926.0
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase
Liquid Phase
17.44
18.60
17.44
2.104
0.1088
2.104
36.71
2.024
36.71
(barrel/day)
964.3
0.0000
964.3
Mass Enthalpy
(Btu/lb)
-1724
-828.9
-1724
30
Mass Entropy
(Btu/lb-F)
1.177
1.786
1.177
31
Heat Capacity
20.76
9.204
20.76
32
Mass Heat Capacity
1.190
0.4949
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.390e+005
1.301e+005
1.390e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.653e+005
1.491e+005
1.653e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
1.540e-002
---
1.540e-002
38
CO2 App WT Con
(lbmol/lb)
4.195e-004
---
4.195e-004
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
41 42 43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.190
9477
8017
9477
17.58
---
17.58
7969
6997
7969
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
(Btu/lb)
140.9
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.194
1.840
2.194
Specific Heat
(Btu/lbmole-F)
20.76
9.204
20.76
Std. Gas Flow
(MMSCFD)
4.315
0.0000
4.315
(lb/ft3)
38.27
34.21
38.27
(USGPS)
0.4687
---
0.4687
Licensed to: LEGENDS
---
0.9015
12.26
11.15
12.26
---
---
---
0.0000
---
---
1.106
1.275
1.106
2.315
1.505
2.315
8988
---
---
(cSt)
0.1900
0.4047
0.1900
(lb/ft3)
38.23
(psia)
(Btu/lbmole)
(barrel/day) (ft3/lbmole) (Btu/lb)
4.925e-002
4.663e-002
38.23
926.0
0.0000
1.000
0.0000
926.0 1.000
0.4752
9.187
0.4752
515.2
---
---
0.0000
0.0000
1.0000
(dyne/cm)
23.80
(Btu/hr-ft-F)
0.2547
2.664e-002
0.2547
0.1117
1.312e-002
0.1117
(cP)
---
23.80
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 227 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 78 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
18.78
7.218
18.78
1.076
0.3881
1.076
8.970
6.114
8.970
0.5142
0.3288
0.5142
5.381
---
5.381
0.3085
---
0.3085
3.859
---
3.859
269.3
---
269.3
590.3
---
590.3
926.0
0.0000
926.0
---
---
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.0008
0.0000
0.0228
0.0000
0.0020
0.0000
30
H2O
3.3146
0.0070
59.7123
0.0072
4.0969
0.0044
31
Oxygen
2.9867
0.0063
95.5757
0.0115
5.7524
0.0062
32
Methane
2.7386
0.0058
43.9354
0.0053
10.0482
0.0109
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.7228
0.0015
1.4572
0.0002
1.4283
0.0015
35
Ethane
4.3224
0.0091
129.9730
0.0157
25.0212
0.0271
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
3.4735
0.0073
152.8664
0.0185
12.6824
0.0137
38
Nitrogen
0.2951
0.0006
8.2663
0.0010
0.7019
0.0008
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
42
Ammonia
456.6575
0.9620
7776.8783
0.9392
864.3577
0.9345
43
Total
474.7096
1.0000
8280.7547
1.0000
924.9034
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0001
0.0000
0.0002
0.0000
0.0001
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.1764
0.0000
0.3036
0.0000
0.1462
51
Methane
0.0000
0.1134
0.0000
0.0978
0.0000
0.1791
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.1947
0.0000
0.0211
0.0000
0.1656
54
Ethane
0.0000
0.0333
0.0000
0.0538
0.0000
0.0829
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0179
0.0000
0.0424
0.0000
0.0282
57
Nitrogen
0.0000
0.0949
0.0000
0.1429
0.0000
0.0971
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.3692
0.0000
0.3381
0.0000
0.3007
62
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0008
0.0000
0.0228
0.0000
0.0020
68
H2O
3.3146
0.0070
59.7123
0.0072
4.0969
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.000 LIQUID VOLUME FRACTION 0.0000 0.0044
Page 228 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 78 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Oxygen
2.9867
0.0063
95.5757
0.0115
5.7524
0.0062
16
Methane
2.7386
0.0058
43.9354
0.0053
10.0482
0.0109
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.7228
0.0015
1.4572
0.0002
1.4283
0.0015
19
Ethane
4.3224
0.0091
129.9730
0.0157
25.0212
0.0271
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
3.4735
0.0073
152.8664
0.0185
12.6824
0.0137
22
Nitrogen
0.2951
0.0006
8.2663
0.0010
0.7019
0.0008
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
26
Ammonia
456.6575
0.9620
7776.8783
0.9392
864.3577
0.9345
27
Total
474.7096
1.0000
8280.7547
1.0000
924.9034
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
28.04
28.04
---
34
Methane
19.66
19.66
---
---
---
---
35
79.22
79.22
9.790e-004
H2S
---
9.790e-004
---
36
Hydrogen
127.9
127.9
---
37
Ethane
3.653
3.653
---
38
Propane
---
---
---
39
CO2
2.451
2.451
---
40
Nitrogen
152.7
152.7
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
1.015e-004 0.3838
45
---
0.3838
---
UNIT OPERATIONS
46 47 48
1.015e-004
FEED TO
PRODUCT FROM
Valve:
VLV-103 Separator:
49
LOGICAL CONNECTION D-6
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
579.7 psia 474.7 lbmole/hrMass:
8281 lb/hr Std Ideal Liq Volume:
924.9 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 229 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 79
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Vapour Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
2069
2050
18
Molar Enthalpy
(Btu/lbmole)
-8420
-8168
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Liquid Phase
0.9888
0.9888
0.0112
(F)
30.80
30.80
30.80
(psia)
579.7
579.7
579.7
902.4
892.3
10.13
(lbmole/hr) (lb/hr)
1.519e+004
29.61
1.501e+004
29.74
(Btu/hr)
-7.598e+006
-7.289e+006
(barrel/day)
* 1.460e+006
1.443e+006
22
175.7 19.65 -3.058e+004 18.14 -3.097e+005 19.69
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-500.3
-485.5
-1762
30
Mass Entropy
(Btu/lb-F)
1.759
1.767
1.045
31
Heat Capacity
8.064
7.940
18.96
32
Mass Heat Capacity
0.4791
0.4719
33
LHV Molar Basis (Std)
(Btu/lbmole)
9.858e+004
9.812e+004
1.388e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.127e+005
1.121e+005
1.652e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
16.83
16.82
17.35
0.1160
0.1147
2.281
1.952
1.930
39.58
3.326e+004
3.324e+004
18.98
1.093
6698
6665
9519
---
---
252.0
(lbmole/ft3)
---
---
1.498e-002
(lbmol/lb)
---
---
3.786e-004
(Btu/lb)
5857
5832
Phase Fraction [Vol. Basis]
0.9905
0.9905
9.496e-003
41
Phase Fraction [Mass Basis]
0.9884
0.9884
1.157e-002
42
Phase Fraction [Act. Vol. Basis]
0.9994
0.9994
5.706e-004
43
Mass Exergy
(Btu/lb)
232.3
---
44
Partial Pressure of CO2
(psia)
5.407
---
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
8001
---
(ACFM)
129.6
129.6
---
(lbmole/ft3)
1.864
1.861
2.203
Specific Heat
(Btu/lbmole-F)
8.064
7.940
Std. Gas Flow
(MMSCFD)
8.203
8.111
31.38
31.31
Licensed to: LEGENDS
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
9.226e-003
(Btu/lb)
9.226e-003 4.829e-002
---
0.9599 10.42
12.26
---
---
---
0.0000
---
---
1.327
1.334
1.117
1.451
1.469
2.291
6672
---
---
---
0.4158
0.2542
4.448e-002
4.446e-002
38.14
1.460e+006
1.443e+006
19.69
8.623
0.0000
1.000
8.715
0.4384
396.4
---
---
0.9888
0.9888
0.0112
(dyne/cm)
31.44
(Btu/hr-ft-F)
---
(cP)
38.23
---
10.46
1.122e-002 (ft3/lbmole)
18.96 9.205e-002
---
---
31.44
3.163e-002
0.3003
1.286e-002
0.1612
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 230 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 79 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
6.078
5.954
16.98
0.3611
0.3539
0.9782
5.556
5.406
8.276
0.3302
0.3213
0.4769
---
---
7.024
---
---
0.4047
---
---
2.700
---
---
256.1
---
---
535.2
1.443e+006 ---
1.443e+006 ---
23
19.69 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9888
LIQUID VOLUME FRACTION
29
CO
0.1879
0.0002
5.2641
0.0003
0.4509
0.0002
30
H2O
0.0113
0.0000
0.2043
0.0000
0.0140
0.0000
31
Oxygen
127.8998
0.1417
4092.7930
0.2695
246.3303
0.1190
32
Methane
76.1493
0.0844
1221.6554
0.0804
279.3984
0.1350
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
326.1304
0.3614
657.4789
0.0433
644.4320
0.3114
35
Ethane
18.8221
0.0209
565.9774
0.0373
108.9568
0.0527
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
8.3890
0.0093
369.1980
0.0243
30.6300
0.0148
38
Nitrogen
218.7696
0.2424
6128.3941
0.4035
520.3894
0.2515
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0003
0.0000
0.0161
0.0000
0.0011
0.0000
42
Ammonia
126.0805
0.1397
2147.1509
0.1414
238.6441
0.1153
43
Total
902.4402
1.0000
15188.1323
1.0000
2069.2471
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9888 LIQUID VOLUME FRACTION
48
CO
0.1879
0.0002
5.2636
0.0004
0.4509
0.0002
49
H2O
0.0001
0.0000
0.0011
0.0000
0.0001
0.0000
50
Oxygen
127.8563
0.1433
4091.4026
0.2725
246.2467
0.1201
51
Methane
76.1105
0.0853
1221.0333
0.0813
279.2561
0.1362
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
326.1148
0.3655
657.4474
0.0438
644.4012
0.3144
54
Ethane
18.7457
0.0210
563.6823
0.0375
108.5149
0.0529
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
8.3225
0.0093
366.2700
0.0244
30.3871
0.0148
57
Nitrogen
218.7617
0.2452
6128.1726
0.4082
520.3706
0.2539
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
116.2143
0.1302
1979.1303
0.1318
219.9696
0.1073
62
Total
892.3139
1.0000
15012.4032
1.0000
2049.5970
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0005
0.0000
0.0000
68
H2O
0.0113
0.0011
0.2032
0.0012
0.0139
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.122e-002 LIQUID VOLUME FRACTION 0.0000 0.0007
Page 231 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 79 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.122e-002 LIQUID VOLUME FRACTION
15
Oxygen
0.0435
0.0043
1.3905
0.0079
0.0837
0.0043
16
Methane
0.0388
0.0038
0.6221
0.0035
0.1423
0.0072
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0156
0.0015
0.0315
0.0002
0.0309
0.0016
19
Ethane
0.0763
0.0075
2.2951
0.0131
0.4418
0.0225
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0665
0.0066
2.9280
0.0167
0.2429
0.0124
22
Nitrogen
0.0079
0.0008
0.2215
0.0013
0.0188
0.0010
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0003
0.0000
0.0161
0.0001
0.0011
0.0001
26
Ammonia
9.8662
0.9743
168.0206
0.9561
18.6746
0.9504
27
Total
10.1263
1.0000
175.7291
1.0000
19.6500
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
33.39
33.39
---
34
Methane
22.27
22.27
---
---
---
---
35
H2S
124.0
124.0
6.284e-005
---
6.284e-005
---
36
Hydrogen
236.9
236.9
---
37
Ethane
2.787
2.787
---
38
Propane
---
---
---
39
CO2
1.420
1.420
---
40
Nitrogen
313.9
313.9
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
45
3.801e-006
0.1337
---
0.1337
---
UNIT OPERATIONS
46 47 48
3.801e-006
FEED TO
PRODUCT FROM
Mixer:
MIX-107 Mixer:
49
LOGICAL CONNECTION MIX-104
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
579.7 psia 902.4 lbmole/hrMass:
1.519e+004 lb/hrStd Ideal Liq Volume:
2069 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 232 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 80
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0450
0.0450
0.9550
(F)
79.29
79.29
79.29
(psia)
229.7*
229.7
229.7
474.7
21.38
453.3
8281
423.1
7858
924.9
49.93
875.0
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-3.008e+004 20.62 -1.428e+007 926.0*
(barrel/day)
22
-2.368e+004 36.78 -5.063e+005 58.99
-3.038e+004 19.86 -1.377e+007 873.7
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase 17.44
(lbmole/ft3) (lb/ft3)
0.6827
19.79 4.403e-002
Liquid Phase 17.33 2.161
11.91
0.8712
37.47
(barrel/day)
2972
2076
896.5
Mass Enthalpy
(Btu/lb)
-1724
-1197
-1753
30
Mass Entropy
(Btu/lb-F)
1.182
1.859
1.146
31
Heat Capacity
19.96
9.556
20.45
32
Mass Heat Capacity
1.144
0.4829
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.390e+005
1.596e+005
1.380e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.653e+005
1.840e+005
1.644e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
5.399e-002
5.399e-002
0.9460
41
Phase Fraction [Mass Basis]
5.110e-002
5.110e-002
0.9489
42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.180
9477
9297
9487
---
---
14.19
(lbmole/ft3)
---
---
1.336e-002
(lbmol/lb)
---
---
3.567e-004
(Btu/lb)
7969
8065
7964
0.6984
0.6984
0.3016
(Btu/lb)
138.1
---
---
(psia)
7.202
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
8.094
8.094
---
(lbmole/ft3)
2.194
1.831
2.215
Specific Heat
(Btu/lbmole-F)
19.96
9.556
20.45
Std. Gas Flow
(MMSCFD)
4.315
0.1944
4.121
(lb/ft3)
38.27
36.22
38.39
(USGPS)
0.4358
---
0.4358
Licensed to: LEGENDS
(psia)
(Btu/lbmole)
---
0.9020
12.26
12.02
12.27
---
---
---
0.0000
---
---
1.110
1.262
1.108
1.010
1.434
2.319
1.781e+004
1.837e-002
---
---
(cSt)
---
0.7361
0.2063
(lb/ft3)
38.23
30.66
38.45
926.0
58.99
873.7
0.9550
0.0000
1.000
1.465
22.71
0.4626
(barrel/day) (ft3/lbmole) (Btu/lb)
1021
---
---
0.0450
0.0450
0.9550
(dyne/cm)
25.66
(Btu/hr-ft-F)
---
(cP)
---
---
25.66
1.775e-002
0.2688
1.027e-002
0.1238
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 233 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 80 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F)
Vapour Phase
Liquid Phase
17.98
7.570
18.47
1.030
0.3826
1.065
19.76
6.664
8.820
1.133
0.3368
0.5088
---
---
---
---
---
---
---
---
---
(psia)
269.3
1139
234.0
(psia)
590.3
4258
287.9
932.6
58.99
873.7
-95.12
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0450
LIQUID VOLUME FRACTION
29
CO
0.0008
0.0000
0.0228
0.0000
0.0020
0.0000
30
H2O
3.3146
0.0070
59.7123
0.0072
4.0969
0.0044
31
Oxygen
2.9867
0.0063
95.5757
0.0115
5.7524
0.0062
32
Methane
2.7386
0.0058
43.9354
0.0053
10.0482
0.0109
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.7228
0.0015
1.4572
0.0002
1.4283
0.0015
35
Ethane
4.3224
0.0091
129.9730
0.0157
25.0212
0.0271
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
3.4735
0.0073
152.8664
0.0185
12.6824
0.0137
38
Nitrogen
0.2951
0.0006
8.2663
0.0010
0.7019
0.0008
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
42
Ammonia
456.6575
0.9620
7776.8783
0.9392
864.3577
0.9345
43
Total
474.7096
1.0000
8280.7547
1.0000
924.9034
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
4.504e-002 LIQUID VOLUME FRACTION
48
CO
0.0007
0.0000
0.0208
0.0000
0.0018
0.0000
49
H2O
0.0002
0.0000
0.0030
0.0000
0.0002
0.0000
50
Oxygen
2.3046
0.1078
73.7467
0.1743
4.4385
0.0889
51
Methane
1.9138
0.0895
30.7036
0.0726
7.0221
0.1406
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.6839
0.0320
1.3788
0.0033
1.3514
0.0271
54
Ethane
1.1831
0.0553
35.5767
0.0841
6.8489
0.1372
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6704
0.0314
29.5045
0.0697
2.4478
0.0490
57
Nitrogen
0.2817
0.0132
7.8902
0.0186
0.6700
0.0134
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
14.3442
0.6708
244.2812
0.5774
27.1505
0.5438
62
Total
21.3826
1.0000
423.1056
1.0000
49.9312
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0001
0.0000
0.0020
0.0000
0.0002
68
H2O
3.3144
0.0073
59.7093
0.0076
4.0967
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.9550 LIQUID VOLUME FRACTION 0.0000 0.0047
Page 234 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 80 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9550 LIQUID VOLUME FRACTION
15
Oxygen
0.6822
0.0015
21.8290
0.0028
1.3138
0.0015
16
Methane
0.8248
0.0018
13.2318
0.0017
3.0262
0.0035
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0389
0.0001
0.0784
0.0000
0.0769
0.0001
19
Ethane
3.1392
0.0069
94.3963
0.0120
18.1723
0.0208
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
2.8031
0.0062
123.3618
0.0157
10.2345
0.0117
22
Nitrogen
0.0134
0.0000
0.3761
0.0000
0.0319
0.0000
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
26
Ammonia
442.3134
0.9757
7532.5971
0.9586
837.2072
0.9568
27
Total
453.3270
1.0000
7857.6491
1.0000
874.9722
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
71.62
71.62
---
34
Methane
49.19
49.19
---
---
---
---
35
218.0
218.0
1.068e-003
H2S
---
1.068e-003
---
36
Hydrogen
372.7
372.7
---
37
Ethane
7.990
7.990
---
38
Propane
---
---
---
39
CO2
5.071
5.071
---
40
Nitrogen
444.8
444.8
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
8.673e-005 0.6875
45
---
0.6875
---
UNIT OPERATIONS
46 47 48
8.673e-005
FEED TO
PRODUCT FROM
Separator:
D-7
49
Valve:
LOGICAL CONNECTION VLV-103
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Active):
58
Flow Specification
(Inactive) Molar:
59
* 229.7 psia
474.7 lbmole/hrMass:
8281 lb/hr Std Ideal Liq Volume:
924.9 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 235 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 81
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
1.0000
1.0000
0.0000
(F)
79.29
79.29
79.29
(psia)
229.7
229.7
229.7
21.38
21.38
0.0000
423.1
423.1
0.0000
49.93
49.93
(lbmole/hr) (lb/hr)
(Btu/hr)
-2.368e+004 36.78 -5.063e+005 58.99*
(barrel/day)
22
-2.368e+004 36.78 -5.063e+005 58.99
0.0000 -3.038e+004 19.86 0.0000 0.0000
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29 30 31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.596e+005
1.596e+005
1.380e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.840e+005
1.840e+005
1.644e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40 41 42
Phase Fraction [Act. Vol. Basis]
43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48
Specific Heat
(Btu/lbmole-F)
9.556
9.556
20.45
49
Std. Gas Flow
(MMSCFD)
0.1944
0.1944
0.0000
50
Std. Ideal Liq. Mass Density
(lb/ft3)
36.22
36.22
38.39
51
Act. Liq. Flow
(USGPS)
---
---
52
Z Factor
---
0.9020
53
Watson K
12.02
12.02
12.27
54
User Property
---
---
---
55
Partial Pressure of H2S
0.0000
---
---
56
Cp/(Cp - R)
1.262
1.262
1.108
57
Cp/Cv
1.434
1.434
2.319
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
19.79 (lbmole/ft3) (lb/ft3)
4.403e-002
19.79 4.403e-002
17.33 2.161
0.8712
0.8712
37.47
(barrel/day)
2076
2076
0.0000
Mass Enthalpy
(Btu/lb)
-1197
-1197
-1753
Mass Entropy
(Btu/lb-F)
1.859
1.859
1.146
9.556
9.556
20.45
0.4829
0.4829
(Btu/lbmole-F) (Btu/lb-F)
9297
9297
9487
---
---
---
(lbmole/ft3)
---
---
---
(lbmol/lb)
---
---
---
(Btu/lb)
8065
8065
7964
Phase Fraction [Vol. Basis]
1.000
1.000
---
Phase Fraction [Mass Basis]
1.000
1.000
0.0000
Licensed to: LEGENDS
(Btu/lb)
1.180
1.000
1.000
0.0000
(Btu/lb)
143.2
---
---
(psia)
7.202
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
8.094
8.094
---
(lbmole/ft3)
1.831
1.831
2.215
(psia)
(Btu/lbmole)
1.458e+004
--1.837e-002
---
--0.2063
(cSt)
0.7361
0.7361
(lb/ft3)
30.66
30.66
38.45
58.99
58.99
0.0000
0.0000
0.0000
1.000
22.71
22.71
0.4626
(barrel/day) (ft3/lbmole) (Btu/lb) (dyne/cm) (Btu/hr-ft-F) (cP)
736.9
---
---
1.0000
1.0000
0.0000
---
---
25.66
1.775e-002
1.775e-002
0.2688
1.027e-002
1.027e-002
0.1238
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 236 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 81 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
7.570
7.570
18.47
0.3826
0.3826
1.065
6.664
6.664
8.820
0.3368
0.3368
0.5088
---
---
---
---
---
---
---
---
---
1139
1139
234.0
4258
4258
287.9
58.99
58.99
0.0000
---
---
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.0007
0.0000
0.0208
0.0000
0.0018
0.0000
30
H2O
0.0002
0.0000
0.0030
0.0000
0.0002
0.0000
31
Oxygen
2.3046
0.1078
73.7467
0.1743
4.4385
0.0889
32
Methane
1.9138
0.0895
30.7036
0.0726
7.0221
0.1406
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.6839
0.0320
1.3788
0.0033
1.3514
0.0271
35
Ethane
1.1831
0.0553
35.5767
0.0841
6.8489
0.1372
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.6704
0.0314
29.5045
0.0697
2.4478
0.0490
38
Nitrogen
0.2817
0.0132
7.8902
0.0186
0.6700
0.0134
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
14.3442
0.6708
244.2812
0.5774
27.1505
0.5438
43
Total
21.3826
1.0000
423.1056
1.0000
49.9312
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0007
0.0000
0.0208
0.0000
0.0018
0.0000
49
H2O
0.0002
0.0000
0.0030
0.0000
0.0002
0.0000
50
Oxygen
2.3046
0.1078
73.7467
0.1743
4.4385
0.0889
51
Methane
1.9138
0.0895
30.7036
0.0726
7.0221
0.1406
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.6839
0.0320
1.3788
0.0033
1.3514
0.0271
54
Ethane
1.1831
0.0553
35.5767
0.0841
6.8489
0.1372
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.6704
0.0314
29.5045
0.0697
2.4478
0.0490
57
Nitrogen
0.2817
0.0132
7.8902
0.0186
0.6700
0.0134
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
14.3442
0.6708
244.2812
0.5774
27.1505
0.5438
62
Total
21.3826
1.0000
423.1056
1.0000
49.9312
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
0.0000
0.0073
0.0000
0.0076
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000 LIQUID VOLUME FRACTION 0.0000 0.0047
Page 237 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 81 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
15
Oxygen
0.0000
0.0015
0.0000
0.0028
0.0000
0.0015
16
Methane
0.0000
0.0018
0.0000
0.0017
0.0000
0.0035
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0000
0.0001
0.0000
0.0000
0.0000
0.0001
19
Ethane
0.0000
0.0069
0.0000
0.0120
0.0000
0.0208
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0000
0.0062
0.0000
0.0157
0.0000
0.0117
22
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0000
0.0004
0.0000
0.0015
0.0000
0.0009
26
Ammonia
0.0000
0.9757
0.0000
0.9586
0.0000
0.9568
27
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
71.62
71.62
---
34
Methane
49.19
49.19
---
---
---
---
35
218.0
218.0
1.068e-003
H2S
---
1.068e-003
---
36
Hydrogen
372.7
372.7
---
37
Ethane
7.990
7.990
---
38
Propane
---
---
---
39
CO2
5.071
5.071
---
40
Nitrogen
444.8
444.8
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
8.673e-005 0.6875
45
---
0.6875
---
UNIT OPERATIONS
46 47 48
8.673e-005
FEED TO
PRODUCT FROM
Mixer:
MIX-107 Separator:
49
LOGICAL CONNECTION D-7
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
229.7 psia 21.38 lbmole/hrMass:
423.1 lb/hr Std Ideal Liq Volume:
49.93 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 238 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 82
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
79.29
79.29
79.29
(psia)
229.7
229.7
229.7
453.3
0.0000
453.3
7858
0.0000
7858
875.0
0.0000
875.0
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-3.038e+004 19.86 -1.377e+007 873.7*
(barrel/day)
22
-2.368e+004 36.78 0.0000 0.0000
-3.038e+004 19.86 -1.377e+007 873.7
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase 17.33
(lbmole/ft3) (lb/ft3)
2.161
19.79 4.403e-002
Liquid Phase 17.33 2.161
37.47
0.8712
37.47
(barrel/day)
896.5
0.0000
896.5
Mass Enthalpy
(Btu/lb)
-1753
-1197
-1753
30
Mass Entropy
(Btu/lb-F)
1.146
1.859
1.146
31
Heat Capacity
20.45
9.556
20.45
32
Mass Heat Capacity
1.180
0.4829
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.380e+005
1.596e+005
1.380e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.644e+005
1.840e+005
1.644e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
1.336e-002
---
1.336e-002
38
CO2 App WT Con
(lbmol/lb)
3.567e-004
---
3.567e-004
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
41 42 43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.180
9487
9297
9487
14.19
---
14.19
7964
8065
7964
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
(Btu/lb)
135.7
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.215
1.831
2.215
Specific Heat
(Btu/lbmole-F)
20.45
9.556
20.45
Std. Gas Flow
(MMSCFD)
4.121
0.0000
4.121
(lb/ft3)
38.39
36.22
38.39
(USGPS)
0.4358
---
0.4358
Licensed to: LEGENDS
---
0.9020
12.27
12.02
12.27
---
---
---
0.0000
---
---
1.108
1.262
1.108
2.319
1.434
2.319
9450
---
---
(cSt)
0.2063
0.7361
0.2063
(lb/ft3)
38.45
30.66
38.45
873.7
0.0000
873.7
1.000
0.0000
1.000
0.4626
22.71
0.4626
(psia)
(Btu/lbmole)
(barrel/day) (ft3/lbmole) (Btu/lb)
1.837e-002
545.2
---
---
0.0000
0.0000
1.0000
(dyne/cm)
25.66
(Btu/hr-ft-F)
0.2688
1.775e-002
0.2688
0.1238
1.027e-002
0.1238
(cP)
---
25.66
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 239 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 82 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Liquid Phase
18.47
7.570
18.47
1.065
0.3826
1.065
8.820
6.664
8.820
0.5088
0.3368
0.5088
5.936
---
---
0.3425
---
---
3.445
---
---
(psia)
234.0
1139
234.0
(psia)
287.9
4258
287.9
873.7
0.0000
873.7
-62.73
---
---
(Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.0001
0.0000
0.0020
0.0000
0.0002
0.0000
30
H2O
3.3144
0.0073
59.7093
0.0076
4.0967
0.0047
31
Oxygen
0.6822
0.0015
21.8290
0.0028
1.3138
0.0015
32
Methane
0.8248
0.0018
13.2318
0.0017
3.0262
0.0035
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0389
0.0001
0.0784
0.0000
0.0769
0.0001
35
Ethane
3.1392
0.0069
94.3963
0.0120
18.1723
0.0208
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
2.8031
0.0062
123.3618
0.0157
10.2345
0.0117
38
Nitrogen
0.0134
0.0000
0.3761
0.0000
0.0319
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
42
Ammonia
442.3134
0.9757
7532.5971
0.9586
837.2072
0.9568
43
Total
453.3270
1.0000
7857.6491
1.0000
874.9722
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.1078
0.0000
0.1743
0.0000
0.0889
51
Methane
0.0000
0.0895
0.0000
0.0726
0.0000
0.1406
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0320
0.0000
0.0033
0.0000
0.0271
54
Ethane
0.0000
0.0553
0.0000
0.0841
0.0000
0.1372
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0314
0.0000
0.0697
0.0000
0.0490
57
Nitrogen
0.0000
0.0132
0.0000
0.0186
0.0000
0.0134
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.6708
0.0000
0.5774
0.0000
0.5438
62
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0001
0.0000
0.0020
0.0000
0.0002
68
H2O
3.3144
0.0073
59.7093
0.0076
4.0967
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.000 LIQUID VOLUME FRACTION 0.0000 0.0047
Page 240 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 82 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Oxygen
0.6822
0.0015
21.8290
0.0028
1.3138
0.0015
16
Methane
0.8248
0.0018
13.2318
0.0017
3.0262
0.0035
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0389
0.0001
0.0784
0.0000
0.0769
0.0001
19
Ethane
3.1392
0.0069
94.3963
0.0120
18.1723
0.0208
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
2.8031
0.0062
123.3618
0.0157
10.2345
0.0117
22
Nitrogen
0.0134
0.0000
0.3761
0.0000
0.0319
0.0000
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.1976
0.0004
12.0673
0.0015
0.8125
0.0009
26
Ammonia
442.3134
0.9757
7532.5971
0.9586
837.2072
0.9568
27
Total
453.3270
1.0000
7857.6491
1.0000
874.9722
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
71.62
71.62
---
34
Methane
49.19
49.19
---
---
---
---
35
218.0
218.0
1.068e-003
H2S
---
1.068e-003
---
36
Hydrogen
372.7
372.7
---
37
Ethane
7.990
7.990
---
38
Propane
---
---
---
39
CO2
5.071
5.071
---
40
Nitrogen
444.8
444.8
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
8.673e-005 0.6875
45
---
0.6875
---
UNIT OPERATIONS
46 47 48
8.673e-005
FEED TO
PRODUCT FROM
Tee:
TEE-105 Separator:
49
LOGICAL CONNECTION D-7
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
229.7 psia 453.3 lbmole/hrMass:
7858 lb/hr Std Ideal Liq Volume:
875.0 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 241 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 83
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18 19 20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.9999
0.9999
0.0001
(F)
6.086
6.086
6.086
(psia)
229.7
229.7
229.7
923.8
923.7
0.1169
(lbmole/hr) (lb/hr)
1.561e+004
1.561e+004
(barrel/day)
2119
2119
Molar Enthalpy
(Btu/lbmole)
-8773
-8769
Molar Entropy
(Btu/lbmole-F)
31.55
31.55
2.022 0.2166 -3.862e+004 16.32
(Btu/hr)
-8.104e+006
-8.100e+006
-4514
(barrel/day)
* 1.494e+006
1.494e+006
0.2158
22
PROPERTIES
23 24
Overall
Vapour Phase
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-519.1
-518.9
-2233
30
Mass Entropy
(Btu/lb-F)
1.867
1.867
0.9436
31
Heat Capacity
7.605
7.603
18.49
32
Mass Heat Capacity
0.4500
0.4499
33
LHV Molar Basis (Std)
(Btu/lbmole)
9.999e+004
9.998e+004
1.261e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.144e+005
1.144e+005
1.519e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
16.90 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
4.708e-002 0.7956 8.388e+004
16.90 4.708e-002 0.7955 8.388e+004
17.30 2.448 42.35 0.2041
1.069
6768
6768
8780
---
---
1.229
(lbmole/ft3)
---
---
6.601e-003
(lbmol/lb)
---
---
1.559e-004
(Btu/lb)
5917
5917
Phase Fraction [Vol. Basis]
0.9999
0.9999
1.022e-004
41
Phase Fraction [Mass Basis]
0.9999
0.9999
1.295e-004
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
2.433e-006
43
Mass Exergy
(Btu/lb)
174.9
---
44
Partial Pressure of CO2
(psia)
2.253
---
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
7292
---
(ACFM)
327.0
327.0
---
(lbmole/ft3)
1.863
1.863
2.307
Specific Heat
(Btu/lbmole-F)
7.605
7.603
Std. Gas Flow
(MMSCFD)
8.398
8.397
31.49
31.49
Licensed to: LEGENDS
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
9.920e-005
(Btu/lb)
9.920e-005 1.877e-002
---
0.9762 10.51
12.19
---
---
---
0.0000
---
---
1.353
1.354
1.120
1.419
1.419
1.939
6761
---
---
---
0.9345
0.3524
4.466e-002
4.466e-002
40.04
1.494e+006
1.494e+006
0.2158
21.24
0.0000
1.000
21.24
0.4084
400.1
---
---
0.9999
0.9999
0.0001
(dyne/cm)
38.74
(Btu/hr-ft-F)
---
(cP)
39.90
---
10.51
1.265e-004 (ft3/lbmole)
18.49 1.062e-003
---
---
38.74
2.875e-002
0.3254
1.191e-002
0.2391
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 242 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 83 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Vapour Phase
Liquid Phase
5.619
5.617
16.51
0.3325
0.3324
0.9543
5.359
5.357
9.538
0.3171
0.3170
0.5514
---
---
8.582
---
---
0.4961
---
---
2.155
---
---
218.7
---
---
1.494e+006 -40.52
23
1.494e+006 ---
292.8 0.2158 ---
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9999
LIQUID VOLUME FRACTION
29
CO
0.1887
0.0002
5.2849
0.0003
0.4527
0.0002
30
H2O
0.0115
0.0000
0.2074
0.0000
0.0142
0.0000
31
Oxygen
130.2044
0.1409
4166.5397
0.2669
250.7689
0.1183
32
Methane
78.0631
0.0845
1252.3590
0.0802
286.4204
0.1352
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
326.8143
0.3538
658.8577
0.0422
645.7834
0.3047
35
Ethane
20.0052
0.0217
601.5541
0.0385
115.8057
0.0546
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
9.0594
0.0098
398.7025
0.0255
33.0778
0.0156
38
Nitrogen
219.0513
0.2371
6136.2843
0.3931
521.0594
0.2459
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0003
0.0000
0.0162
0.0000
0.0011
0.0000
42
Ammonia
140.4247
0.1520
2391.4321
0.1532
265.7947
0.1254
43
Total
923.8228
1.0000
15611.2379
1.0000
2119.1783
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9999 LIQUID VOLUME FRACTION
48
CO
0.1887
0.0002
5.2849
0.0003
0.4527
0.0002
49
H2O
0.0021
0.0000
0.0377
0.0000
0.0026
0.0000
50
Oxygen
130.2043
0.1410
4166.5366
0.2669
250.7687
0.1183
51
Methane
78.0631
0.0845
1252.3582
0.0802
286.4202
0.1352
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
326.8143
0.3538
658.8576
0.0422
645.7834
0.3048
54
Ethane
20.0051
0.0217
601.5518
0.0385
115.8052
0.0547
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
9.0591
0.0098
398.6886
0.0255
33.0767
0.0156
57
Nitrogen
219.0513
0.2371
6136.2838
0.3931
521.0593
0.2459
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0005
0.0000
0.0000
0.0000
61
Ammonia
140.3180
0.1519
2389.6165
0.1531
265.5929
0.1253
62
Total
923.7060
1.0000
15609.2162
1.0000
2118.9617
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2O
0.0094
0.0806
0.1697
0.0839
0.0116
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.265e-004 LIQUID VOLUME FRACTION 0.0000 0.0537
Page 243 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 83 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.265e-004 LIQUID VOLUME FRACTION
15
Oxygen
0.0001
0.0008
0.0031
0.0015
0.0002
0.0009
16
Methane
0.0001
0.0004
0.0008
0.0004
0.0002
0.0009
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0000
0.0002
0.0001
0.0000
0.0001
0.0003
19
Ethane
0.0001
0.0007
0.0024
0.0012
0.0005
0.0021
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
0.0003
0.0027
0.0139
0.0069
0.0012
0.0053
22
Nitrogen
0.0000
0.0001
0.0005
0.0002
0.0000
0.0002
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0003
0.0022
0.0157
0.0077
0.0011
0.0049
26
Ammonia
0.1066
0.9122
1.8157
0.8981
0.2018
0.9318
27
Total
0.1169
1.0000
2.0217
1.0000
0.2166
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
169.2
169.2
---
34
Methane
194.3
194.3
---
---
---
---
35
744.8
744.8
2.811e-005
H2S
---
2.811e-005
---
36
Hydrogen
1481
1481
---
37
Ethane
32.10
32.10
---
38
Propane
---
---
---
39
CO2
3.638
3.638
---
40
Nitrogen
1626
1626
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
4.239e-006 0.1665
45
---
0.1665
---
UNIT OPERATIONS
46 47 48
4.239e-006
FEED TO
PRODUCT FROM
Absorber:
T-101
49
Mixer:
LOGICAL CONNECTION MIX-107
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
229.7 psia 923.8 lbmole/hrMass:
1.561e+004 lb/hrStd Ideal Liq Volume:
2119 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 244 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 84
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
79.29
79.29
79.29
(psia)
229.7
229.7
229.7
203.0
0.0000
203.0
3518
0.0000
3518
391.8
0.0000
391.8
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-3.038e+004 19.86 -6.167e+006 391.2*
(barrel/day)
22
-2.368e+004 36.78 0.0000 0.0000
-3.038e+004 19.86 -6.167e+006 391.2
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase 17.33
(lbmole/ft3) (lb/ft3)
2.161
19.79 4.403e-002
Liquid Phase 17.33 2.161
37.47
0.8712
37.47
(barrel/day)
401.4
0.0000
401.4
Mass Enthalpy
(Btu/lb)
-1753
-1197
-1753
30
Mass Entropy
(Btu/lb-F)
1.146
1.859
1.146
31
Heat Capacity
20.45
9.556
20.45
32
Mass Heat Capacity
1.180
0.4829
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.380e+005
1.596e+005
1.380e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.644e+005
1.840e+005
1.644e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
1.336e-002
---
1.336e-002
38
CO2 App WT Con
(lbmol/lb)
3.567e-004
---
3.567e-004
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
41 42 43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.180
9487
9297
9487
14.19
---
14.19
7964
8065
7964
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
(Btu/lb)
135.7
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.215
1.831
2.215
Specific Heat
(Btu/lbmole-F)
20.45
9.556
20.45
Std. Gas Flow
(MMSCFD)
1.845
0.0000
1.845
(lb/ft3)
38.39
36.22
38.39
(USGPS)
0.1951
---
0.1951
Licensed to: LEGENDS
---
0.9020
12.27
12.02
12.27
---
---
---
0.0000
---
---
1.108
1.262
1.108
2.319
1.434
2.319
9450
---
---
(cSt)
0.2063
0.7361
0.2063
(lb/ft3)
38.45
30.66
38.45
391.2
0.0000
391.2
1.000
0.0000
1.000
0.4626
22.71
0.4626
(psia)
(Btu/lbmole)
(barrel/day) (ft3/lbmole) (Btu/lb)
1.837e-002
545.2
---
---
0.0000
0.0000
1.0000
(dyne/cm)
25.66
(Btu/hr-ft-F)
0.2688
1.775e-002
0.2688
0.1238
1.027e-002
0.1238
(cP)
---
25.66
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 245 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 84 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Liquid Phase
18.47
7.570
18.47
1.065
0.3826
1.065
8.820
6.664
8.820
0.5088
0.3368
0.5088
5.936
---
---
0.3425
---
---
3.445
---
---
(psia)
234.0
1139
234.0
(psia)
287.9
4258
287.9
391.2
0.0000
391.2
-62.73
---
---
(Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0009
0.0000
0.0001
0.0000
30
H2O
1.4840
0.0073
26.7342
0.0076
1.8343
0.0047
31
Oxygen
0.3054
0.0015
9.7737
0.0028
0.5882
0.0015
32
Methane
0.3693
0.0018
5.9244
0.0017
1.3549
0.0035
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0174
0.0001
0.0351
0.0000
0.0344
0.0001
35
Ethane
1.4056
0.0069
42.2649
0.0120
8.1365
0.0208
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
1.2550
0.0062
55.2339
0.0157
4.5824
0.0117
38
Nitrogen
0.0060
0.0000
0.1684
0.0000
0.0143
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0885
0.0004
5.4030
0.0015
0.3638
0.0009
42
Ammonia
198.0410
0.9757
3372.6386
0.9586
374.8504
0.9568
43
Total
202.9722
1.0000
3518.1772
1.0000
391.7593
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.1078
0.0000
0.1743
0.0000
0.0889
51
Methane
0.0000
0.0895
0.0000
0.0726
0.0000
0.1406
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0320
0.0000
0.0033
0.0000
0.0271
54
Ethane
0.0000
0.0553
0.0000
0.0841
0.0000
0.1372
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0314
0.0000
0.0697
0.0000
0.0490
57
Nitrogen
0.0000
0.0132
0.0000
0.0186
0.0000
0.0134
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.6708
0.0000
0.5774
0.0000
0.5438
62
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0009
0.0000
0.0001
68
H2O
1.4840
0.0073
26.7342
0.0076
1.8343
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.000 LIQUID VOLUME FRACTION 0.0000 0.0047
Page 246 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 84 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Oxygen
0.3054
0.0015
9.7737
0.0028
0.5882
0.0015
16
Methane
0.3693
0.0018
5.9244
0.0017
1.3549
0.0035
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0174
0.0001
0.0351
0.0000
0.0344
0.0001
19
Ethane
1.4056
0.0069
42.2649
0.0120
8.1365
0.0208
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
1.2550
0.0062
55.2339
0.0157
4.5824
0.0117
22
Nitrogen
0.0060
0.0000
0.1684
0.0000
0.0143
0.0000
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.0885
0.0004
5.4030
0.0015
0.3638
0.0009
26
Ammonia
198.0410
0.9757
3372.6386
0.9586
374.8504
0.9568
27
Total
202.9722
1.0000
3518.1772
1.0000
391.7593
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
71.62
71.62
---
34
Methane
49.19
49.19
---
---
---
---
35
218.0
218.0
1.068e-003
H2S
---
1.068e-003
---
36
Hydrogen
372.7
372.7
---
37
Ethane
7.990
7.990
---
38
Propane
---
---
---
39
CO2
5.071
5.071
---
40
Nitrogen
444.8
444.8
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
8.673e-005 0.6875
45
---
0.6875
---
UNIT OPERATIONS
46 47 48
8.673e-005
FEED TO
PRODUCT FROM
Distillation:
T-7
49
Tee:
LOGICAL CONNECTION TEE-105
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
229.7 psia 203.0 lbmole/hrMass:
3518 lb/hr Std Ideal Liq Volume:
391.8 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 247 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 85
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
0.0000
0.0000
1.0000
(F)
79.29
79.29
79.29
(psia)
229.7
229.7
229.7
250.4*
0.0000
250.4
4339
0.0000
4339
483.2
0.0000
483.2
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
-3.038e+004 19.86 -7.606e+006 482.5*
(barrel/day)
22
-2.368e+004 36.78 0.0000 0.0000
-3.038e+004 19.86 -7.606e+006 482.5
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Vapour Phase 17.33
(lbmole/ft3) (lb/ft3)
2.161
19.79 4.403e-002
Liquid Phase 17.33 2.161
37.47
0.8712
37.47
(barrel/day)
495.1
0.0000
495.1
Mass Enthalpy
(Btu/lb)
-1753
-1197
-1753
30
Mass Entropy
(Btu/lb-F)
1.146
1.859
1.146
31
Heat Capacity
20.45
9.556
20.45
32
Mass Heat Capacity
1.180
0.4829
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.380e+005
1.596e+005
1.380e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
1.644e+005
1.840e+005
1.644e+005
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
1.336e-002
---
1.336e-002
38
CO2 App WT Con
(lbmol/lb)
3.567e-004
---
3.567e-004
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
41 42 43
Mass Exergy
44
Partial Pressure of CO2
45
Cost Based on Flow
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.180
9487
9297
9487
14.19
---
14.19
7964
8065
7964
---
---
1.000
Phase Fraction [Mass Basis]
0.0000
0.0000
1.000
Phase Fraction [Act. Vol. Basis]
0.0000
0.0000
1.000
(Btu/lb)
135.7
---
---
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.215
1.831
2.215
Specific Heat
(Btu/lbmole-F)
20.45
9.556
20.45
Std. Gas Flow
(MMSCFD)
2.276
0.0000
2.276
(lb/ft3)
38.39
36.22
38.39
(USGPS)
0.2407
---
0.2407
Licensed to: LEGENDS
---
0.9020
12.27
12.02
12.27
---
---
---
0.0000
---
---
1.108
1.262
1.108
2.319
1.434
2.319
9450
---
---
(cSt)
0.2063
0.7361
0.2063
(lb/ft3)
38.45
30.66
38.45
482.5
0.0000
482.5
1.000
0.0000
1.000
0.4626
22.71
0.4626
(psia)
(Btu/lbmole)
(barrel/day) (ft3/lbmole) (Btu/lb)
1.837e-002
545.2
---
---
0.0000
0.0000
1.0000
(dyne/cm)
25.66
(Btu/hr-ft-F)
0.2688
1.775e-002
0.2688
0.1238
1.027e-002
0.1238
(cP)
---
25.66
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 248 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 85 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Liquid Phase
18.47
7.570
18.47
1.065
0.3826
1.065
8.820
6.664
8.820
0.5088
0.3368
0.5088
5.936
---
---
0.3425
---
---
3.445
---
---
(psia)
234.0
1139
234.0
(psia)
287.9
4258
287.9
482.5
0.0000
482.5
-62.73
---
---
(Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
30
H2O
1.8304
0.0073
32.9751
0.0076
2.2625
0.0047
31
Oxygen
0.3767
0.0015
12.0553
0.0028
0.7256
0.0015
32
Methane
0.4555
0.0018
7.3074
0.0017
1.6712
0.0035
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0215
0.0001
0.0433
0.0000
0.0425
0.0001
35
Ethane
1.7337
0.0069
52.1314
0.0120
10.0359
0.0208
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
1.5480
0.0062
68.1279
0.0157
5.6521
0.0117
38
Nitrogen
0.0074
0.0000
0.2077
0.0000
0.0176
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.1091
0.0004
6.6643
0.0015
0.4487
0.0009
42
Ammonia
244.2724
0.9757
4159.9584
0.9586
462.3567
0.9568
43
Total
250.3547
1.0000
4339.4720
1.0000
483.2129
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.1078
0.0000
0.1743
0.0000
0.0889
51
Methane
0.0000
0.0895
0.0000
0.0726
0.0000
0.1406
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0320
0.0000
0.0033
0.0000
0.0271
54
Ethane
0.0000
0.0553
0.0000
0.0841
0.0000
0.1372
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0314
0.0000
0.0697
0.0000
0.0490
57
Nitrogen
0.0000
0.0132
0.0000
0.0186
0.0000
0.0134
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.6708
0.0000
0.5774
0.0000
0.5438
62
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
63
Liquid Phase
64 65
COMPONENTS
66
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
67
CO
0.0000
0.0000
0.0011
0.0000
0.0001
68
H2O
1.8304
0.0073
32.9751
0.0076
2.2625
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.000 LIQUID VOLUME FRACTION 0.0000 0.0047
Page 249 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 85 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Oxygen
0.3767
0.0015
12.0553
0.0028
0.7256
0.0015
16
Methane
0.4555
0.0018
7.3074
0.0017
1.6712
0.0035
17
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Hydrogen
0.0215
0.0001
0.0433
0.0000
0.0425
0.0001
19
Ethane
1.7337
0.0069
52.1314
0.0120
10.0359
0.0208
20
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
CO2
1.5480
0.0062
68.1279
0.0157
5.6521
0.0117
22
Nitrogen
0.0074
0.0000
0.2077
0.0000
0.0176
0.0000
23
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
MEAmine
0.1091
0.0004
6.6643
0.0015
0.4487
0.0009
26
Ammonia
244.2724
0.9757
4159.9584
0.9586
462.3567
0.9568
27
Total
250.3547
1.0000
4339.4720
1.0000
483.2129
1.0000
28
K VALUE
29 30
COMPONENTS
MIXED
LIGHT
HEAVY
31
CO
32
H2O
33
Oxygen
71.62
71.62
---
34
Methane
49.19
49.19
---
---
---
---
35
H2S
218.0
218.0
1.068e-003
---
1.068e-003
---
36
Hydrogen
372.7
372.7
---
37
Ethane
7.990
7.990
---
38
Propane
---
---
---
39
CO2
5.071
5.071
---
40
Nitrogen
444.8
444.8
---
---
---
---
---
---
---
41
Air
42
Mercury
43
MEAmine
44
Ammonia
45
8.673e-005
0.6875
---
0.6875
---
UNIT OPERATIONS
46 47 48
8.673e-005
FEED TO
PRODUCT FROM
Mixer:
MIX-108 Tee:
49
LOGICAL CONNECTION TEE-105
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Active)
59
229.7 psia Molar:
* Mass: 250.4 lbmole/hr
4339 lb/hr Std Ideal Liq Volume:
483.2 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 250 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 86
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
132.8
132.8
(psia)
117.7*
117.7
(lbmole/hr) (lb/hr)
(Btu/hr)
1087 1.946e+004 1430 -1.112e+005 15.61 -1.209e+008 1399*
(barrel/day)
22
1087 1.946e+004 1430 -1.112e+005 15.61 -1.209e+008 1399
PROPERTIES
23 24
Overall
Aqueous Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
30
Mass Entropy
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
1.642e+004
1.642e+004
34
HHV Molar Basis (Std)
(Btu/lbmole)
3.511e+004
3.511e+004
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
8.102e-005
8.102e-005
38
CO2 App WT Con
(lbmol/lb)
1.412e-006
1.412e-006
39
LHV Mass Basis (Std)
40
(lbmole/ft3) (lb/ft3)
17.90
17.90
3.205
3.205
57.36
57.36
(barrel/day)
1450
1450
(Btu/lb)
-6213
-6213
(Btu/lb-F)
0.8721
0.8721
18.90
18.90
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.056
1.056
1962
1962
581.5
581.5
917.3
917.3
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
3.237
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
3.250
3.250
Specific Heat
(Btu/lbmole-F)
18.90
18.90
Std. Gas Flow
(MMSCFD)
9.883
9.883
Licensed to: LEGENDS
(lb/ft3)
58.17
58.17
(USGPS)
0.7049
0.7049
5.776e-003
(psia)
(Btu/lbmole)
5.776e-003
12.24
12.24
---
---
0.0000
---
1.117
1.117
1.187
1.187
1.725e+004
---
(cSt)
0.4624
0.4624
(lb/ft3)
59.44
59.44
(barrel/day)
1399
1399
1.000
1.000
(ft3/lbmole)
0.3120
0.3120
(Btu/lb)
963.9
---
0.0000
1.0000
(dyne/cm)
60.88
60.88
(Btu/hr-ft-F)
0.3561
0.3561
0.4249
0.4249
(cP)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 251 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 86 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Aqueous Phase 16.91
16.91
0.9451
0.9451
15.92
15.92
0.8895
0.8895
15.87
15.87
0.8870
0.8870
1.191
1.191
211.7
211.7
128.5
128.5
1399
1399
-10.20
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
29
CO
0.0000
0.0000
30
H2O
956.1739
0.8794
31
Oxygen
0.0114
0.0000
32
Methane
0.0001
33
H2S
34
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8852
1181.8636
0.8264
0.3640
0.0000
0.0219
0.0000
0.0000
0.0012
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0117
0.0000
0.0236
0.0000
0.0231
0.0000
35
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.0275
0.0000
1.2095
0.0001
0.1003
0.0001
38
Nitrogen
0.0199
0.0000
0.5585
0.0000
0.0474
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0029
0.0000
0.0002
0.0000
42
Ammonia
131.0322
0.1205
2231.4778
0.1147
248.0166
0.1734
43
Total
1087.2767
1.0000
19459.2060
1.0000
1430.0736
1.0000
44
0.0002
Vapour Fraction
17225.5682
Aqueous Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
48
CO
0.0000
0.0000
49
H2O
956.1739
0.8794
50
Oxygen
0.0114
0.0000
51
Methane
0.0001
52
H2S
53
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8852
1181.8636
0.8264
0.3640
0.0000
0.0219
0.0000
0.0000
0.0012
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0117
0.0000
0.0236
0.0000
0.0231
0.0000
54
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0275
0.0000
1.2095
0.0001
0.1003
0.0001
57
Nitrogen
0.0199
0.0000
0.5585
0.0000
0.0474
0.0000
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0029
0.0000
0.0002
0.0000
61
Ammonia
131.0322
0.1205
2231.4778
0.1147
248.0166
0.1734
62
Total
1087.2767
1.0000
19459.2060
1.0000
1430.0736
1.0000
63
17225.5682
K VALUE
64 65
0.0002
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
0.0000
---
0.0000
67
H2O
0.0000
---
0.0000
68
Oxygen
0.0000
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 252 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 86 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
LIGHT
HEAVY
0.0000
---
---
---
---
Hydrogen
0.0000
---
0.0000
15
Ethane
0.0000
---
0.0000
16
Propane
---
---
---
17
CO2
0.0000
---
0.0000
18
Nitrogen
0.0000
---
0.0000
---
---
---
13
H2S
14
19
Air
0.0000
20
Mercury
---
---
---
21
MEAmine
0.0000
---
0.0000
22
Ammonia
0.0000
---
0.0000
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Component Splitter:
X-102
LOGICAL CONNECTION
Pump:
P-101
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Inactive) Molar:
* 117.7 psia
1087 lbmole/hrMass:
37
1.946e+004 lb/hrStd Ideal Liq Volume:
1430 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: 87
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.7600
0.7600
0.2400
(F)
219.6*
219.6
219.6
(psia)
117.7*
117.7
117.7
178.9
136.0
42.93
3095
2332
763.4
307.3
247.6
(lbmole/hr) (lb/hr)
(Btu/hr)
-4.496e+004 34.40 -8.044e+006 302.3*
(barrel/day)
61
-2.791e+004 39.28 -3.796e+006 246.3
59.72 -9.897e+004 18.96 -4.249e+006 58.27
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.30
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
2.211e-002 0.3824 3.459e+004 -2599
17.15 1.683e-002 0.2886 3.453e+004 -1628
Aqueous Phase 17.78 2.863 50.91 64.10 -5566
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 253 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 87 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Aqueous Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
9.977e+004
1.211e+005
3.218e+004
16
HHV Molar Basis (Std)
(Btu/lbmole)
1.238e+005
1.466e+005
5.189e+004
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.989
2.291
1.066
11.81
9.312
19.73
0.6828
0.5431
1.109
7159
8548
2918
---
---
9.702
(lbmole/ft3)
---
---
1.373e-006
(lbmol/lb)
---
---
2.697e-008
(Btu/lb)
5767
7063
1809
Phase Fraction [Vol. Basis]
0.8057
0.8057
0.1943
23
Phase Fraction [Mass Basis]
0.7533
0.7533
24
Phase Fraction [Act. Vol. Basis]
0.9981
0.9981
25
Mass Exergy
110.3
---
26
Partial Pressure of CO2
27
Cost Based on Flow
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(Btu/lb) (psia)
2.377e-002
0.2467 1.853e-003 ---
---
--0.0000
(Cost/s)
0.0000
0.0000
(ACFM)
134.6
134.6
---
(lbmole/ft3)
2.489
2.348
3.073
Specific Heat
(Btu/lbmole-F)
11.81
9.312
19.73
Std. Gas Flow
(MMSCFD)
1.626
1.236
0.3902
43.05
40.26
(lb/ft3) (USGPS)
3.116e-002
(psia)
(Btu/lbmole)
54.64
---
3.116e-002 5.640e-003
---
0.9591
12.24
12.24
12.24
---
---
---
0.0000
---
---
1.202
1.271
1.112
1.177
1.333
1.112
2.449e+004
---
---
(cSt)
---
2.326
0.2245
(lb/ft3)
43.77
40.46
56.00
302.3
246.3
58.27
0.2400
0.0000
1.000
45.23
59.40
0.3493
(barrel/day) (ft3/lbmole) (Btu/lb)
1416
---
---
0.7600
0.7600
0.2400
(dyne/cm)
45.81
(Btu/hr-ft-F)
---
2.077e-002
0.3310
---
1.075e-002
0.1830
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
45.81
9.826
7.327
17.74
0.5680
0.4273
0.9977
10.04
6.984
17.74
0.5803
0.4073
0.9977
---
---
---
---
---
---
---
---
---
(psia)
211.7
211.8
210.5
(psia)
219.7
229.6
18.09
304.6
246.3
58.27
---
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0002
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
0.7600
LIQUID VOLUME FRACTION 0.0000
Page 254 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 87 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7600
LIQUID VOLUME FRACTION
15
H2O
47.8087
0.2672
861.2784
0.2783
59.0932
0.1923
16
Oxygen
0.0114
0.0001
0.3640
0.0001
0.0219
0.0001
17
Methane
0.0001
0.0000
0.0012
0.0000
0.0003
0.0000
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0117
0.0001
0.0236
0.0000
0.0231
0.0001
20
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.0275
0.0002
1.2095
0.0004
0.1003
0.0003
23
Nitrogen
0.0199
0.0001
0.5585
0.0002
0.0474
0.0002
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0029
0.0000
0.0002
0.0000
27
Ammonia
131.0322
0.7324
2231.4778
0.7210
248.0166
0.8071
28
Total
178.9115
1.0000
3094.9162
1.0000
307.3031
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7600 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
34
H2O
15.0198
0.1105
270.5830
0.1161
18.5650
0.0750
35
Oxygen
0.0114
0.0001
0.3640
0.0002
0.0219
0.0001
36
Methane
0.0001
0.0000
0.0012
0.0000
0.0003
0.0000
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0117
0.0001
0.0236
0.0000
0.0231
0.0001
39
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0275
0.0002
1.2086
0.0005
0.1003
0.0004
42
Nitrogen
0.0199
0.0001
0.5585
0.0002
0.0474
0.0002
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0028
0.0000
0.0002
0.0000
46
Ammonia
120.8910
0.8890
2058.7740
0.8830
228.8215
0.9242
47
Total
135.9814
1.0000
2331.5159
1.0000
247.5797
1.0000
48
Aqueous Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2400 LIQUID VOLUME FRACTION
52
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
H2O
32.7889
0.7638
590.6954
0.7738
40.5282
0.6786
54
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
0.0000
0.0000
0.0009
0.0000
0.0001
0.0000
61
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
65
Ammonia
10.1412
0.2362
172.7038
0.2262
19.1951
0.3214
66
Total
42.9301
1.0000
763.4003
1.0000
59.7234
1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 255 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 87 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
8990
---
8990
13
H2O
0.1446
---
0.1446
3862
---
14
Oxygen
15
Methane
16
6.526e+004
H2S
17
Hydrogen
3862
---
6.526e+004
---
---
---
8146
---
8146
18
Ethane
19
Propane
---
---
---
20
CO2
421.2
---
421.2
21
Nitrogen
8596
---
8596
---
---
---
22
2.781e+005
Air
---
2.781e+005
23
Mercury
---
---
---
24
MEAmine
6.716
---
6.716
25
Ammonia
3.763
---
3.763
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Distillation:
T-7
Component Splitter:
30
LOGICAL CONNECTION X-102
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 117.7 psia
178.9 lbmole/hrMass:
40
3095 lb/hr Std Ideal Liq Volume:
307.3 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: 88
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
13.13
13.13
(psia)
117.7*
117.7
(lbmole/hr) (lb/hr)
(Btu/hr)
908.4 1.636e+004 1123 -1.242e+005 10.47 -1.129e+008 1104*
(barrel/day)
64
908.4 1.636e+004 1123 -1.242e+005 10.47 -1.129e+008 1104
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Aqueous Phase 18.02
18.02
3.582
3.582
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 256 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 88 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Mass Heat Capacity
18
(lb/ft3)
Aqueous Phase 64.53
64.53
(barrel/day)
1084
1084
(Btu/lb)
-6896
-6896
(Btu/lb-F)
0.5811
0.5811
18.66
18.66
(Btu/lbmole-F) (Btu/lb-F)
1.036
1.036
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
19
HHV Molar Basis (Std)
(Btu/lbmole)
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
26
Phase Fraction [Mass Basis]
0.0000
1.000
27
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
28
Mass Exergy
(Btu/lb)
4.628
---
29
Partial Pressure of CO2
(psia)
0.0000
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
---
---
39
User Property
---
---
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63 64
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
18.66
18.66
Std. Gas Flow
(MMSCFD)
8.257
8.257
(lb/ft3)
62.30
62.30
(USGPS)
0.5270
0.5270
6.476e-003
(psia)
(Btu/lbmole)
6.476e-003
0.0000
---
1.119
1.119
1.118
1.118
1.603e+004
---
(cSt)
1.958
1.958
(lb/ft3)
63.35
63.35
(barrel/day)
1104
1104
1.000
1.000
(ft3/lbmole)
0.2792
0.2792
(Btu/lb)
889.6
---
0.0000
1.0000
(dyne/cm)
78.19
78.19
(Btu/hr-ft-F)
0.3193
0.3193
2.024
2.024
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
16.67
16.67
0.9254
0.9254
16.68
16.68
0.9260
0.9260
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
1104
1104
Viscosity Index
11.18
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 257 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 88 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
15
CO
0.0000
0.0000
16
H2O
908.3652
1.0000
17
Oxygen
0.0000
0.0000
18
Methane
0.0000
19
H2S
20
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1122.7705
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
908.3652
1.0000
1.0000
1122.7705
1.0000
30
0.0000
Vapour Fraction
16364.2898
16364.2898
Aqueous Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
34
CO
0.0000
0.0000
35
H2O
908.3652
1.0000
36
Oxygen
0.0000
0.0000
37
Methane
0.0000
38
H2S
39
MASS FLOW (lb/hr)
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1122.7705
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
908.3652
1.0000
1.0000
1122.7705
1.0000
49
16364.2898
16364.2898
K VALUE
50 51
0.0000
Phase Fraction
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
---
---
---
53
H2O
0.0000
---
0.0000
54
Oxygen
---
---
---
55
Methane
---
---
---
---
---
---
56
H2S
57
Hydrogen
---
---
---
58
Ethane
---
---
---
59
Propane
---
---
---
60
CO2
---
---
---
61
Nitrogen
---
---
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
---
---
---
65
Ammonia
---
---
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 258 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 88 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
LOGICAL CONNECTION
Component Splitter:
13
X-102
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 117.7 psia
908.4 lbmole/hrMass:
23
1.636e+004 lb/hrStd Ideal Liq Volume:
1123 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 89
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Liquid Phase
Vapour Phase
* 0.0000
1.0000
0.0000
(F)
76.75
76.75
76.75
(psia)
114.7*
114.7
114.7
281.9
281.9
0.0000
4853
4853
0.0000
501.4
501.4
(lbmole/hr) (lb/hr)
(Btu/hr)
-4.601e+004 18.22 -1.297e+007 496.1*
(barrel/day)
47
-4.601e+004 18.22 -1.297e+007 496.1
0.0000 -1.988e+004 36.42 0.0000 0.0000
PROPERTIES
48 49
Overall
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
(lbmole/ft3)
17.22
2.385
2.385
Vapour Phase 17.03 2.140e-002
41.06
41.06
0.3644
(barrel/day)
505.2
505.2
0.0000
Mass Enthalpy
(Btu/lb)
-2672
-2672
-1167
55
Mass Entropy
(Btu/lb-F)
1.058
1.058
2.139
56
Heat Capacity
19.31
19.31
9.159
57
Mass Heat Capacity
1.122
1.122
0.5378
58
LHV Molar Basis (Std)
(Btu/lbmole)
1.125e+005
1.125e+005
1.362e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
1.375e+005
1.375e+005
1.626e+005
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
Phase Fraction [Vol. Basis]
66
Phase Fraction [Mass Basis]
67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
Liquid Phase 17.22
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
7984
7984
9549
1.381e-006
1.381e-006
---
(lbmole/ft3)
1.034e-009
1.034e-009
---
(lbmol/lb)
2.519e-011
2.519e-011
(Btu/lb)
(Btu/lb)
6537
6537
--7996
---
1.000
---
0.0000
1.000
0.0000
0.0000
1.000
0.0000
77.63
---
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 259 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 89 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Liquid Phase
Vapour Phase
(psia)
0.0000
---
---
(Cost/s)
0.0000
0.0000
0.0000
(ACFM)
---
---
---
(lbmole/ft3)
2.403
2.403
2.259
Specific Heat
(Btu/lbmole-F)
19.31
19.31
9.159
Std. Gas Flow
(MMSCFD)
2.562
2.562
0.0000 38.46
(lb/ft3)
41.38
41.38
(USGPS)
0.2456
0.2456
---
(psia)
(Btu/lbmole)
8.354e-003
--0.9311
12.24
12.24
12.24
---
---
---
0.0000
---
---
1.115
1.115
1.277
1.115
1.115
1.386
1.284e+004
---
--1.458
(cSt)
0.2700
0.2700
(lb/ft3)
41.81
41.81
38.23
(barrel/day)
496.1
496.1
0.0000
1.000
1.000
0.0000
(ft3/lbmole)
0.4193
0.4193
46.73
(Btu/lb)
745.6
---
---
0.0000
1.0000
0.0000
(dyne/cm)
34.13
34.13
(Btu/hr-ft-F)
0.2894
0.2894
1.599e-002
0.1776
0.1776
8.509e-003
17.33
17.33
7.173
1.006
1.006
0.4212
17.33
17.33
6.610
1.006
1.006
0.3881
---
---
---
---
---
---
---
---
---
(psia)
210.4
210.4
210.5
(psia)
168.2
168.2
210.4
496.1
496.1
0.0000
-28.18
---
---
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
* 0.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
56
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
67
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
68
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 260 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 89 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
28
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
29
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
1.0000
30
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
0.0000
0.0003
0.0000
0.0003
0.0000
0.0002
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Ammonia
0.0000
0.9997
0.0000
0.9997
0.0000
0.9998
48
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
53
H2O
54
Oxygen
473.4
473.4
---
55
Methane
812.2
812.2
---
---
---
---
56
H2S
1471 1.519e-003
1471 1.519e-003
-----
57
Hydrogen
2097
2097
---
58
Ethane
304.6
304.6
---
59
Propane
---
---
---
60
CO2
22.60
22.60
---
61
Nitrogen
2083
2083
---
---
---
---
---
---
---
62
Air
63
Mercury
64
MEAmine
65
Ammonia
9.855e-004 1.212
9.855e-004 1.212
-----
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 261 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 89 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Pump:
P-102
Cooler:
LOGICAL CONNECTION E-107
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Active):
22
Flow Specification
(Inactive) Molar:
* 114.7 psia
281.9 lbmole/hrMass:
23
501.4 barrel/day
User Variables
24 25
NOTES
26 27
4853 lb/hr Std Ideal Liq Volume:
29285
28 29
(Last modified Mon Dec 17, 2018, 15:26)
30 31
Description
32 33 34
Material Stream: 90
35 36 37
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
38 39
Overall
40
Vapour / Phase Fraction
41
Temperature:
42
Pressure:
43
Molar Flow
44
Mass Flow
45
Std Ideal Liq Vol Flow
46
Molar Enthalpy
(Btu/lbmole)
47
Molar Entropy
(Btu/lbmole-F)
48
Heat Flow
49
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
77.06
77.06
(psia)
214.7*
214.7
281.9
281.9
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
4853
4853
501.4
501.4
-4.600e+004 18.22 -1.297e+007 496.1*
(barrel/day)
50
-4.600e+004 18.22 -1.297e+007 496.1
PROPERTIES
51 52
Overall
53
Molecular Weight
54
Molar Density
55
Mass Density
56
Act. Volume Flow
57
Liquid Phase 17.22
17.22
2.385
2.385
41.07
41.07
(barrel/day)
505.1
505.1
Mass Enthalpy
(Btu/lb)
-2672
-2672
58
Mass Entropy
(Btu/lb-F)
1.058
1.058
59
Heat Capacity
19.30
19.30
60
Mass Heat Capacity
61
LHV Molar Basis (Std)
(Btu/lbmole)
1.125e+005
1.125e+005
62
HHV Molar Basis (Std)
(Btu/lbmole)
1.375e+005
1.375e+005
63
HHV Mass Basis (Std)
64
CO2 Loading
65
CO2 App ML Con
66
CO2 App WT Con
67
LHV Mass Basis (Std)
68
Phase Fraction [Vol. Basis]
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.121
7984
1.121
7984
1.381e-006
1.381e-006
(lbmole/ft3)
1.034e-009
1.034e-009
(lbmol/lb)
2.519e-011
2.519e-011
(Btu/lb)
6537
6537
0.0000
1.000
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 262 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 90 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Liquid Phase
12
Phase Fraction [Mass Basis]
0.0000
1.000
13
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
14
Mass Exergy
(Btu/lb)
78.12
---
15
Partial Pressure of CO2
(psia)
0.0000
---
16
Cost Based on Flow
(Cost/s)
0.0000
0.0000
17
Act. Gas Flow
18
Avg. Liq. Density
19 20 21
Std. Ideal Liq. Mass Density
22
Act. Liq. Flow
23
Z Factor
24
Watson K
25
User Property
26
Partial Pressure of H2S
27
Cp/(Cp - R)
28
Cp/Cv
29
Heat of Vap.
30
Kinematic Viscosity
31
Liq. Mass Density (Std. Cond)
32
Liq. Vol. Flow (Std. Cond)
33
Liquid Fraction
34
Molar Volume
35
Mass Heat of Vap.
36
Phase Fraction [Molar Basis]
37
Surface Tension
38
Thermal Conductivity
39
Viscosity
40
Cv (Semi-Ideal)
41
Mass Cv (Semi-Ideal)
42
Cv
43
Mass Cv
44
Cv (Ent. Method)
45
Mass Cv (Ent. Method)
46
Cp/Cv (Ent. Method)
47
Reid VP at 37.8 C
(psia)
48
True VP at 37.8 C
(psia)
49 50
(ACFM)
---
---
(lbmole/ft3)
2.403
2.403
Specific Heat
(Btu/lbmole-F)
19.30
19.30
Std. Gas Flow
(MMSCFD)
2.562
2.562
(lb/ft3)
41.38
41.38
(USGPS)
0.2455
0.2455
1.563e-002
(psia)
(Btu/lbmole)
1.563e-002
12.24
12.24
---
---
0.0000
---
1.115
1.115
1.732
1.732
1.227e+004
---
(cSt)
0.2695
0.2695
(lb/ft3)
41.81
41.81
496.1
496.1
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4192
0.4192
712.8
---
0.0000
1.0000
(dyne/cm)
34.09
34.09
(Btu/hr-ft-F)
0.2892
0.2892
0.1773
0.1773
17.31
17.31
1.006
1.006
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
11.14
11.14
0.6471
0.6471
11.78
11.78
0.6844
0.6844
1.638
1.638
210.4
210.4
168.2
168.2
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
496.1
496.1
Viscosity Index
-28.28
---
(Btu/lb-F)
51
COMPOSITION
52 53
Overall Phase
54 55
COMPONENTS
56
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
57
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
59
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 263 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 90 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
16
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
17
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
1.0000
18
Liquid Phase
19 20
COMPONENTS
MOLAR FLOW (lbmole/hr)
21
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
22
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
24
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
35
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
36
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
1.0000
37
K VALUE
38 39
COMPONENTS
MIXED
LIGHT
HEAVY
40
CO
0.0000
0.0000
---
41
H2O
0.0000
0.0000
---
42
Oxygen
0.0000
0.0000
---
43
Methane
0.0000
0.0000
---
---
---
---
44
H2S
45
Hydrogen
0.0000
0.0000
---
46
Ethane
0.0000
0.0000
---
47
Propane
---
---
---
48
CO2
0.0000
0.0000
---
49
Nitrogen
0.0000
0.0000
---
---
---
---
50
Air
51
Mercury
---
---
---
52
MEAmine
0.0000
0.0000
---
53
Ammonia
0.0000
0.0000
---
54
UNIT OPERATIONS
55 56 57
FEED TO
PRODUCT FROM
Recycle:
RCY-3
58
Pump:
LOGICAL CONNECTION P-102
UTILITIES
59 60
( No utilities reference this stream )
61
PROCESS UTILITY
62 63 64
DYNAMICS
65 66
Pressure Specification
(Active):
67
Flow Specification
(Inactive) Molar:
* 214.7 psia
281.9 lbmole/hrMass:
4853 lb/hr Std Ideal Liq Volume:
501.4 barrel/day
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 264 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 90 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
User Variables
10 11
NOTES
12 13 14
Description
15 16 17
Material Stream: 91
18 19 20
CONDITIONS
21 22
Overall
23
Vapour / Phase Fraction
24
Temperature:
25
Pressure:
26
Molar Flow
27
Mass Flow
28
Std Ideal Liq Vol Flow
29
Molar Enthalpy
(Btu/lbmole)
30
Molar Entropy
(Btu/lbmole-F)
31
Heat Flow
32
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
77.06*
77.06
(psia)
214.7*
214.7
281.9*
281.9
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
4853
4853
501.4
501.4
-4.600e+004 18.22 -1.297e+007 496.1*
(barrel/day)
33
-4.600e+004 18.22 -1.297e+007 496.1
PROPERTIES
34 35
Overall
36
Molecular Weight
37
Molar Density
38
Mass Density
39
Act. Volume Flow
40
Liquid Phase 17.22
17.22
2.385
2.385
41.07
41.07
(barrel/day)
505.1
505.1
Mass Enthalpy
(Btu/lb)
-2672
-2672
41
Mass Entropy
(Btu/lb-F)
1.058
1.058
42
Heat Capacity
19.30
19.30
43
Mass Heat Capacity
44
LHV Molar Basis (Std)
(Btu/lbmole)
1.125e+005
1.125e+005
45
HHV Molar Basis (Std)
(Btu/lbmole)
1.375e+005
1.375e+005
46
HHV Mass Basis (Std)
47
CO2 Loading
48
CO2 App ML Con
49
CO2 App WT Con
50
LHV Mass Basis (Std)
51
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.121
7984
1.121
7984
1.381e-006
1.381e-006
(lbmole/ft3)
1.034e-009
1.034e-009
(lbmol/lb)
2.519e-011
2.519e-011
(Btu/lb)
6537
6537
Phase Fraction [Vol. Basis]
0.0000
1.000
52
Phase Fraction [Mass Basis]
0.0000
1.000
53
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
54
Mass Exergy
(Btu/lb)
78.12
---
55
Partial Pressure of CO2
(psia)
0.0000
---
56
Cost Based on Flow
(Cost/s)
0.0000
0.0000
57
Act. Gas Flow
58
Avg. Liq. Density
59 60 61
Std. Ideal Liq. Mass Density
62
Act. Liq. Flow
63
Z Factor
64
Watson K
65
User Property
66
Partial Pressure of H2S
67
(ACFM)
---
---
(lbmole/ft3)
2.403
2.403
Specific Heat
(Btu/lbmole-F)
19.30
19.30
Std. Gas Flow
(MMSCFD)
2.562
2.562
(lb/ft3)
41.38
41.38
(USGPS)
0.2455
0.2455
1.563e-002
12.24
---
---
0.0000
---
Cp/(Cp - R)
1.115
1.115
68
Cp/Cv
1.732
1.732
69
Aspen Technology Inc. Licensed to: LEGENDS
(psia)
1.563e-002
12.24
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 265 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 91 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Heat of Vap.
13
Kinematic Viscosity
14
Liq. Mass Density (Std. Cond)
15
Liq. Vol. Flow (Std. Cond)
16
Liquid Fraction
17
Molar Volume
18
Mass Heat of Vap.
19
Phase Fraction [Molar Basis]
20
Surface Tension
21
Thermal Conductivity
22
Viscosity
23
Cv (Semi-Ideal)
24
Mass Cv (Semi-Ideal)
25
Cv
26
Mass Cv
27
Cv (Ent. Method)
28
Mass Cv (Ent. Method)
29
Cp/Cv (Ent. Method)
30
Reid VP at 37.8 C
(psia)
31
True VP at 37.8 C
(psia)
32 33
(Btu/lbmole)
Liquid Phase
1.227e+004
---
(cSt)
0.2695
0.2695
(lb/ft3)
41.81
41.81
496.1
496.1
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4192
0.4192
712.8
---
0.0000
1.0000
(dyne/cm)
34.09
34.09
(Btu/hr-ft-F)
0.2892
0.2892
0.1773
0.1773
17.31
17.31
1.006
1.006
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
11.14
11.14
0.6471
0.6471
11.78
11.78
0.6843
0.6843
1.638
1.638
210.4
210.4
168.2
168.2
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
496.1
496.1
Viscosity Index
-28.28
---
(Btu/lb-F)
34
COMPOSITION
35 36
Overall Phase
37 38
COMPONENTS
39 40
CO
41
H2O
42
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 49.2854
* 0.1748
* 887.8813
* 0.1830
* 60.9184
* 0.1215
Oxygen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
43
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
44
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
45
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
46
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
47
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
48
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
49
Nitrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
50
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
51
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
52
MEAmine
* 0.0885
* 0.0003
* 5.4059
* 0.0011
* 0.3640
* 0.0007
53
Ammonia
* 232.5108
* 0.8248
* 3959.6584
* 0.8159
* 440.0945
* 0.8778
54
Total
281.8847
1.0000
4852.9456
1.0000
501.3769
1.0000
55
Liquid Phase
56 57
COMPONENTS
58
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
59
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
H2O
49.2854
0.1748
887.8813
0.1830
60.9184
0.1215
61
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 266 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 91 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase (continued)
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
18
Ammonia
232.5108
0.8248
3959.6584
0.8159
440.0945
0.8778
19
Total
281.8847
1.0000
4852.9456
1.0000
501.3769
1.0000
20
K VALUE
21 22
COMPONENTS
MIXED
LIGHT
HEAVY
23
CO
0.0000
0.0000
---
24
H2O
0.0000
0.0000
---
25
Oxygen
0.0000
0.0000
---
26
Methane
0.0000
0.0000
---
---
---
---
27
H2S
28
Hydrogen
0.0000
0.0000
---
29
Ethane
0.0000
0.0000
---
30
Propane
---
---
---
31
CO2
0.0000
0.0000
---
32
Nitrogen
0.0000
0.0000
---
---
---
---
33
Air
34
Mercury
---
---
---
35
MEAmine
0.0000
0.0000
---
36
Ammonia
0.0000
0.0000
---
37
UNIT OPERATIONS
38 39
FEED TO
PRODUCT FROM
40
Recycle:
LOGICAL CONNECTION RCY-3
41
UTILITIES
42 43
( No utilities reference this stream )
44
PROCESS UTILITY
45 46 47
DYNAMICS
48 49
Pressure Specification
(Inactive):
50
Flow Specification
(Inactive) Molar:
* 214.7 psia * Mass: 281.9 lbmole/hr
51
4853 lb/hr Std Ideal Liq Volume:
501.4 barrel/day
User Variables
52 53
NOTES
54 55 56
Description
57 58 59
Material Stream: 92
60 61 62
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
63 64
Overall
65
Vapour / Phase Fraction
66
Temperature:
67
Pressure:
68
Molar Flow
69
Aspen Technology Inc. Licensed to: LEGENDS
Aqueous Phase 0.0000
1.0000
(F)
310.0
310.0
(psia)
364.7
364.7
479.6
479.6
(lbmole/hr)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 267 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 92 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Mass Flow
13
Std Ideal Liq Vol Flow
14
Molar Enthalpy
(Btu/lbmole)
15
Molar Entropy
(Btu/lbmole-F)
16
Heat Flow
17
Liq Vol Flow @Std Cond
(lb/hr) (barrel/day)
(Btu/hr)
Aqueous Phase 8640
8640
592.8
592.8
-1.186e+005 19.63 -5.689e+007 583.0*
(barrel/day)
18
-1.186e+005 19.63 -5.689e+007 583.0
PROPERTIES
19 20
Overall
21
Molecular Weight
22
Molar Density
23
Mass Density
24
Act. Volume Flow
25
Aqueous Phase 18.02
18.02
3.122
3.122
56.24
56.24
(barrel/day)
656.7
656.7
Mass Enthalpy
(Btu/lb)
-6585
-6585
26
Mass Entropy
(Btu/lb-F)
1.089
1.089
27
Heat Capacity
19.72
19.72
28
Mass Heat Capacity
29
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
1.095
1.095
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
30
HHV Molar Basis (Std)
(Btu/lbmole)
31
HHV Mass Basis (Std)
32
CO2 Loading
33
CO2 App ML Con
34
CO2 App WT Con
35
LHV Mass Basis (Std)
36
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
37
Phase Fraction [Mass Basis]
0.0000
1.000
38
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
39
Mass Exergy
(Btu/lb)
43.03
---
40
Partial Pressure of CO2
(psia)
0.0000
---
41
Cost Based on Flow
(Cost/s)
0.0000
0.0000
42
Act. Gas Flow
43
Avg. Liq. Density
44 45 46
Std. Ideal Liq. Mass Density
47
Act. Liq. Flow
48
Z Factor
49
Watson K
---
---
50
User Property
---
---
51
Partial Pressure of H2S
52
Cp/(Cp - R)
53
Cp/Cv
54
Heat of Vap.
55
Kinematic Viscosity
56
Liq. Mass Density (Std. Cond)
57
Liq. Vol. Flow (Std. Cond)
58
Liquid Fraction
59
Molar Volume
60
Mass Heat of Vap.
61
Phase Fraction [Molar Basis]
62
Surface Tension
63
Thermal Conductivity
64
Viscosity
65
Cv (Semi-Ideal)
66
Mass Cv (Semi-Ideal)
67
Cv
68
Mass Cv
69
Fluid Package:
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.72
19.72
Std. Gas Flow
(MMSCFD)
4.360
4.360
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
62.30
62.30
(USGPS)
0.3192
0.3192
1.414e-002
(psia)
(Btu/lbmole)
1.414e-002
0.0000
---
1.112
1.112
1.188
1.188
1.445e+004
---
(cSt)
0.1949
0.1949
(lb/ft3)
63.35
63.35
583.0
583.0
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.3203
0.3203
802.3
---
0.0000
1.0000
(dyne/cm)
47.75
47.75
(Btu/hr-ft-F)
0.3962
0.3962
0.1755
0.1755
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
17.73
17.73
0.9844
0.9844
16.60
16.60
0.9216
0.9216
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 268 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 92 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Ent. Method)
13
Mass Cv (Ent. Method)
14
Cp/Cv (Ent. Method)
15
Reid VP at 37.8 C
16
True VP at 37.8 C
17
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
18
Viscosity Index
(Btu/lbmole-F)
Aqueous Phase ---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
583.0
583.0
---
---
(Btu/lb-F)
19
COMPOSITION
20 21
Overall Phase
22 23
COMPONENTS
24
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
25
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
H2O
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
27
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Total
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
40
Aqueous Phase
41 42
COMPONENTS
43
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
44
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
H2O
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
46
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Total
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
59
K VALUE
60 61
COMPONENTS
MIXED
LIGHT
HEAVY
62
CO
---
---
---
63
H2O
0.0000
---
0.0000
64
Oxygen
---
---
---
65
Methane
---
---
---
---
---
-----
66
H2S
67
Hydrogen
---
---
68
Ethane
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 269 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 92 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
Propane
---
---
---
13
CO2
---
---
---
14
Nitrogen
---
---
---
---
---
---
15
Air
16
Mercury
---
---
---
17
MEAmine
---
---
---
18
Ammonia
---
---
---
19
UNIT OPERATIONS
20 21 22
FEED TO
PRODUCT FROM
Component Splitter:
D-4A
Tee:
LOGICAL CONNECTION TEE-106
23
UTILITIES
24 25
( No utilities reference this stream )
26
PROCESS UTILITY
27 28 29
DYNAMICS
30 31
Pressure Specification
(Inactive):
32
Flow Specification
(Inactive) Molar:
364.7 psia 479.6 lbmole/hrMass:
33
8640 lb/hr Std Ideal Liq Volume:
592.8 barrel/day
User Variables
34 35
NOTES
36 37 38
Description
39 40 41
Material Stream: 93
42 43 44
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
45 46
Overall
47
Vapour / Phase Fraction
48
Temperature:
49
Pressure:
50
Molar Flow
51
Mass Flow
52
Std Ideal Liq Vol Flow
53
Molar Enthalpy
(Btu/lbmole)
54
Molar Entropy
(Btu/lbmole-F)
55
Heat Flow
56
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
310.0
310.0
(psia)
364.7
364.7
479.6
479.6
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
8640*
8640
592.8
592.8
-1.186e+005 19.63 -5.689e+007 583.0*
(barrel/day)
57
-1.186e+005 19.63 -5.689e+007 583.0
PROPERTIES
58 59
Overall
60
Molecular Weight
61
Molar Density
62
Mass Density
63
Act. Volume Flow
64
Aqueous Phase 18.02
18.02
3.122
3.122
56.24
56.24
(barrel/day)
656.7
656.7
Mass Enthalpy
(Btu/lb)
-6585
-6585
65
Mass Entropy
(Btu/lb-F)
1.089
1.089
66
Heat Capacity
19.72
19.72
67
Mass Heat Capacity
68
LHV Molar Basis (Std)
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
1.095
1.095
(Btu/lbmole)
0.0000
0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 270 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 93 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
HHV Molar Basis (Std)
13
HHV Mass Basis (Std)
14
CO2 Loading
15
CO2 App ML Con
16
CO2 App WT Con
17
LHV Mass Basis (Std)
18
(Btu/lbmole) (Btu/lb)
Aqueous Phase
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
19
Phase Fraction [Mass Basis]
0.0000
1.000
20
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
21
Mass Exergy
(Btu/lb)
43.03
---
22
Partial Pressure of CO2
(psia)
0.0000
---
23
Cost Based on Flow
(Cost/s)
0.0000
0.0000
24
Act. Gas Flow
25
Avg. Liq. Density
26 27 28
Std. Ideal Liq. Mass Density
29
Act. Liq. Flow
30
Z Factor
31
Watson K
---
---
32
User Property
---
---
33
Partial Pressure of H2S
34
Cp/(Cp - R)
35
Cp/Cv
36
Heat of Vap.
37
Kinematic Viscosity
38
Liq. Mass Density (Std. Cond)
39
Liq. Vol. Flow (Std. Cond)
40
Liquid Fraction
41
Molar Volume
42
Mass Heat of Vap.
43
Phase Fraction [Molar Basis]
44
Surface Tension
45
Thermal Conductivity
46
Viscosity
47
Cv (Semi-Ideal)
48
Mass Cv (Semi-Ideal)
49
Cv
50
Mass Cv
51
Cv (Ent. Method)
52
Mass Cv (Ent. Method)
53
Cp/Cv (Ent. Method)
54
Reid VP at 37.8 C
55
True VP at 37.8 C
56
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
57
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.72
19.72
Std. Gas Flow
(MMSCFD)
4.360
4.360
(lb/ft3)
62.30
62.30
(USGPS)
0.3192
0.3192
1.414e-002
(psia)
(Btu/lbmole)
1.414e-002
0.0000
---
1.112
1.112
1.188
1.188
1.445e+004
---
(cSt)
0.1949
0.1949
(lb/ft3)
63.35
63.35
583.0
583.0
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.3203
0.3203
802.3
---
0.0000
1.0000
(dyne/cm)
47.75
47.75
(Btu/hr-ft-F)
0.3962
0.3962
0.1755
0.1755
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
17.73
17.73
0.9844
0.9844
16.60
16.60
0.9216
0.9216
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
583.0
583.0
---
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
58
COMPOSITION
59 60
Overall Phase
61 62
COMPONENTS
63
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
64
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
H2O
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
66
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 271 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 93 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Total
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
25
Aqueous Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
H2O
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
479.5977
1.0000
8640.0000
1.0000
592.7991
1.0000
44
K VALUE
45 46
COMPONENTS
MIXED
LIGHT
HEAVY
47
CO
---
---
---
48
H2O
0.0000
---
0.0000
49
Oxygen
---
---
---
50
Methane
---
---
---
---
---
---
51
H2S
52
Hydrogen
---
---
---
53
Ethane
---
---
---
54
Propane
---
---
---
55
CO2
---
---
---
56
Nitrogen
---
---
---
---
---
---
57
Air
58
Mercury
---
---
---
59
MEAmine
---
---
---
60
Ammonia
---
---
---
61
UNIT OPERATIONS
62 63 64
FEED TO Component Splitter:
65
PRODUCT FROM D-4B
Tee:
LOGICAL CONNECTION TEE-106
UTILITIES
66 67
( No utilities reference this stream )
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 272 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 93 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROCESS UTILITY
10 11 12
DYNAMICS
13 14
Pressure Specification
(Inactive):
15
Flow Specification
(Active)
364.7 psia Molar:
* Std Ideal Liq Volume: 8640 lb/hr
479.6 lbmole/hrMass:
16
592.8 barrel/day
User Variables
17 18
NOTES
19 20 21
Description
22 23 24
Material Stream: 1000
25 26 27
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
28 29
Overall
30
Vapour / Phase Fraction
31
Temperature:
32
Pressure:
33
Molar Flow
34
Mass Flow
35
Std Ideal Liq Vol Flow
(barrel/day)
36
Molar Enthalpy
(Btu/lbmole)
37
Molar Entropy
(Btu/lbmole-F)
38
Heat Flow
39
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
Liquid Phase
0.0003
0.0003
0.9789
0.0208
(F)
-289.4
-289.4
-289.4
-289.4
(psia)
114.7
114.7
114.7
114.7
97.89
2.079
1702
57.79
(lbmole/hr)
100.0
(lb/hr)
(Btu/hr)
1760 197.7 -3.735e+004 -0.8232 -3.735e+006 196.4*
(barrel/day)
40
2.995e-002 0.1299 5.997e-002 -2698 18.74 -80.83 48.51
187.6 -3.731e+004 -1.142 -3.653e+006 187.8
10.04 -3.973e+004 13.91 -8.262e+004 3346
PROPERTIES
41 42
Overall
43
Molecular Weight
44
Molar Density
45
Mass Density
46
Act. Volume Flow
47
Vapour Phase 17.60
(lbmole/ft3)
6.426e-002
Liquid Phase
Liquid Phase
17.39
27.79
2.996
1.514
51.00
0.2787
52.10
42.07
(barrel/day)
147.5
1.993
139.7
5.872
Mass Enthalpy
(Btu/lb)
-2122
-622.2
-2146
48
Mass Entropy
(Btu/lb-F)
49
Heat Capacity
50
Mass Heat Capacity
51
LHV Molar Basis (Std)
(Btu/lbmole)
1.415e+005
9.715e+004
1.344e+005
4.727e+005
52
HHV Molar Basis (Std)
(Btu/lbmole)
1.679e+005
1.135e+005
1.605e+005
5.144e+005
53
HHV Mass Basis (Std)
54
CO2 Loading
55
CO2 App ML Con
56
CO2 App WT Con
57
LHV Mass Basis (Std)
58
Phase Fraction [Vol. Basis]
59
Phase Fraction [Mass Basis]
60
Phase Fraction [Act. Vol. Basis]
61
Mass Exergy
62
Partial Pressure of CO2
63
Cost Based on Flow
64
Act. Gas Flow
65
Avg. Liq. Density
66
Specific Heat
(Btu/lbmole-F)
18.78
67
Std. Gas Flow
(MMSCFD)
0.9090
68
Std. Ideal Liq. Mass Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lb/ft3)
2.898
4.337
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
-4.677e-002
4.321
-6.569e-002
-1430 0.5007
18.78
6.926
18.89
13.94
1.067
1.597
1.086
0.5015
9538
2.617e+004
9232
1.851e+004
9.966e+008
---
9.956e+008
9.532e+011
(lbmole/ft3)
3.716e-002
---
3.921e-002
1.006e-003
(lbmol/lb)
7.286e-004
---
7.526e-004
(Btu/lb)
(Btu/lb) (psia) (Cost/s) (ACFM) (lbmole/ft3)
(lb/ft3)
8037
2.392e-005
2.240e+004
7732
1.701e+004
3.033e-004
3.033e-004
0.9489
5.077e-002
7.380e-005
7.380e-005
0.9671
3.283e-002
1.351e-002
1.351e-002
0.9467
3.980e-002
397.7 7.982e-006 0.0000 7.769e-003 2.162
38.06
---
---
---
---
---
0.0000
0.0000
0.0000
7.769e-003 2.135 6.926 2.723e-004 9.260
---
---
---
2.231
0.8856
18.89 0.8898 38.79
Aspen HYSYS Version 8.8 (34.0.0.8909)
13.94 1.890e-002 24.61
Page 273 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1000 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Act. Liq. Flow
13
Z Factor
14
Watson K
15
User Property
16
Partial Pressure of H2S
17
Cp/(Cp - R)
18
Cp/Cv
19
Heat of Vap.
20
Kinematic Viscosity
21
Liq. Mass Density (Std. Cond)
22
Liq. Vol. Flow (Std. Cond)
23
Liquid Fraction
24
Molar Volume
25
Mass Heat of Vap.
26
Phase Fraction [Molar Basis]
27
Surface Tension
28
Thermal Conductivity
29
Viscosity
30
Cv (Semi-Ideal)
31
Mass Cv (Semi-Ideal)
32
Cv
33
Mass Cv
34
Cv (Ent. Method)
35
Mass Cv (Ent. Method)
36
Cp/Cv (Ent. Method)
37
Reid VP at 37.8 C
38
True VP at 37.8 C
39 40
(USGPS)
Vapour Phase
7.074e-002
(psia)
(Btu/lbmole)
Liquid Phase
6.789e-002
2.854e-003
---
0.9771
2.096e-002
4.148e-002
12.30
24.03
12.12
16.79
---
---
---
---
0.0000
---
---
---
1.118
1.402
1.117
1.166
1.000
1.462
1.000
1.357
---
---
---
0.8471
12.41
0.9411
1.808e+004
(cSt)
---
(lb/ft3)
38.32
(barrel/day)
Liquid Phase
---
1.145e-002
38.75
7.384e-002
196.4
48.51
187.8
3346
0.9997
0.0000
1.000
1.000
(ft3/lbmole)
0.3451
15.56
0.3337
0.6606
(Btu/lb)
1027
---
---
---
0.0003
0.0003
0.9789
0.0208
(dyne/cm)
---
73.26
27.79
(Btu/hr-ft-F)
---
3.351e-002
0.5407
0.1267
---
3.781e-003
(cP)
---
10.36
0.6342
16.79
4.941
16.90
---
0.9541
1.139
0.9719
---
18.78
4.738
18.89
---
1.067
1.092
1.086
---
---
---
17.04
---
---
---
0.9798
---
---
---
1.109
---
(psia)
259.4
---
223.8
---
(psia)
383.4
---
232.8
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
236.3
48.51
187.8
0.0000
Viscosity Index
24.35
---
---
---
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
41
COMPOSITION
42 43
Overall Phase
44 45
COMPONENTS
46
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0003
LIQUID VOLUME FRACTION
47
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
48
H2O
0.0073
0.0001
0.1314
0.0001
0.0090
0.0000
49
Oxygen
0.3167
0.0032
10.1331
0.0058
0.6099
0.0031
50
Methane
0.3692
0.0037
5.9229
0.0034
1.3546
0.0069
51
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
Hydrogen
0.0290
0.0003
0.0585
0.0000
0.0574
0.0003
53
Ethane
1.4056
0.0141
42.2649
0.0240
8.1365
0.0412
54
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
CO2
1.2825
0.0128
56.4434
0.0321
4.6828
0.0237
56
Nitrogen
0.0259
0.0003
0.7247
0.0004
0.0615
0.0003
57
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Ammonia
96.5630
0.9656
1644.4678
0.9343
182.7736
0.9246
61
Total
99.9992
1.0000
1760.1478
1.0000
197.6853
1.0000
62
Vapour Phase
63 64
COMPONENTS
65
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
2.995e-004 LIQUID VOLUME FRACTION
66
CO
0.0000
0.0000
0.0000
0.0002
0.0000
0.0000
67
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Oxygen
0.0011
0.0370
0.0355
0.2731
0.0021
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0356
Page 274 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1000 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
2.995e-004 LIQUID VOLUME FRACTION
15
Methane
0.0002
0.0061
0.0030
0.0227
0.0007
0.0113
16
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Hydrogen
0.0274
0.9136
0.0552
0.4247
0.0541
0.9017
18
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Nitrogen
0.0013
0.0432
0.0363
0.2793
0.0031
0.0514
22
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Total
0.0300
1.0000
0.1299
1.0000
0.0600
1.0000
27
Liquid Phase
28 29
COMPONENTS
30
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.9789 LIQUID VOLUME FRACTION
31
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
H2O
0.0073
0.0001
0.1314
0.0001
0.0090
0.0000
33
Oxygen
0.0296
0.0003
0.9487
0.0006
0.0571
0.0003
34
Methane
0.0052
0.0001
0.0833
0.0000
0.0191
0.0001
35
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Ethane
0.0117
0.0001
0.3518
0.0002
0.0677
0.0004
38
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
CO2
1.2811
0.0131
56.3825
0.0331
4.6777
0.0249
40
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Ammonia
96.5547
0.9864
1644.3272
0.9660
182.7580
0.9742
45
Total
97.8897
1.0000
1702.2250
1.0000
187.5886
1.0000
46
Liquid Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
2.079e-002 LIQUID VOLUME FRACTION
50
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
51
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
Oxygen
0.2859
0.1375
9.1489
0.1583
0.5506
0.0549
53
Methane
0.3638
0.1750
5.8366
0.1010
1.3349
0.1330
54
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Hydrogen
0.0017
0.0008
0.0033
0.0001
0.0033
0.0003
56
Ethane
1.3939
0.6703
41.9131
0.7252
8.0687
0.8039
57
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
CO2
0.0014
0.0007
0.0608
0.0011
0.0050
0.0005
59
Nitrogen
0.0246
0.0118
0.6884
0.0119
0.0585
0.0058
60
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Ammonia
0.0083
0.0040
0.1406
0.0024
0.0156
0.0016
64
Total
2.0795
1.0000
57.7928
1.0000
10.0367
1.0000
65
K VALUE
66 67
COMPONENTS
68 69
MIXED CO
Aspen Technology Inc. Licensed to: LEGENDS
LIGHT 70.80
Aspen HYSYS Version 8.8 (34.0.0.8909)
HEAVY 2.002e+004
1.478
Page 275 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1000 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
H2O
13
Oxygen
11.73
122.2
14
Methane
1.664
115.8
15
4.996e-027
H2S
16
4.892e-027
---
0.2692 3.510e-002
---
---
Hydrogen
5.480e+004
7.090e+006
17
Ethane
3.473e-004
4.085e-002
18
Propane
19
CO2
20
Nitrogen
21
---
1149 7.284e-006
---
5.425e-006
---
5.317e-006
175.9
Air
1.518e-004
1.047e-004
1.182e+007
---
---
---
---
3.659 ---
22
Mercury
23
MEAmine
2.394e-033
2.344e-033
4.419e-029
24
Ammonia
1.067e-010
1.045e-010
2.596e-008
25
---
UNIT OPERATIONS
26 27
FEED TO
PRODUCT FROM
28
Distillation:
LOGICAL CONNECTION T-7
29
UTILITIES
30 31
( No utilities reference this stream )
32
PROCESS UTILITY
33 34 35
DYNAMICS
36 37
Pressure Specification
(Inactive):
38
Flow Specification
(Inactive) Molar:
114.7 psia 100.0 lbmole/hrMass:
39
1760 lb/hr Std Ideal Liq Volume:
197.7 barrel/day
User Variables
40 41
NOTES
42 43 44
Description
45 46 47
Material Stream: 1001
48 49 50
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
51 52
Overall
53
Vapour / Phase Fraction
54
Temperature:
55
Pressure:
56
Molar Flow
57
Mass Flow
58
Std Ideal Liq Vol Flow
59
Molar Enthalpy
(Btu/lbmole)
60
Molar Entropy
(Btu/lbmole-F)
61
Heat Flow
62
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
76.75
76.75
(psia)
114.7
114.7
281.9
281.9
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
4853
4853
501.4
501.4
-4.601e+004 18.22 -1.297e+007 496.1*
(barrel/day)
63
-4.601e+004 18.22 -1.297e+007 496.1
PROPERTIES
64 65
Overall
66
Molecular Weight
67
Molar Density
68
Mass Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
Liquid Phase 17.22
17.22
2.385
2.385
41.06
41.06
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 276 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1001 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Act. Volume Flow
13
Liquid Phase
(barrel/day)
505.2
505.2
Mass Enthalpy
(Btu/lb)
-2672
-2672
14
Mass Entropy
(Btu/lb-F)
1.058
1.058
15
Heat Capacity
19.31
19.31
16
Mass Heat Capacity
17
LHV Molar Basis (Std)
(Btu/lbmole)
1.125e+005
1.125e+005
18
HHV Molar Basis (Std)
(Btu/lbmole)
1.375e+005
1.375e+005
19
HHV Mass Basis (Std)
20
CO2 Loading
21
CO2 App ML Con
22
CO2 App WT Con
23
LHV Mass Basis (Std)
24
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
1.122
7984
1.122
7984
1.381e-006
1.381e-006
(lbmole/ft3)
1.034e-009
1.034e-009
(lbmol/lb)
2.519e-011
2.519e-011
(Btu/lb)
6537
6537
Phase Fraction [Vol. Basis]
0.0000
1.000
25
Phase Fraction [Mass Basis]
0.0000
1.000
26
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
27
Mass Exergy
(Btu/lb)
77.63
---
28
Partial Pressure of CO2
(psia)
0.0000
---
29
Cost Based on Flow
(Cost/s)
0.0000
0.0000
30
Act. Gas Flow
31
Avg. Liq. Density
32 33 34
Std. Ideal Liq. Mass Density
35
Act. Liq. Flow
36
Z Factor
37
Watson K
38
User Property
39
Partial Pressure of H2S
40
Cp/(Cp - R)
41
Cp/Cv
42
Heat of Vap.
43
Kinematic Viscosity
44
Liq. Mass Density (Std. Cond)
45
Liq. Vol. Flow (Std. Cond)
46
Liquid Fraction
47
Molar Volume
48
Mass Heat of Vap.
49
Phase Fraction [Molar Basis]
50
Surface Tension
51
Thermal Conductivity
52
Viscosity
53
Cv (Semi-Ideal)
54
Mass Cv (Semi-Ideal)
55
Cv
56
Mass Cv
57
Cv (Ent. Method)
58
Mass Cv (Ent. Method)
59
Cp/Cv (Ent. Method)
60
Reid VP at 37.8 C
61
True VP at 37.8 C
62
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
63
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
2.403
2.403
Specific Heat
(Btu/lbmole-F)
19.31
19.31
Std. Gas Flow
(MMSCFD)
2.562
2.562
(lb/ft3)
41.38
41.38
(USGPS)
0.2456
0.2456
8.354e-003
(psia)
(Btu/lbmole)
8.354e-003
12.24
12.24
---
---
0.0000
---
1.115
1.115
1.115
1.115
1.284e+004
---
(cSt)
0.2700
0.2700
(lb/ft3)
41.81
41.81
496.1
496.1
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4193
0.4193
745.6
---
0.0000
1.0000
(dyne/cm)
34.13
34.13
(Btu/hr-ft-F)
0.2894
0.2894
0.1776
0.1776
17.33
17.33
1.006
1.006
17.33
17.33
1.006
1.006
---
---
---
---
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
---
(psia)
210.4
210.4
(psia)
168.2
168.2
496.1
496.1
-28.18
---
64 65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 277 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1001 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
28
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
29
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
H2O
49.2854
0.1748
887.8812
0.1830
60.9184
0.1215
36
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0885
0.0003
5.4059
0.0011
0.3640
0.0007
47
Ammonia
232.5102
0.8248
3959.6487
0.8159
440.0934
0.8778
48
Total
281.8841
1.0000
4852.9358
1.0000
501.3758
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
0.0000
0.0000
---
53
H2O
0.0000
0.0000
---
54
Oxygen
0.0000
0.0000
---
55
Methane
0.0000
0.0000
---
---
---
---
56
H2S
57
Hydrogen
0.0000
0.0000
---
58
Ethane
0.0000
0.0000
---
59
Propane
---
---
---
60
CO2
0.0000
0.0000
---
61
Nitrogen
0.0000
0.0000
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
0.0000
0.0000
---
65
Ammonia
0.0000
0.0000
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 278 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 1001 (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11 12
Fluid Package:
FEED TO
PRODUCT FROM
Cooler:
E-107
Distillation:
LOGICAL CONNECTION T-7
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
114.7 psia 281.9 lbmole/hrMass:
23
4853 lb/hr Std Ideal Liq Volume:
501.4 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: 94-
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
110.0*
110.0
(psia)
229.7*
229.7
2349*
(lbmole/hr) (lb/hr)
3.772e+004 5579 -2.337e+004 31.08
2349 3.772e+004 5579 -2.337e+004 31.08
(Btu/hr)
-5.489e+007
-5.489e+007
(barrel/day)
* 3.801e+006
3.801e+006
47
PROPERTIES
48 49
Overall
Vapour Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-1455
-1455
55
Mass Entropy
(Btu/lb-F)
1.935
1.935
56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
7.748e+004
7.748e+004
59
HHV Molar Basis (Std)
(Btu/lbmole)
8.874e+004
8.874e+004
60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66
16.06 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
0.6049 2.665e+005
16.06 3.767e-002 0.6049 2.665e+005
7.431
7.431
0.4627
0.4627
5525
5525
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
4824
4824
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
67
Phase Fraction [Act. Vol. Basis]
1.000
1.000
68
Mass Exergy
182.6
---
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
3.767e-002
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 279 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 94- (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16 17 18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
Z Factor
21
Watson K
22
User Property
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
Vapour Phase
(psia)
27.40
---
(Cost/s)
0.0000
0.0000
(ACFM)
1039
1039
(lbmole/ft3)
1.799
1.799
Specific Heat
(Btu/lbmole-F)
7.431
7.431
Std. Gas Flow
(MMSCFD)
21.35
21.35
(lb/ft3)
28.90
28.90
(USGPS)
---
---
0.9975
0.9975
10.51
10.51
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.365
1.365
1.390
1.390
5705
---
1.407
1.407
4.242e-002
4.242e-002
3.801e+006
3.801e+006
0.0000
0.0000
(ft3/lbmole)
26.55
26.55
(Btu/lb)
355.2
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
4.304e-002
4.304e-002
1.363e-002
1.363e-002
5.445
5.445
0.3391
0.3391
5.344
5.344
0.3328
0.3328
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
3.801e+006 -30.27
48
3.801e+006 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
54
CO
* 58.9761
* 0.0251
* 1651.9750
* 0.0438
* 141.5025
* 0.0254
55
H2O
* 14.4510
* 0.0062
* 260.3363
* 0.0069
* 17.8619
* 0.0032
56
Oxygen
* 134.8287
* 0.0574
* 4314.5184
* 0.1144
* 259.6752
* 0.0465
57
Methane
* 75.8667
* 0.0323
* 1217.1211
* 0.0323
* 278.3614
* 0.0499
58
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
59
Hydrogen
60
Ethane
61
Propane
62
* 0.0000
* 1234.9677
* 0.5258
* 2489.6950
* 0.0660
* 2440.2900
* 0.4374
* 32.8159
* 0.0140
* 986.7710
* 0.0262
* 189.9641
* 0.0340
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
CO2
* 280.2107
* 0.1193
* 12331.9893
* 0.3269
* 1023.1072
* 0.1834
63
Nitrogen
* 516.4873
* 0.2199
* 14468.3579
* 0.3836
* 1228.5731
* 0.2202
64
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
65
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
66
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
67
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
68
Total
69
Aspen Technology Inc. Licensed to: LEGENDS
2348.6041
1.0000
37720.7641
1.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
5579.3353
1.0000
Page 280 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 94- (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
1.000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
CO
58.9761
0.0251
1651.9750
0.0438
141.5025
0.0254
16
H2O
14.4510
0.0062
260.3363
0.0069
17.8619
0.0032
17
Oxygen
134.8287
0.0574
4314.5184
0.1144
259.6752
0.0465
18
Methane
75.8667
0.0323
1217.1211
0.0323
278.3614
0.0499
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
1234.9677
0.5258
2489.6950
0.0660
2440.2900
0.4374
21
Ethane
32.8159
0.0140
986.7710
0.0262
189.9641
0.0340
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
280.2107
0.1193
12331.9893
0.3269
1023.1072
0.1834
24
Nitrogen
516.4873
0.2199
14468.3579
0.3836
1228.5731
0.2202
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
2348.6041
1.0000
1.0000
5579.3353
1.0000
37720.7641
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Stream Cutter:
94-Cutter Recycle:
51
LOGICAL CONNECTION RCY-4
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Inactive) Molar:
61
* 229.7 psia * Mass: 2349 lbmole/hr
3.772e+004 lb/hrStd Ideal Liq Volume:
5579 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 281 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 94+
7 8 9
Fluid Package:
Basis-2
Property Package:
Acid Gas
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase
Aqueous Phase
0.9999
0.9999
0.0001
(F)
110.0
110.0
110.0
(psia)
229.7
229.7
229.7
2349
2348
0.2814
(lbmole/hr) (lb/hr)
3.772e+004
(barrel/day)
8648 -2.334e+004 -2.978
3.772e+004 8647 -2.333e+004 -2.974
(Btu/hr)
-5.483e+007
-5.479e+007
(barrel/day)
* 1.142e+004
1.142e+004
22
5.075 0.3484 -1.223e+005 -37.88 -3.442e+004 0.3481
PROPERTIES
23 24
Overall
Vapour Phase
Aqueous Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-1453
-1453
-6782
30
Mass Entropy
(Btu/lb-F)
-0.1854
-0.1852
-2.101
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
7.745e+004
7.746e+004
34
HHV Molar Basis (Std)
(Btu/lbmole)
8.871e+004
8.872e+004
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
38
CO2 App WT Con
(lbmol/lb)
39
LHV Mass Basis (Std)
(Btu/lb)
40
Phase Fraction [Vol. Basis]
1.000
1.000
4.029e-005
41
Phase Fraction [Mass Basis]
0.9999
0.9999
1.345e-004
42
Phase Fraction [Act. Vol. Basis]
1.000
1.000
1.315e-006
43
Mass Exergy
(Btu/lb)
182.8
---
44
Partial Pressure of CO2
(psia)
27.41
---
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
16.06 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
3.757e-002 0.6034 2.672e+005
16.06 3.757e-002 0.6033 2.672e+005
18.03 3.424 61.75 0.3513
7.454
7.452
18.00
0.4641
0.4640
0.9981 17.82 1.764e+004
5523
5524
---
---
977.9
---
---
2.497e-003
---
---
4.044e-005
4822
4823
---
0.9880
---
(ACFM)
1042
1042
---
(lbmole/ft3)
1.161
1.161
3.452
Specific Heat
(Btu/lbmole-F)
7.454
7.452
Std. Gas Flow
(MMSCFD)
21.35
21.35
18.65
18.64
Licensed to: LEGENDS
(lb/ft3) (USGPS)
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
1.708e-004
(Btu/lb)
1.708e-004 1.097e-002
---
1.000 15.79
9.357
---
---
---
0.0000
---
---
1.363
1.363
1.124
1.387
1.387
1.033
---
---
---
---
1.703
0.6340
14.12 1.142e+004 26.62
14.12 1.142e+004
62.32 0.3481
0.0000
1.000
26.62
0.2920
-877.1
---
---
0.9999
0.9999
0.0001
(dyne/cm)
69.12
(Btu/hr-ft-F)
---
(cP)
62.26
---
15.79
1.198e-004 (ft3/lbmole)
18.00 2.558e-003
---
---
69.12
4.864e-002
0.3388
1.646e-002
0.6271
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 282 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 94+ (continued)
7 8 9
Fluid Package:
Basis-2
Property Package:
Acid Gas
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase
Aqueous Phase
5.468
5.466
16.01
0.3404
0.3404
0.8879
5.373
5.372
17.43
0.3346
0.3345
0.9666
---
---
14.46
(Btu/lb-F)
---
---
0.8017
---
---
1.245
Reid VP at 37.8 C
(psia)
5181
5181
1958
20
True VP at 37.8 C
(psia)
---
---
220.8
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
23
pH[Ele]
24
Ionic Strength[Ele]
25
Heat Capacity[Ele]
26
pOH[Ele]
27
Osmotic Coefficient[Ele]
(lbmol/lb) (Btu/lbmole-F)
1.142e+004
1.142e+004
0.3481
---
---
---
3.872
---
3.872
2.465e-006
---
2.465e-006
7.454
7.452
9.591
---
9.591
0.9995
---
0.9995
28
18.00
COMPOSITION
29 30
Overall Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
0.9999
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
34
CO
58.9761
0.0251
1651.9455
0.0438
216.2805
0.0250
35
H2O
14.4510
0.0062
260.3389
0.0069
17.8605
0.0021
36
Oxygen
134.8287
0.0574
4314.3566
0.1144
494.4511
0.0572
37
Methane
75.8667
0.0323
1217.1105
0.0323
278.2223
0.0322
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
1234.9677
0.5258
2489.5468
0.0660
4528.9405
0.5237
40
Ethane
32.8159
0.0140
986.7624
0.0262
190.3468
0.0220
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
280.2107
0.1193
12332.0171
0.3269
1027.6039
0.1188
43
Nitrogen
516.4873
0.2199
14468.6055
0.3836
1894.0900
0.2190
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
2348.6041
1.0000
1.0000
8647.7956
1.0000
48
37720.6835
Vapour Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
0.9999
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
52
CO
58.9761
0.0251
1651.9454
0.0438
216.2805
0.0250
53
H2O
14.1698
0.0060
255.2737
0.0068
17.5130
0.0020
54
Oxygen
134.8287
0.0574
4314.3565
0.1144
494.4511
0.0572
55
Methane
75.8667
0.0323
1217.1105
0.0323
278.2223
0.0322
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
1234.9677
0.5259
2489.5467
0.0660
4528.9404
0.5237
58
Ethane
32.8159
0.0140
986.7624
0.0262
190.3468
0.0220
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
280.2105
0.1193
12332.0081
0.3270
1027.6031
0.1188
61
Nitrogen
516.4873
0.2199
14468.6053
0.3836
1894.0900
0.2190
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Total
2348.3227
1.0000
1.0000
8647.4472
1.0000
37715.6086
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 283 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: 94+ (continued)
7 8 9
Fluid Package:
Basis-2
Property Package:
Acid Gas
COMPOSITION
10 11
Aqueous Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.198e-004 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.2812
0.9991
5.0653
0.9981
0.3475
0.9973
17
Oxygen
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0001
0.0001
0.0000
0.0001
0.0003
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0002
0.0007
0.0090
0.0018
0.0008
0.0022
24
Nitrogen
0.0000
0.0000
0.0003
0.0001
0.0000
0.0001
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
0.2814
1.0000
5.0749
1.0000
0.3484
1.0000
29
K VALUE
30 31
COMPONENTS
MIXED
32
CO
33
H2O
LIGHT 4732
HEAVY ---
6.039e-003
4732
---
6.039e-003
34
Oxygen
3636
---
3636
35
Methane
3452
---
3452
---
---
---
Hydrogen
4847
---
4847
38
Ethane
3225
---
3225
39
Propane
---
---
---
40
CO2
163.6
---
163.6
41
Nitrogen
6799
---
6799
---
---
---
36
H2S
37
42
Air
43
Mercury
---
---
---
44
MEAmine
---
---
---
45
UNIT OPERATIONS
46 47 48
FEED TO
PRODUCT FROM
Absorber:
T-100
49
Stream Cutter:
LOGICAL CONNECTION 94-Cutter
UTILITIES
50 51
( No utilities reference this stream )
52
PROCESS UTILITY
53 54 55
DYNAMICS
56 57
Pressure Specification
(Inactive):
58
Flow Specification
(Inactive) Molar:
59
229.7 psia 2349 lbmole/hrMass:
3.772e+004 lb/hrStd Ideal Liq Volume:
8648 barrel/day
User Variables
60 61
NOTES
62 63 64
Description
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 284 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: a
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Aqueous Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
1.839e+005
1.839e+005
18
Molar Enthalpy
(Btu/lbmole)
-1.224e+005
-1.224e+005
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
0.0000
1.0000
(F)
110.1
110.1
(psia)
274.7*
(lbmole/hr) (lb/hr)
274.7
1.486e+005
1.486e+005
2.679e+006
2.679e+006
13.95
13.95
(Btu/hr)
-1.820e+010
-1.820e+010
(barrel/day)
* 1.807e+005
1.807e+005
22
PROPERTIES
23 24
Overall
Aqueous Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-6791
-6791
30
Mass Entropy
(Btu/lb-F)
0.7735
0.7735
31
Heat Capacity
32
Mass Heat Capacity
33
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F)
18.03
18.03
3.442
3.442
62.06 1.845e+005
62.06 1.845e+005
18.57
18.57
(Btu/lb-F)
1.030
1.030
LHV Molar Basis (Std)
(Btu/lbmole)
1.714
34
HHV Molar Basis (Std)
(Btu/lbmole)
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
(lbmole/ft3)
2.053e-003
2.053e-003
38
CO2 App WT Con
(lbmol/lb)
3.308e-005
3.308e-005
39
LHV Mass Basis (Std)
(Btu/lb)
9.508e-002
9.508e-002
40
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
1.938
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(Btu/lb)
1.762e+004 977.3 ---
1.714 1.762e+004 977.3 ---
(ACFM)
---
---
(lbmole/ft3)
3.454
3.454
Specific Heat
(Btu/lbmole-F)
18.57
18.57
Std. Gas Flow
(MMSCFD)
1351
1351
62.28
62.28
Licensed to: LEGENDS
(lb/ft3) (USGPS)
89.71 1.305e-002
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb)
89.71 1.305e-002
8.466
8.466
---
---
0.0000
---
1.120
1.120
1.157
1.157
1.579e+004 0.6154 63.37 1.807e+005
--0.6154 63.37 1.807e+005
1.000
1.000
0.2905
0.2905
875.6
---
0.0000
1.0000
(dyne/cm)
68.86
68.86
(Btu/hr-ft-F)
0.3673
0.3673
0.6118
0.6118
(cP)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 285 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: a (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Aqueous Phase
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
---
---
20
True VP at 37.8 C
(psia)
232.7
232.7
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.58
16.58
0.9196
0.9196
16.05
16.05
0.8900
0.8900
15.78
15.78
0.8753
0.8753
1.176
1.176
1.807e+005
1.807e+005
-4.392
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
30
H2O
31
Oxygen
0.6059
0.0000
19.3875
0.0000
1.1669
0.0000
32
Methane
0.0012
0.0000
0.0186
0.0000
0.0043
0.0000
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
2.2934
0.0000
4.6235
0.0000
4.5317
0.0000
35
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
88.6369
0.0006
3900.8838
0.0015
323.6317
0.0018
38
Nitrogen
5.0873
0.0000
142.5111
0.0001
12.1013
0.0001
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
0.1299 148503.7872
148600.5418
0.0000
3.6398
0.9993
2.675310649e+06
1.0000
44
2.679381713e+06
0.0000
0.3118
0.9985
1.0000
46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
0.9981
183897.5147
Aqueous Phase
45
0.0000
183555.7671
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
49
H2O
50
Oxygen
0.6059
0.0000
19.3875
0.0000
1.1669
0.0000
51
Methane
0.0012
0.0000
0.0186
0.0000
0.0043
0.0000
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
2.2934
0.0000
4.6235
0.0000
4.5317
0.0000
54
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
88.6369
0.0006
3900.8838
0.0015
323.6317
0.0018
57
Nitrogen
5.0873
0.0000
142.5111
0.0001
12.1013
0.0001
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
0.1299 148503.7872
148600.5418
0.0000 0.9993
1.0000
63
2.679381713e+06
0.0000
0.3118
0.9985
0.0000
183555.7671
1.0000
0.9981
183897.5147
1.0000
K VALUE
64 65
3.6398 2.675310649e+06
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
0.0000
---
0.0000
67
H2O
0.0000
---
0.0000
68
Oxygen
0.0000
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 286 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: a (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
LIGHT
HEAVY
0.0000
---
---
---
---
Hydrogen
0.0000
---
0.0000
15
Ethane
0.0000
---
0.0000
16
Propane
---
---
---
17
CO2
0.0000
---
0.0000
18
Nitrogen
0.0000
---
0.0000
---
---
---
13
H2S
14
19
Air
0.0000
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Recycle:
RCY-1
Pump:
LOGICAL CONNECTION P-100
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Inactive) Molar:
* 274.7 psia
1.486e+005 lbmole/hr Mass:
37
2.679e+006 lb/hrStd Ideal Liq Volume: 1.839e+005 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: ACIDO NITRICO
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
205.2
205.2
(psia)
114.7
114.7
(lbmole/hr) (lb/hr)
896.0 1.524e+004 1999 -1.660e+004 35.61
896.0 1.524e+004 1999 -1.660e+004 35.61
(Btu/hr)
-1.488e+007
-1.488e+007
(barrel/day)
* 1.449e+006
1.449e+006
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.01
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
1.613e-002 0.2744 2.374e+005 -976.3
17.01 1.613e-002 0.2744 2.374e+005 -976.3
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 287 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: ACIDO NITRICO (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
8.317e+004
8.317e+004
16
HHV Molar Basis (Std)
(Btu/lbmole)
9.616e+004
9.616e+004
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22 23
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.094
2.094
7.595
7.595
0.4466
0.4466
5654
5654
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
4890
4890
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
24
Phase Fraction [Act. Vol. Basis]
1.000
1.000
25
Mass Exergy
(Btu/lb)
138.6
---
26
Partial Pressure of CO2
(psia)
1.156
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30
(ACFM)
925.6
925.6
(lbmole/ft3)
1.916
1.916
Specific Heat
(Btu/lbmole-F)
7.595
7.595
31
Std. Gas Flow
(MMSCFD)
8.145
8.145
32
Std. Ideal Liq. Mass Density
(lb/ft3)
32.59
32.59
33
Act. Liq. Flow
(USGPS)
---
---
34
Z Factor
0.9963
0.9963
35
Watson K
9.936
9.936
36
User Property
---
---
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(psia)
(Btu/lbmole) (cSt)
0.0000
---
1.354
1.354
1.370
1.370
1.077e+004 3.502
(lb/ft3) (barrel/day)
--3.502
4.497e-002
4.497e-002
1.449e+006
1.449e+006
0.0000
0.0000
(ft3/lbmole)
61.98
61.98
(Btu/lb)
633.3
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
3.840e-002
3.840e-002
1.539e-002
1.539e-002
5.609
5.609
0.3298
0.3298
5.542
5.542
0.3259
0.3259
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.449e+006 -15.65
62
1.449e+006 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.1887
MOLE FRACTION 0.0002
MASS FLOW (lb/hr) 5.2847
Vapour Fraction MASS FRACTION 0.0003
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.4527
1.0000
LIQUID VOLUME FRACTION 0.0002
Page 288 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: ACIDO NITRICO (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
1.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
H2O
103.3251
0.1153
1861.4115
0.1221
127.7133
0.0639
16
Oxygen
130.1930
0.1453
4166.1757
0.2734
250.7470
0.1255
17
Methane
78.0631
0.0871
1252.3578
0.0822
286.4202
0.1433
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
326.8026
0.3647
658.8341
0.0432
645.7603
0.3231
20
Ethane
20.0052
0.0223
601.5541
0.0395
115.8057
0.0579
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
9.0319
0.0101
397.4930
0.0261
32.9775
0.0165
23
Nitrogen
219.0314
0.2444
6135.7258
0.4026
521.0120
0.2607
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0002
0.0000
0.0133
0.0000
0.0009
0.0000
27
Ammonia
9.3925
0.0105
159.9543
0.0105
17.7780
0.0089
28
Total
896.0336
1.0000
15238.8043
1.0000
1998.6675
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
33
CO
0.1887
0.0002
5.2847
0.0003
0.4527
0.0002
34
H2O
103.3251
0.1153
1861.4115
0.1221
127.7133
0.0639
35
Oxygen
130.1930
0.1453
4166.1757
0.2734
250.7470
0.1255
36
Methane
78.0631
0.0871
1252.3578
0.0822
286.4202
0.1433
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
326.8026
0.3647
658.8341
0.0432
645.7603
0.3231
39
Ethane
20.0052
0.0223
601.5541
0.0395
115.8057
0.0579
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
9.0319
0.0101
397.4930
0.0261
32.9775
0.0165
42
Nitrogen
219.0314
0.2444
6135.7258
0.4026
521.0120
0.2607
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0002
0.0000
0.0133
0.0000
0.0009
0.0000
46
Ammonia
9.3925
0.0105
159.9543
0.0105
17.7780
0.0089
47
Total
896.0336
1.0000
15238.8043
1.0000
1998.6675
1.0000
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
---
---
---
52
H2O
---
---
---
53
Oxygen
---
---
---
54
Methane
---
---
---
---
---
---
55
H2S
56
Hydrogen
---
---
---
57
Ethane
---
---
---
58
Propane
---
---
---
59
CO2
---
---
---
60
Nitrogen
---
---
---
---
---
---
61
Air
62
Mercury
---
---
---
63
MEAmine
---
---
---
64
Ammonia
---
---
---
65
UNIT OPERATIONS
66 67
FEED TO
68 69
PRODUCT FROM Absorber:
Aspen Technology Inc. Licensed to: LEGENDS
LOGICAL CONNECTION T-101
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 289 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: ACIDO NITRICO (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Inactive):
18
Flow Specification
(Inactive) Molar:
114.7 psia 896.0 lbmole/hrMass:
19
1.524e+004 lb/hrStd Ideal Liq Volume:
1999 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: Aire-1
28 29 30
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
Vapour Phase
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
1470
39
Molar Enthalpy
(Btu/lbmole)
1417
1417
40
Molar Entropy
(Btu/lbmole-F)
32.81
32.81
41
Heat Flow
42
Liq Vol Flow @Std Cond
1.0000
1.0000
(F)
282.0*
282.0
(psia)
254.7*
254.7
643.9*
(lbmole/hr) (lb/hr)
1.858e+004
643.9 1.858e+004 1470
(Btu/hr)
9.123e+005
9.123e+005
(barrel/day)
* 1.042e+006
1.042e+006
43
PROPERTIES
44 45
Overall
Vapour Phase
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Mass Enthalpy
(Btu/lb)
49.11
49.11
51
Mass Entropy
(Btu/lb-F)
1.137
1.137
52
Heat Capacity
53
Mass Heat Capacity
54 55 56
HHV Mass Basis (Std)
57
CO2 Loading
58
CO2 App ML Con
59
CO2 App WT Con
60
LHV Mass Basis (Std)
61 62
28.85 (lbmole/ft3) (lb/ft3) (barrel/day)
0.9211 8.620e+004
28.85 3.193e-002 0.9211 8.620e+004
7.238
7.238
(Btu/lb-F)
0.2509
0.2509
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
HHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
0.0000
0.0000
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
63
Phase Fraction [Act. Vol. Basis]
1.000
1.000
64
Mass Exergy
(Btu/lb)
112.9
---
65
Partial Pressure of CO2
(psia)
0.0000
---
66
Cost Based on Flow
(Cost/s)
0.0000
0.0000
67
Act. Gas Flow
(ACFM)
336.1
336.1
68
Avg. Liq. Density
(lbmole/ft3)
1.872
1.872
69
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lbmole-F)
3.193e-002
(Btu/lb)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 290 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Aire-1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Specific Heat
(Btu/lbmole-F)
7.238
7.238
13
Std. Gas Flow
(MMSCFD)
5.853
5.853
14
Std. Ideal Liq. Mass Density
(lb/ft3)
54.00
54.00
15
Act. Liq. Flow
(USGPS)
---
---
16
Z Factor
1.002
1.002
17
Watson K
6.042
6.042
18
User Property
---
---
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
41
True VP at 37.8 C
42
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
43
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.378
1.378
1.400
1.400
1632
---
1.627
1.627
7.622e-002
7.622e-002
1.042e+006
1.042e+006
0.0000
0.0000
(ft3/lbmole)
31.32
31.32
(Btu/lb)
56.57
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.980e-002
1.980e-002
2.400e-002
2.400e-002
5.252
5.252
0.1820
0.1820
5.169
5.169
0.1792
0.1792
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.042e+006 -24.67
44
1.042e+006 ---
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
50
CO
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
51
H2O
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
52
Oxygen
* 135.2105
* 0.2100
* 0.2329
* 260.4106
* 0.1771
53
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
54
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
55
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
56
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
57
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
58
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
59
Nitrogen
* 508.6491
* 0.7900
60
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
61
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
62
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
63
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
64
Total
643.8596
1.0000
* 4326.7368
* 14248.7881
18575.5250
* 0.7671
1.0000
* 1209.9284
1470.3390
* 0.8229
1.0000
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 291 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Aire-1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
135.2105
0.2100
4326.7368
0.2329
260.4106
0.1771
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
508.6491
0.7900
0.7671
1209.9284
0.8229
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
643.8596
1.0000
1.0000
1470.3390
1.0000
14248.7881
18575.5250
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Mixer:
LOGICAL CONNECTION
MIX-100
51
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Active):
60
Flow Specification
(Active)
61
* 254.7 psia
Molar:
* Mass: 643.9 lbmole/hr
1.858e+004 lb/hrStd Ideal Liq Volume:
1470 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 292 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: AMINA
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Liquid Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
2.054e+004
2.054e+004
18
Molar Enthalpy
(Btu/lbmole)
-1.007e+005
-1.007e+005
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
0.0000
1.0000
(F)
407.7
407.7
(psia)
190.0
190.0
(lbmole/hr) (lb/hr)
5020 3.033e+005
24.43
5020 3.033e+005
24.43
(Btu/hr)
-5.054e+008
-5.054e+008
(barrel/day)
* 2.041e+004
2.041e+004
22
PROPERTIES
23 24
Overall
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
-1666
-1666
30
Mass Entropy
(Btu/lb-F)
0.4044
0.4044
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
5.668e+005
5.668e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
6.265e+005
6.265e+005
35
HHV Mass Basis (Std)
1.037e+004
1.037e+004
36
CO2 Loading
3.103e-002
3.103e-002
37
CO2 App ML Con
(lbmole/ft3)
2.356e-002
2.356e-002
38
CO2 App WT Con
(lbmol/lb)
4.963e-004
4.963e-004
39
LHV Mass Basis (Std)
40
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
60.42
60.42
0.7855
0.7855
47.46 2.732e+004
47.46 2.732e+004
53.34
53.34
0.8828
0.8828
9380
9380
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
58.93
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
1.045
1.045
Specific Heat
(Btu/lbmole-F)
53.34
53.34
Std. Gas Flow
(MMSCFD)
45.63
45.63
(lb/ft3)
63.12
63.12
(USGPS)
13.28
Licensed to: LEGENDS
2.598e-002
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
13.28 2.598e-002
9.099
9.099
---
---
0.0000
---
1.039
1.039
1.039
1.039
2.081e+004 0.9731 63.54 2.041e+004
--0.9731 63.54 2.041e+004
1.000
1.000
(ft3/lbmole)
1.273
1.273
(Btu/lb)
344.3
---
0.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
17.31 7.049e-002 0.7398
17.31 7.049e-002 0.7398
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 293 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: AMINA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
Liquid Phase 51.36
51.36
0.8499
0.8499
51.36
51.36
0.8499
0.8499
---
---
---
---
---
---
21.16
21.16
37.71
37.71
2.041e+004
2.041e+004
2.873
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
30
H2O
14.4510
0.0029
260.3363
0.0009
17.8619
0.0009
31
Oxygen
0.0005
0.0000
0.0151
0.0000
0.0009
0.0000
32
Methane
0.0046
0.0000
0.0743
0.0000
0.0170
0.0000
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
3.8453
0.0008
115.6287
0.0004
22.2598
0.0011
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
150.5434
0.0300
6625.3710
0.0218
549.6652
0.0268
38
Nitrogen
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
4850.9181
0.9664
42
Ammonia
0.0000
0.0000
43
Total
5019.7630
1.0000
44
296312.9955 0.0000 303314.4222
0.9769
19950.8243
0.0000 1.0000
46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
0.0000
20540.6292
Liquid Phase
45
0.9713
0.0000
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
49
H2O
14.4510
0.0029
260.3363
0.0009
17.8619
0.0009
50
Oxygen
0.0005
0.0000
0.0151
0.0000
0.0009
0.0000
51
Methane
0.0046
0.0000
0.0743
0.0000
0.0170
0.0000
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
3.8453
0.0008
115.6287
0.0004
22.2598
0.0011
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
150.5434
0.0300
6625.3710
0.0218
549.6652
0.0268
57
Nitrogen
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
4850.9181
0.9664
61
Ammonia
0.0000
0.0000
62
Total
5019.7630
1.0000
63
0.0000 303314.4222
0.9769
19950.8243
0.0000
0.9713
0.0000
1.0000
0.0000
20540.6292
1.0000
K VALUE
64 65
296312.9955
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
0.0000
0.0000
---
67
H2O
0.0000
0.0000
---
68
Oxygen
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 294 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: AMINA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
0.0000
0.0000
---
---
---
---
14
Hydrogen
0.0000
0.0000
---
15
Ethane
0.0000
0.0000
---
16
Propane
---
---
---
17
CO2
0.0000
0.0000
---
18
Nitrogen
0.0000
0.0000
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
0.0000
0.0000
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Valve:
VLV-104 Distillation:
LOGICAL CONNECTION T-102
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
190.0 psia 5020 lbmole/hrMass:
37
3.033e+005 lb/hrStd Ideal Liq Volume: 2.054e+004 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: Anmonia
46 47 48
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
132.8
132.8
(psia)
114.7
114.7
(lbmole/hr) (lb/hr)
(Btu/hr)
1087 1.946e+004 1430 -1.112e+005 15.61 -1.209e+008 1399*
(barrel/day)
61
1087 1.946e+004 1430 -1.112e+005 15.61 -1.209e+008 1399
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
Aqueous Phase 17.90
17.90
3.205
3.205
57.36
57.36
(barrel/day)
1450
1450
(Btu/lb)
-6213
-6213
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 295 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Anmonia (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Aqueous Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
1.642e+004
1.642e+004
16
HHV Molar Basis (Std)
(Btu/lbmole)
3.511e+004
3.511e+004
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
(lbmole/ft3)
8.102e-005
8.102e-005
20
CO2 App WT Con
(lbmol/lb)
1.412e-006
1.412e-006
21
LHV Mass Basis (Std)
22
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
0.8721
0.8721
18.90
18.90
1.056
1.056
1962
1962
581.5
581.5
917.3
917.3
Phase Fraction [Vol. Basis]
0.0000
1.000
23
Phase Fraction [Mass Basis]
0.0000
1.000
24
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
25
Mass Exergy
(Btu/lb)
3.225
---
26
Partial Pressure of CO2
(psia)
0.0000
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
(psia)
59
True VP at 37.8 C
(psia)
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
3.250
3.250
Specific Heat
(Btu/lbmole-F)
18.90
18.90
Std. Gas Flow
(MMSCFD)
9.883
9.883
(lb/ft3)
58.17
58.17
(USGPS)
0.7049
0.7049
5.628e-003
(psia)
(Btu/lbmole)
5.628e-003
12.24
12.24
---
---
0.0000
---
1.117
1.117
1.187
1.187
1.732e+004
---
(cSt)
0.4624
0.4624
(lb/ft3)
59.44
59.44
(barrel/day)
1399
1399
1.000
1.000
(ft3/lbmole)
0.3120
0.3120
(Btu/lb)
967.9
---
0.0000
1.0000
(dyne/cm)
60.88
60.88
(Btu/hr-ft-F)
0.3561
0.3561
0.4249
0.4249
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.91
16.91
0.9451
0.9451
15.92
15.92
0.8895
0.8895
15.87
15.87
0.8870
0.8870
1.191
1.191
211.7
211.7
128.5
128.5
1399
1399
-10.20
---
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0002
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
0.0000
LIQUID VOLUME FRACTION 0.0000
Page 296 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Anmonia (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
0.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
15
H2O
956.1739
0.8794
0.8852
1181.8636
0.8264
16
Oxygen
0.0114
0.0000
0.3640
0.0000
0.0219
0.0000
17
Methane
0.0001
0.0000
0.0012
0.0000
0.0003
0.0000
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0117
0.0000
0.0236
0.0000
0.0231
0.0000
20
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.0275
0.0000
1.2095
0.0001
0.1003
0.0001
23
Nitrogen
0.0199
0.0000
0.5585
0.0000
0.0474
0.0000
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0029
0.0000
0.0002
0.0000
27
Ammonia
131.0322
0.1205
2231.4778
0.1147
248.0166
0.1734
28
Total
1087.2767
1.0000
19459.2060
1.0000
1430.0736
1.0000
29
17225.5682
Aqueous Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
33
CO
0.0000
0.0000
34
H2O
956.1739
0.8794
35
Oxygen
0.0114
0.0000
36
Methane
0.0001
37
H2S
38
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
0.0002
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
0.8852
1181.8636
0.8264
0.3640
0.0000
0.0219
0.0000
0.0000
0.0012
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0117
0.0000
0.0236
0.0000
0.0231
0.0000
39
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0275
0.0000
1.2095
0.0001
0.1003
0.0001
42
Nitrogen
0.0199
0.0000
0.5585
0.0000
0.0474
0.0000
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0029
0.0000
0.0002
0.0000
46
Ammonia
131.0322
0.1205
2231.4778
0.1147
248.0166
0.1734
47
Total
1087.2767
1.0000
19459.2060
1.0000
1430.0736
1.0000
17225.5682
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
0.0000
---
0.0000
52
H2O
0.0000
---
0.0000
53
Oxygen
0.0000
---
0.0000
54
Methane
0.0000
---
0.0000
---
---
---
Hydrogen
0.0000
---
0.0000
57
Ethane
0.0000
---
0.0000
58
Propane
---
---
---
59
CO2
0.0000
---
0.0000
60
Nitrogen
0.0000
---
0.0000
---
---
---
55
H2S
56
61
Air
62
Mercury
---
---
---
63
MEAmine
0.0000
---
0.0000
64
Ammonia
0.0000
---
0.0000
65
UNIT OPERATIONS
66 67 68 69
FEED TO Pump:
Aspen Technology Inc. Licensed to: LEGENDS
PRODUCT FROM P-101
Absorber:
LOGICAL CONNECTION T-101
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 297 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Anmonia (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Inactive):
18
Flow Specification
(Inactive) Molar:
114.7 psia 1087 lbmole/hrMass:
19
1.946e+004 lb/hrStd Ideal Liq Volume:
1430 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: CONDENSADO #1
28 29 30
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
Aqueous Phase
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
1.823e+005
1.823e+005
39
Molar Enthalpy
(Btu/lbmole)
-1.225e+005
-1.225e+005
40
Molar Entropy
(Btu/lbmole-F)
41
Heat Flow
42
Liq Vol Flow @Std Cond
0.0000
1.0000
(F)
110.1*
110.1
(psia)
274.7*
(lbmole/hr) (lb/hr)
274.7
1.473e+005
1.473e+005
* 2.656e+006
2.656e+006
13.95
13.95
(Btu/hr)
-1.804e+010
-1.804e+010
(barrel/day)
* 1.792e+005
1.792e+005
43
PROPERTIES
44 45
Overall
Aqueous Phase
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Mass Enthalpy
(Btu/lb)
-6790
-6790
51
Mass Entropy
(Btu/lb-F)
0.7736
0.7736
52
Heat Capacity
53
Mass Heat Capacity
54
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F)
18.03
18.03
3.442
3.442
62.06 1.830e+005
62.06 1.830e+005
18.57
18.57
(Btu/lb-F)
1.030
1.030
LHV Molar Basis (Std)
(Btu/lbmole)
1.868
55
HHV Molar Basis (Std)
(Btu/lbmole)
56
HHV Mass Basis (Std)
57
CO2 Loading
58
CO2 App ML Con
(lbmole/ft3)
2.424e-003
2.424e-003
59
CO2 App WT Con
(lbmol/lb)
3.906e-005
3.906e-005
60
LHV Mass Basis (Std)
61
(Btu/lb)
1.762e+004 977.1 ---
977.1 ---
0.1036
Phase Fraction [Vol. Basis]
0.0000
1.000
62
Phase Fraction [Mass Basis]
0.0000
1.000
63
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
64
Mass Exergy
(Btu/lb)
1.943
---
65
Partial Pressure of CO2
(psia)
0.0000
---
66
Cost Based on Flow
(Cost/s)
0.0000
0.0000
67
Act. Gas Flow
68
Avg. Liq. Density
Aspen Technology Inc. Licensed to: LEGENDS
(Btu/lb)
1.868 1.762e+004
0.1036
69
Fluid Package:
(ACFM)
---
---
(lbmole/ft3)
3.453
3.453
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 298 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: CONDENSADO #1 (continued)Property Package:
7 8 9
Basis-1 Peng-Robinson
PROPERTIES
10 11
Overall
Aqueous Phase
12
Specific Heat
(Btu/lbmole-F)
18.57
13
Std. Gas Flow
(MMSCFD)
1339
1339
14
Std. Ideal Liq. Mass Density
62.28
62.28
15
Act. Liq. Flow
16
Z Factor
17
Watson K
18
User Property
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
(psia)
---
---
41
True VP at 37.8 C
(psia)
238.9
238.9
42
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
43
Viscosity Index
(lb/ft3) (USGPS)
88.94 1.305e-002
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
8.489
---
---
0.0000
---
1.120
1.120
1.157
1.157
1.591e+004 63.37
(ft3/lbmole) (Btu/lb)
88.94 1.305e-002
8.489
0.6154
(barrel/day)
18.57
1.792e+005
--0.6154 63.37 1.792e+005
1.000
1.000
0.2906
0.2906
882.5
---
0.0000
1.0000
(dyne/cm)
68.85
68.85
(Btu/hr-ft-F)
0.3673
0.3673
0.6118
0.6118
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
16.58
16.58
0.9194
0.9194
16.05
16.05
0.8898
0.8898
15.84
15.84
0.8784
0.8784
1.172
1.172
1.792e+005 -4.393
44
1.792e+005 ---
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr) * 0.1396
MOLE FRACTION
H2O
52
Oxygen
* 0.2240
* 0.0000
* 7.1691
* 0.0000
* 0.4315
* 0.0000
53
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
54
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
55
Hydrogen
* 2.4818
* 0.0000
* 5.0032
* 0.0000
* 4.9040
* 0.0000
56
Ethane
* 0.0000
* 0.0000
* 0.0004
* 0.0000
* 0.0001
* 0.0000
57
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
58
CO2
* 103.7602
* 0.0007
* 4566.4535
* 0.0017
* 378.8498
* 0.0021
59
Nitrogen
* 4.9861
* 0.0000
* 139.6763
* 0.0001
* 11.8605
* 0.0001
60
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
61
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
62
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
63
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
64
Total
147299.3457
1.0000
2.656324390e+06
* 0.9982
1.0000
* 0.3349
LIQUID VOLUME FRACTION
CO
* 2.651602178e+06
* 0.0000
LIQUID VOLUME FLOW (barrel/day)
51
* 0.9992
* 3.9096
MASS FRACTION
0.0000
50
* 147187.7540
* 0.0000
MASS FLOW (lb/hr)
Vapour Fraction
* 181929.1050
182325.4857
* 0.0000 * 0.9978
1.0000
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 299 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: CONDENSADO #1 (continued)Property Package:
7 8 9
Basis-1 Peng-Robinson
COMPOSITION
10 11
Aqueous Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
16
H2O
17
Oxygen
0.2240
0.0000
7.1691
0.0000
0.4315
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
2.4818
0.0000
5.0032
0.0000
4.9040
0.0000
21
Ethane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
103.7602
0.0007
4566.4535
0.0017
378.8498
0.0021
24
Nitrogen
4.9861
0.0000
139.6763
0.0001
11.8605
0.0001
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.1396
0.0000
147187.7540
3.9096
0.9992
147299.3457
0.0000
2.651602178e+06
1.0000
2.656324390e+06
30
0.3349
0.9982
0.0000
181929.1050
1.0000
0.9978
182325.4857
1.0000
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
0.0000
---
0.0000
34
H2O
0.0000
---
0.0000
35
Oxygen
0.0000
---
0.0000
36
Methane
---
---
---
---
---
---
Hydrogen
0.0000
---
0.0000
39
Ethane
0.0000
---
0.0000
40
Propane
---
---
---
41
CO2
0.0000
---
0.0000
42
Nitrogen
0.0000
---
0.0000
---
---
---
37
H2S
38
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO Conversion Reactor:
PRODUCT FROM
H-1 REFORMADOR SECUNDARIO Recycle:
51
LOGICAL CONNECTION RCY-1
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Inactive) Molar:
61
* 274.7 psia
1.473e+005 lbmole/hr Mass:
2.656e+006 *lb/hrStd Ideal Liq Volume: 1.823e+005 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 300 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: DESTILATE WATER
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
213.2*
213.2
(psia)
214.7*
214.7
1059*
(lbmole/hr) (lb/hr)
(Btu/hr)
1.909e+004 1310 -1.205e+005 17.04 -1.277e+008 1288*
(barrel/day)
22
1059 1.909e+004 1310 -1.205e+005 17.04 -1.277e+008 1288
PROPERTIES
23 24
Overall
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
30
Mass Entropy
31
Heat Capacity
32
Mass Heat Capacity
33
(lbmole/ft3) (lb/ft3)
Aqueous Phase 18.02
18.02
3.285
3.285
59.18
59.18
(barrel/day)
1379
1379
(Btu/lb)
-6689
-6689
(Btu/lb-F)
0.9461
0.9461
18.91
18.91
(Btu/lbmole-F) (Btu/lb-F)
1.050
1.050
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
34
HHV Molar Basis (Std)
(Btu/lbmole)
35
HHV Mass Basis (Std)
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
16.11
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
---
---
54
User Property
---
---
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
18.91
18.91
Std. Gas Flow
(MMSCFD)
9.631
9.631
Licensed to: LEGENDS
(lb/ft3)
62.30
62.30
(USGPS)
0.6702
0.6702
9.051e-003
(psia)
(Btu/lbmole)
9.051e-003
0.0000
---
1.117
1.117
1.175
1.175
1.529e+004
---
(cSt)
0.2922
0.2922
(lb/ft3)
63.35
63.35
(barrel/day)
1288
1288
1.000
1.000
(ft3/lbmole)
0.3044
0.3044
(Btu/lb)
849.0
---
0.0000
1.0000
(dyne/cm)
58.48
58.48
(Btu/hr-ft-F)
0.3935
0.3935
0.2770
0.2770
(cP)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 301 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: DESTILATE WATER (continued) Property Package:
7 8 9
Basis-1 Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Aqueous Phase 16.93
16.93
0.9397
0.9397
16.10
16.10
0.8936
0.8936
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
1288
1288
-24.32
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr) * 0.0000
MOLE FRACTION
MASS FLOW (lb/hr)
LIQUID VOLUME FLOW (barrel/day)
CO H2O
31
Oxygen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
32
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
33
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
34
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
35
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
36
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
37
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
38
Nitrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
39
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
40
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
41
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
42
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
43
Total
* 1.0000
* 19086.7724
1.0000
44
19086.7724
* 0.0000
LIQUID VOLUME FRACTION
30
1059.4874
* 0.0000
MASS FRACTION
0.0000
29
* 1059.4874
* 0.0000
Vapour Fraction
* 0.0000
* 1.0000
1.0000
46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
48
CO
0.0000
0.0000
49
H2O
1059.4874
1.0000
50
Oxygen
0.0000
0.0000
51
Methane
0.0000
52
H2S
53
MASS FLOW (lb/hr)
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
1309.5627
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
1059.4874
1.0000
1.0000
1309.5627
1.0000
63
19086.7724
19086.7724
K VALUE
64 65
0.0000
* 1.0000
1309.5627
Aqueous Phase
45
* 0.0000
* 1309.5627
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
0.0000
---
0.0000
---
---
68 69
Oxygen
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 302 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: DESTILATE WATER (continued) Property Package:
7 8 9
Basis-1 Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Absorber:
LOGICAL CONNECTION
T-101
27
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Active)
* 214.7 psia * Mass: 1059 lbmole/hr
Molar:
37
1.909e+004 lb/hrStd Ideal Liq Volume:
1310 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: Entrada de Vapor
46 47 48
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Aqueous Phase 0.0000
1.0000
(F)
274.9
274.9
(psia)
364.7*
364.7
(lbmole/hr) (lb/hr)
(Btu/hr)
1918 * 3.456e+004
2371 -1.193e+005 18.72 -2.289e+008 2332*
(barrel/day)
61
1918 3.456e+004 2371 -1.193e+005 18.72 -2.289e+008 2332
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3) (lb/ft3)
Aqueous Phase 18.02
18.02
3.184
3.184
57.35
57.35
(barrel/day)
2576
2576
(Btu/lb)
-6623
-6623
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 303 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: Entrada de Vapor (continued)Property Package:
7 8 9
Basis-1 Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
(Btu/lb-F) (Btu/lbmole-F)
Aqueous Phase 1.039
1.039
19.36
19.36
(Btu/lb-F)
1.074
1.074
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
16
HHV Molar Basis (Std)
(Btu/lbmole)
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
(Btu/lb)
1.763e+004 978.7
1.763e+004 978.7
---
---
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
0.0000
1.000
23
Phase Fraction [Mass Basis]
0.0000
1.000
24
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
25
Mass Exergy
(Btu/lb)
32.15
---
26
Partial Pressure of CO2
(psia)
0.0000
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
---
---
36
User Property
---
---
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
3.458
3.458
Specific Heat
(Btu/lbmole-F)
19.36
19.36
Std. Gas Flow
(MMSCFD)
17.44
17.44
(lb/ft3)
62.30
62.30
(USGPS)
1.252 1.453e-002
(psia)
(Btu/lbmole)
1.252 1.453e-002
0.0000
---
1.114
1.114
1.182
1.182
1.445e+004
---
(cSt)
0.2207
0.2207
(lb/ft3)
63.35
63.35
(barrel/day)
2332
2332
1.000
1.000
(ft3/lbmole)
0.3141
0.3141
(Btu/lb)
802.3
---
0.0000
1.0000
(dyne/cm)
51.76
51.76
(Btu/hr-ft-F)
0.3975
0.3975
0.2027
0.2027
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
17.37
17.37
0.9642
0.9642
16.37
16.37
0.9089
0.9089
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
2332
2332
-45.55
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) * 0.0000
MOLE FRACTION * 0.0000
MASS FLOW (lb/hr) * 0.0000
Vapour Fraction MASS FRACTION * 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) * 0.0000
0.0000
LIQUID VOLUME FRACTION * 0.0000
Page 304 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: Entrada de Vapor (continued)Property Package:
7 8 9
Basis-1 Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr) * 1918.3906
MOLE FRACTION
MASS FLOW (lb/hr) * 34560.0000
MASS FRACTION
0.0000
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
* 2371.1965
* 1.0000
15
H2O
16
Oxygen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
17
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
18
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
19
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
20
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
21
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
22
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
23
Nitrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
24
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
25
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
26
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
27
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
28
Total
1918.3906
* 1.0000
Vapour Fraction
1.0000
29
34560.0000
* 1.0000
1.0000
2371.1965
Aqueous Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
33
CO
0.0000
0.0000
34
H2O
1918.3906
1.0000
35
Oxygen
0.0000
0.0000
36
Methane
0.0000
37
H2S
38
MASS FLOW (lb/hr) 0.0000
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
0.0000
0.0000
0.0000
1.0000
2371.1965
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
1918.3906
1.0000
1.0000
2371.1965
1.0000
34560.0000
34560.0000
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
---
---
---
52
H2O
0.0000
---
0.0000
53
Oxygen
---
---
---
54
Methane
---
---
---
---
---
---
55
H2S
56
Hydrogen
---
---
---
57
Ethane
---
---
---
58
Propane
---
---
---
59
CO2
---
---
---
60
Nitrogen
---
---
---
---
---
---
61
Air
62
Mercury
---
---
---
63
MEAmine
---
---
---
64
Ammonia
---
---
---
65
UNIT OPERATIONS
66 67 68 69
FEED TO LNG:
Aspen Technology Inc. Licensed to: LEGENDS
PRODUCT FROM
LOGICAL CONNECTION
LNG-101
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 305 of 336 * Specified by user.
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LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: Entrada de Vapor (continued)Property Package:
7 8 9
Basis-1 Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Active):
18
Flow Specification
(Active)
* 364.7 psia
Molar:
1918 lbmole/hrMass:
19
2371 barrel/day
User Variables
20 21
NOTES
22 23
3.456e+004 *lb/hrStd Ideal Liq Volume:
29285
24 25
(Last modified Tue Dec 11, 2018, 17:29)
26 27
Description
28 29 30
Material Stream: FEED GAS
31 32 33
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
34 35
Overall
36
Vapour / Phase Fraction
37
Temperature:
38
Pressure:
39
Molar Flow
40
Mass Flow
41
Std Ideal Liq Vol Flow
(barrel/day)
42
Molar Enthalpy
(Btu/lbmole)
43
Molar Entropy
(Btu/lbmole-F)
44
Heat Flow
45
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
60.00*
60.00
(psia)
414.7*
414.7
792.2*
(lbmole/hr) (lb/hr)
1.374e+004 3013 -3.254e+004 37.34
792.2 1.374e+004 3013 -3.254e+004 37.34
(Btu/hr)
-2.578e+007
-2.578e+007
(barrel/day)
* 1.279e+006
1.279e+006
46
PROPERTIES
47 48
Overall
Vapour Phase
49
Molecular Weight
50
Molar Density
51
Mass Density
52
Act. Volume Flow
53
Mass Enthalpy
(Btu/lb)
-1876
-1876
54
Mass Entropy
(Btu/lb-F)
2.153
2.153
55
Heat Capacity
56
Mass Heat Capacity
57
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
58
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
59
HHV Mass Basis (Std)
2.274e+004
2.274e+004
60
CO2 Loading
61
CO2 App ML Con
62
CO2 App WT Con
63
LHV Mass Basis (Std)
64
Phase Fraction [Vol. Basis]
1.000
1.000
65
Phase Fraction [Mass Basis]
1.000
1.000
66
Phase Fraction [Act. Vol. Basis]
1.000
1.000
67
Mass Exergy
(Btu/lb)
201.3
---
68
Partial Pressure of CO2
(psia)
0.5811
---
69
Aspen Technology Inc. Licensed to: LEGENDS
17.34 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
8.051e-002 1.396 4.207e+004
17.34 8.051e-002 1.396 4.207e+004
9.668
9.668
0.5575
0.5575
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 306 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: FEED GAS (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Cost Based on Flow
(Cost/s)
6445
6445
13
Act. Gas Flow
(ACFM)
164.0
164.0
14
Avg. Liq. Density
(lbmole/ft3)
1.124
1.124
15
Specific Heat
(Btu/lbmole-F)
9.668
9.668
16
Std. Gas Flow
(MMSCFD)
7.201
7.201
17
Std. Ideal Liq. Mass Density
(lb/ft3)
19.49
19.49
18
Act. Liq. Flow
(USGPS)
---
---
19
Z Factor
0.9237
0.9237
20
Watson K
19.04
19.04
21
User Property
---
---
22
Partial Pressure of H2S
23
Cp/(Cp - R)
24
Cp/Cv
25
Heat of Vap.
26
Kinematic Viscosity
27
Liq. Mass Density (Std. Cond)
28
Liq. Vol. Flow (Std. Cond)
29
Liquid Fraction
30
Molar Volume
31
Mass Heat of Vap.
32
Phase Fraction [Molar Basis]
33
Surface Tension
34
Thermal Conductivity
35
Viscosity
36
Cv (Semi-Ideal)
37
Mass Cv (Semi-Ideal)
38
Cv
39
Mass Cv
40
Cv (Ent. Method)
41
Mass Cv (Ent. Method)
42
Cp/Cv (Ent. Method)
43
Reid VP at 37.8 C
44
True VP at 37.8 C
45
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
46
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.258
1.258
1.406
1.406
2673
---
0.5163
0.5163
4.592e-002
4.592e-002
1.279e+006
1.279e+006
0.0000
0.0000
(ft3/lbmole)
12.42
12.42
(Btu/lb)
154.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.944e-002
1.944e-002
1.155e-002
1.155e-002
7.682
7.682
0.4430
0.4430
6.876
6.876
0.3965
0.3965
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
1.279e+006 -38.94
47
1.279e+006 ---
COMPOSITION
48 49
Overall Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
53
CO
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
54
H2O
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
55
Oxygen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
56
Methane
* 717.8618
* 0.9061
57
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
58
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
59
Ethane
* 58.9958
* 0.0745
* 0.1291
* 341.5139
* 0.1133
60
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
61
CO2
* 1.1101
* 0.0014
* 48.8568
* 0.0036
* 4.0533
* 0.0013
62
Nitrogen
* 14.2732
* 0.0180
* 399.8347
* 0.0291
* 33.9518
* 0.0113
63
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
64
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
65
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
66
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
67
Total
792.2409
1.0000
* 11516.5851
* 1773.9985
13739.2751
* 0.8382
1.0000
* 2633.8976
3013.4166
* 0.8741
1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 307 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: FEED GAS (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
717.8618
0.9061
0.8382
2633.8976
0.8741
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
58.9958
0.0745
1773.9985
0.1291
341.5139
0.1133
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
1.1101
0.0014
48.8568
0.0036
4.0533
0.0013
24
Nitrogen
14.2732
0.0180
399.8347
0.0291
33.9518
0.0113
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
792.2409
1.0000
1.0000
3013.4166
1.0000
11516.5851
13739.2751
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Tee:
LOGICAL CONNECTION
TEE-101
51
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Active):
60
Flow Specification
(Active)
* 414.7 psia
Molar:
61
1.374e+004 lb/hrStd Ideal Liq Volume:
3013 barrel/day
User Variables
62 63
NOTES
64 65
* Mass: 792.2 lbmole/hr
29285
66 67 68 69
(Last modified Tue Dec 11, 2018, 17:24)
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 308 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: FEED GAS (continued)
7 8
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
9 10
Description
11 12 13
Material Stream: gas Acido
14 15 16
CONDITIONS
17 18
Overall
19
Vapour / Phase Fraction
20
Temperature:
21
Pressure:
22
Molar Flow
23
Mass Flow
24
Std Ideal Liq Vol Flow
25
Molar Enthalpy
(Btu/lbmole)
26
Molar Entropy
(Btu/lbmole-F)
27
Heat Flow
28
Liq Vol Flow @Std Cond
Vapour Phase
Liquid Phase
Liquid Phase
0.0384
0.0384
0.3974
0.5642
(F)
-341.2
-341.2
-341.2
-341.2
(psia)
170.0
170.0
170.0
170.0
198.2
7.606
78.79
111.9
7099
17.67
2171
4910
633.0
15.07
210.5
407.4
(lbmole/hr) (lb/hr) (barrel/day)
-1.206e+005 2.718
-3274 14.33
-4.573e+004 9.465
(Btu/hr)
-2.391e+007
-2.490e+004
-3.603e+006
(barrel/day)
* 3.199e+005
1.232e+004
1.274e+005
29
-1.813e+005 -2.824 -2.028e+007 7119
PROPERTIES
30 31
Overall
32
Molecular Weight
33
Molar Density
34
Mass Density
35
Act. Volume Flow
36
Vapour Phase
Liquid Phase
Liquid Phase
35.81
2.324
27.55
43.90
1.370
0.1433
1.898
2.234
49.07
0.3329
52.31
98.06
(barrel/day)
618.4
226.9
177.4
214.1
Mass Enthalpy
(Btu/lb)
-3367
-1409
-1660
37
Mass Entropy
(Btu/lb-F)
6.167
0.3435
38
Heat Capacity
39
Mass Heat Capacity
40
LHV Molar Basis (Std)
(Btu/lbmole)
6.420e+004
1.038e+005
1.504e+005
773.4
41
HHV Molar Basis (Std)
(Btu/lbmole)
6.709e+004
1.213e+005
1.560e+005
774.6
42
HHV Mass Basis (Std)
43
CO2 Loading
44
CO2 App ML Con
45
CO2 App WT Con
46
LHV Mass Basis (Std)
4.469e+004
5459
17.62
47
Phase Fraction [Vol. Basis]
2.380e-002
2.380e-002
0.3325
0.6437
48
Phase Fraction [Mass Basis]
2.489e-003
2.489e-003
49
Phase Fraction [Act. Vol. Basis]
50
Mass Exergy
51
Partial Pressure of CO2
52
Cost Based on Flow
53
Act. Gas Flow
54
Avg. Liq. Density
55 56 57
Std. Ideal Liq. Mass Density
58
Act. Liq. Flow
59
Z Factor
60
Watson K
61
User Property
62
Partial Pressure of H2S
63
Cp/(Cp - R)
64
Cp/Cv
65
Heat of Vap.
66
Kinematic Viscosity
67
Liq. Mass Density (Std. Cond)
68
Liq. Vol. Flow (Std. Cond)
69
Aspen Technology Inc.
(lbmole/ft3) (lb/ft3)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
7.590e-002 15.59
7.310
13.02
17.96
0.4354
3.146
0.4724
0.4092
1874
5.219e+004
5662
---
---
2.463e+039
(lbmole/ft3)
---
---
5.194e-003
(lbmol/lb)
---
---
9.929e-005
(Btu/lb)
(Btu/lb) (psia)
-4129 -6.433e-002
1793
17.64 1.071e+028 2.218 2.262e-002
0.3058
0.6917
0.3670
0.3670
0.2869
0.3461
314.0
---
---
---
---
---
---
0.0000
0.0000
1.189e-009
(Cost/s)
0.0000
0.0000
(ACFM)
0.8849
0.8849
---
---
(lbmole/ft3)
1.339
2.158
1.600
1.173
Specific Heat
(Btu/lbmole-F)
15.59
13.02
17.96
Std. Gas Flow
(MMSCFD)
1.802
0.7162
1.017
Licensed to: LEGENDS
7.310 6.914e-002
(lb/ft3)
47.94
5.014
(USGPS)
0.1903
---
8.624e-002 7.046e-002
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
44.09
51.52 0.1041
---
0.9337
8.360
41.81
7.782
5.989e-002 8.514
---
---
---
---
0.0000
---
---
---
1.146
1.373
1.180
1.124
1.008
1.525
1.629
1.000
9149
---
---
---
---
0.5273
0.4493
54.44
9.486e-002
6.133e-003
7.282e-002
2.948
3.199e+005
1.232e+004
1.274e+005
7119
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 309 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: gas Acido (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Liquid Fraction
13
Molar Volume
14
Mass Heat of Vap.
15
Phase Fraction [Molar Basis]
16
Surface Tension
17
Thermal Conductivity
18
Viscosity
19
Cv (Semi-Ideal)
20
Mass Cv (Semi-Ideal)
21
Cv
22
Mass Cv
23
Cv (Ent. Method)
24
Mass Cv (Ent. Method)
25
Cp/Cv (Ent. Method)
26
Reid VP at 37.8 C
27
True VP at 37.8 C
28
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
29
Viscosity Index
(ft3/lbmole) (Btu/lb)
Vapour Phase
Liquid Phase
Liquid Phase
0.9616
0.0000
1.000
1.000
0.7297
6.980
0.5267
0.4477
255.5
---
---
---
0.0384
0.0384
0.3974
0.5642
(dyne/cm)
---
14.31
58.41
(Btu/hr-ft-F)
---
3.033e-002
0.1377
0.1467
---
2.812e-003
(cP)
---
0.3765
85.51
13.60
5.324
11.03
---
0.3799
2.291
0.4004
---
15.46
4.794
7.992
---
0.4318
2.063
0.2901
---
---
---
9.018
---
---
---
0.3273
---
---
---
1.444
---
(psia)
---
---
---
---
(psia)
---
---
---
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
1.397e+005 19.01
30
1.232e+004 ---
1.274e+005 ---
--0.0000 ---
COMPOSITION
31 32
Overall Phase
33 34
COMPONENTS
35
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
0.0384
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
36
CO
58.6846
0.2960
1643.8092
0.2316
140.8030
0.2224
37
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Oxygen
4.1926
0.0211
134.1640
0.0189
8.0748
0.0128
39
Methane
3.6586
0.0185
58.6943
0.0083
13.4237
0.0212
40
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Hydrogen
8.4386
0.0426
17.0122
0.0024
16.6746
0.0263
42
Ethane
5.6111
0.0283
168.7244
0.0238
32.4813
0.0513
43
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
CO2
111.3102
0.5615
4898.7266
0.6901
406.4164
0.6421
45
Nitrogen
6.3500
0.0320
177.8812
0.0251
15.1047
0.0239
46
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Total
198.2456
1.0000
7099.0117
1.0000
632.9785
1.0000
51
Vapour Phase
52 53
COMPONENTS
54
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
3.837e-002 LIQUID VOLUME FRACTION
55
CO
0.0655
0.0086
1.8346
0.1038
0.1571
0.0104
56
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Oxygen
0.0017
0.0002
0.0551
0.0031
0.0033
0.0002
58
Methane
0.0001
0.0000
0.0017
0.0001
0.0004
0.0000
59
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Hydrogen
7.5159
0.9882
15.1521
0.8574
14.8514
0.9858
61
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Nitrogen
0.0225
0.0030
0.6293
0.0356
0.0534
0.0035
65
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.0000
Page 310 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: gas Acido (continued)
7 8 9
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase (continued)
12 13
Fluid Package:
Total
7.6057
1.0000
14
17.6726
Phase Fraction 1.0000
15.0657
Liquid Phase
15 16
COMPONENTS
17
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
3.837e-002 1.0000
Phase Fraction MASS FRACTION
0.3974
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
18
CO
57.9190
0.7351
1622.3628
0.7473
138.9660
0.6603
19
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Oxygen
4.1729
0.0530
133.5337
0.0615
8.0369
0.0382
21
Methane
3.6555
0.0464
58.6448
0.0270
13.4123
0.0637
22
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Hydrogen
0.9226
0.0117
1.8599
0.0009
1.8230
0.0087
24
Ethane
5.6106
0.0712
168.7105
0.0777
32.4786
0.1543
25
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
CO2
0.2156
0.0027
9.4864
0.0044
0.7870
0.0037
27
Nitrogen
6.2916
0.0799
176.2452
0.0812
14.9658
0.0711
28
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Total
78.7877
1.0000
2170.8433
1.0000
210.4697
1.0000
33
Liquid Phase
34 35
COMPONENTS
36
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.5642 LIQUID VOLUME FRACTION
37
CO
0.7001
0.0063
19.6118
0.0040
1.6799
0.0041
38
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Oxygen
0.0180
0.0002
0.5752
0.0001
0.0346
0.0001
40
Methane
0.0030
0.0000
0.0478
0.0000
0.0109
0.0000
41
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Hydrogen
0.0001
0.0000
0.0002
0.0000
0.0002
0.0000
43
Ethane
0.0005
0.0000
0.0138
0.0000
0.0027
0.0000
44
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
CO2
111.0946
0.9932
4889.2402
0.9957
405.6294
0.9955
46
Nitrogen
0.0359
0.0003
1.0067
0.0002
0.0855
0.0002
47
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Total
111.8522
1.0000
4910.4957
1.0000
407.4431
1.0000
52
K VALUE
53 54
COMPONENTS
MIXED
LIGHT
HEAVY
55
CO
2.801e-002
56
H2O
2.612e-042
57
Oxygen
1.029e-002
4.271e-003
1.407
58
Methane
7.205e-004
2.980e-004
0.5190
59
H2S
60
Hydrogen
1.171e-002 ---
---
---
204.2
84.39
61
Ethane
62
Propane
63
CO2
1.198e-011
2.556e-009
64
Nitrogen
8.898e-002
3.699e-002
65
Air
66
Mercury
67
MEAmine
68 69
Ammonia
Aspen Technology Inc. Licensed to: LEGENDS
1.218e-008 ---
5.034e-009 ---
---
---
---
---
2.084e-053 ---
Aspen HYSYS Version 8.8 (34.0.0.8909)
-----
1.376 1.533e-042
--1.229e+006 8.711e-005 --7.040e-012 9.192 ----1.223e-053 ---
Page 311 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: gas Acido (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Distillation:
LOGICAL CONNECTION T-102
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
170.0 psia 198.2 lbmole/hrMass:
23
7099 lb/hr Std Ideal Liq Volume:
633.0 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: GAS COMBUSTIBLE
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
44
Molar Entropy
(Btu/lbmole-F)
45
Heat Flow
46
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
60.00
60.00
(psia)
414.7
414.7
351.6
351.6
6097
6097
(lbmole/hr) (lb/hr)
1337 -3.254e+004 37.34
1337 -3.254e+004 37.34
(Btu/hr)
-1.144e+007
-1.144e+007
(barrel/day)
* 5.676e+005
5.676e+005
47
PROPERTIES
48 49
Overall
Vapour Phase
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Mass Enthalpy
(Btu/lb)
-1876
-1876
55
Mass Entropy
(Btu/lb-F)
2.153
2.153
56
Heat Capacity
57
Mass Heat Capacity
58
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
59
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
60
HHV Mass Basis (Std)
2.274e+004
2.274e+004
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65
Phase Fraction [Vol. Basis]
1.000
1.000
66
Phase Fraction [Mass Basis]
1.000
1.000
67
Phase Fraction [Act. Vol. Basis]
1.000
1.000
68
Mass Exergy
201.3
---
69
Aspen Technology Inc. Licensed to: LEGENDS
17.34 (lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
8.051e-002 1.396 1.867e+004
17.34 8.051e-002 1.396 1.867e+004
9.668
9.668
0.5575
0.5575
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
(Btu/lb)
---
2.067e+004
2.067e+004
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 312 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: GAS COMBUSTIBLE (continued) Property Package:
7 8 9
Basis-1 Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Vapour Phase
(psia)
0.5811
---
(Cost/s)
0.0000
0.0000
(ACFM)
72.78
72.78
(lbmole/ft3)
1.124
1.124
Specific Heat
(Btu/lbmole-F)
9.668
9.668
17
Std. Gas Flow
(MMSCFD)
3.196
3.196
18
Std. Ideal Liq. Mass Density
(lb/ft3)
19.49
19.49
19
Act. Liq. Flow
(USGPS)
---
---
20
Z Factor
0.9237
0.9237
21
Watson K
19.04
19.04
22
User Property
---
---
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
47
Viscosity Index
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.258
1.258
1.406
1.406
2673
---
0.5163
0.5163
4.592e-002
4.592e-002
5.676e+005
5.676e+005
0.0000
0.0000
(ft3/lbmole)
12.42
12.42
(Btu/lb)
154.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.944e-002
1.944e-002
1.155e-002
1.155e-002
7.682
7.682
0.4430
0.4430
6.876
6.876
0.3965
0.3965
---
---
---
---
---
---
(psia)
---
---
(psia)
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
5.676e+005 -38.94
48
5.676e+005 ---
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
54
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Methane
318.5575
0.9061
5110.5864
0.8382
1168.8153
0.8741
58
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Ethane
26.1799
0.0745
787.2275
0.1291
151.5498
0.1133
61
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
CO2
0.4926
0.0014
21.6806
0.0036
1.7987
0.0013
63
Nitrogen
6.3339
0.0180
177.4302
0.0291
15.0664
0.0113
64
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
66
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
67
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
68
Total
351.5639
1.0000
6096.9247
1.0000
1337.2302
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 313 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Fluid Package:
Material Stream: GAS COMBUSTIBLE (continued) Property Package:
7 8 9
Basis-1 Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
318.5575
0.9061
5110.5864
0.8382
1168.8153
0.8741
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
26.1799
0.0745
787.2275
0.1291
151.5498
0.1133
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.4926
0.0014
21.6806
0.0036
1.7987
0.0013
24
Nitrogen
6.3339
0.0180
177.4302
0.0291
15.0664
0.0113
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
351.5639
1.0000
6096.9247
1.0000
1337.2302
1.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49
FEED TO
PRODUCT FROM
50
Tee:
51
LOGICAL CONNECTION TEE-101
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Inactive):
60
Flow Specification
(Inactive) Molar:
61
414.7 psia 351.6 lbmole/hrMass:
6097 lb/hr Std Ideal Liq Volume:
1337 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 314 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
18
Molar Enthalpy
(Btu/lbmole)
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
60.00*
60.00
(psia)
414.7*
414.7
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
0.0000 -3.254e+004
0.0000 -3.254e+004
37.34
37.34
(Btu/hr)
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
22
PROPERTIES
23 24
Overall
Vapour Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29 30 31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
35
HHV Mass Basis (Std)
2.274e+004
2.274e+004
36
CO2 Loading
37
CO2 App ML Con
38
CO2 App WT Con
39
LHV Mass Basis (Std)
40
Phase Fraction [Vol. Basis]
1.000
1.000
41
Phase Fraction [Mass Basis]
1.000
1.000
42
Phase Fraction [Act. Vol. Basis]
---
---
43
Mass Exergy
(Btu/lb)
201.3
---
44
Partial Pressure of CO2
(psia)
0.5811
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
0.0000
47
Avg. Liq. Density
48
17.34 (lbmole/ft3) (lb/ft3)
8.051e-002
17.34 8.051e-002
1.396
1.396
(barrel/day)
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
-1876
-1876
Mass Entropy
(Btu/lb-F)
2.153
2.153
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
9.668
9.668
0.5575
0.5575
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
(ACFM)
0.0000
(lbmole/ft3)
---
---
Specific Heat
(Btu/lbmole-F)
9.668
9.668
49
Std. Gas Flow
(MMSCFD)
50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc. Licensed to: LEGENDS
0.0000
0.0000
(lb/ft3)
19.49
19.49
(USGPS)
---
---
0.9237
0.9237
19.04
19.04
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
0.0000
---
1.258
1.258
1.406
1.406
2673
---
0.5163
0.5163
4.592e-002
4.592e-002
0.0000
0.0000
0.0000
0.0000
(ft3/lbmole)
12.42
12.42
(Btu/lb)
154.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP)
---
---
1.944e-002
1.944e-002
1.155e-002
1.155e-002
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 315 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
21 22
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
Vapour Phase 7.682
7.682
0.4430
0.4430
6.876
6.876
0.3965
0.3965
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
Viscosity Index
-38.94
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
29
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Methane
0.0000
0.9061
0.0000
0.8382
0.0000
0.8741
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Ethane
0.0000
0.0745
0.0000
0.1291
0.0000
0.1133
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
0.0000
0.0014
0.0000
0.0036
0.0000
0.0013
38
Nitrogen
0.0000
0.0180
0.0000
0.0291
0.0000
0.0113
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
43
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
44
Vapour Phase
45 46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
51
Methane
0.0000
0.9061
0.0000
0.8382
0.0000
0.8741
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Ethane
0.0000
0.0745
0.0000
0.1291
0.0000
0.1133
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
0.0000
0.0014
0.0000
0.0036
0.0000
0.0013
57
Nitrogen
0.0000
0.0180
0.0000
0.0291
0.0000
0.0113
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
63
K VALUE
64 65
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
---
---
---
67
H2O
---
---
---
68
Oxygen
---
---
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 316 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
---
---
---
---
---
---
14
Hydrogen
---
---
---
15
Ethane
---
---
---
16
Propane
---
---
---
17
CO2
---
---
---
18
Nitrogen
---
---
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
---
---
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25
FEED TO
PRODUCT FROM
26
Component Splitter:
27
LOGICAL CONNECTION D-4A
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Active):
36
Flow Specification
(Inactive) Molar:
* 414.7 psia
0.0000 lbmole/hrMass:
37
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: H2S-1
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
57
Molar Enthalpy
(Btu/lbmole)
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Vapour Phase 1.0000
1.0000
(F)
60.00*
60.00
(psia)
414.7*
414.7
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
0.0000 -3.254e+004
0.0000 -3.254e+004
37.34
37.34
(Btu/hr)
0.0000
0.0000
(barrel/day)
* 0.0000
0.0000
61
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 17.34
(lbmole/ft3) (lb/ft3)
8.051e-002
17.34 8.051e-002
1.396
1.396
(barrel/day)
0.0000
0.0000
(Btu/lb)
-1876
-1876
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 317 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S-1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
3.584e+005
3.584e+005
16
HHV Molar Basis (Std)
(Btu/lbmole)
3.943e+005
3.943e+005
17
HHV Mass Basis (Std)
2.274e+004
2.274e+004
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
Phase Fraction [Vol. Basis]
1.000
1.000
23
Phase Fraction [Mass Basis]
1.000
1.000
24
Phase Fraction [Act. Vol. Basis]
---
---
25
Mass Exergy
(Btu/lb)
201.3
---
26
Partial Pressure of CO2
(psia)
0.5811
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
28
Act. Gas Flow
0.0000
29
Avg. Liq. Density
30
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
2.153
2.153
9.668
9.668
0.5575
0.5575
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
(Btu/lb)
---
2.067e+004
2.067e+004
(ACFM)
0.0000
(lbmole/ft3)
---
---
Specific Heat
(Btu/lbmole-F)
9.668
9.668
31
Std. Gas Flow
(MMSCFD)
32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
59
True VP at 37.8 C
60 61
0.0000
0.0000
(lb/ft3)
19.49
19.49
(USGPS)
---
---
0.9237
0.9237
19.04
19.04
---
---
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
0.0000
---
1.258
1.258
1.406
1.406
2673
---
0.5163
0.5163
4.592e-002
(barrel/day)
4.592e-002
0.0000
0.0000
0.0000
0.0000
(ft3/lbmole)
12.42
12.42
(Btu/lb)
154.1
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
1.944e-002
1.944e-002
1.155e-002
1.155e-002
7.682
7.682
0.4430
0.4430
6.876
6.876
0.3965
0.3965
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
Viscosity Index
-38.94
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
62
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0000
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0000
1.0000
LIQUID VOLUME FRACTION 0.0000
Page 318 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S-1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
15
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Methane
0.0000
0.9061
0.0000
0.8382
0.0000
0.8741
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
0.0000
0.0745
0.0000
0.1291
0.0000
0.1133
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
0.0000
0.0014
0.0000
0.0036
0.0000
0.0013
23
Nitrogen
0.0000
0.0180
0.0000
0.0291
0.0000
0.0113
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
29
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Methane
0.0000
0.9061
0.0000
0.8382
0.0000
0.8741
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
0.0000
0.0745
0.0000
0.1291
0.0000
0.1133
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
0.0000
0.0014
0.0000
0.0036
0.0000
0.0013
42
Nitrogen
0.0000
0.0180
0.0000
0.0291
0.0000
0.0113
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
48
K VALUE
49 50
COMPONENTS
MIXED
LIGHT
HEAVY
51
CO
---
---
---
52
H2O
---
---
---
53
Oxygen
---
---
---
54
Methane
---
---
---
---
---
---
55
H2S
56
Hydrogen
---
---
---
57
Ethane
---
---
---
58
Propane
---
---
---
59
CO2
---
---
---
60
Nitrogen
---
---
---
---
---
---
61
Air
62
Mercury
---
---
---
63
MEAmine
---
---
---
64
Ammonia
---
---
---
65
UNIT OPERATIONS
66 67
FEED TO
68 69
PRODUCT FROM Component Splitter:
Aspen Technology Inc. Licensed to: LEGENDS
LOGICAL CONNECTION D-4B
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 319 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: H2S-1 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UTILITIES
10 11
( No utilities reference this stream )
12
PROCESS UTILITY
13 14 15
DYNAMICS
16 17
Pressure Specification
(Active):
18
Flow Specification
(Inactive) Molar:
* 414.7 psia
0.0000 lbmole/hrMass:
19
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
20 21
NOTES
22 23 24
Description
25 26 27
Material Stream: MEA
28 29 30
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
31 32
Overall
Liquid Phase
33
Vapour / Phase Fraction
34
Temperature:
35
Pressure:
36
Molar Flow
37
Mass Flow
38
Std Ideal Liq Vol Flow
(barrel/day)
* 1.995e+004
1.995e+004
39
Molar Enthalpy
(Btu/lbmole)
-1.128e+005
-1.128e+005
40
Molar Entropy
(Btu/lbmole-F)
41
Heat Flow
42
Liq Vol Flow @Std Cond
0.0000
1.0000
(F)
110.0*
110.0
(psia)
244.7*
244.7
(lbmole/hr) (lb/hr)
4851 2.963e+005
3.899
4851 2.963e+005
3.899
(Btu/hr)
-5.474e+008
-5.474e+008
(barrel/day)
* 1.994e+004
1.994e+004
43
PROPERTIES
44 45
Overall
Liquid Phase
46
Molecular Weight
47
Molar Density
48
Mass Density
49
Act. Volume Flow
50
Mass Enthalpy
(Btu/lb)
51
Mass Entropy
(Btu/lb-F)
52
Heat Capacity
53
Mass Heat Capacity
54
LHV Molar Basis (Std)
(Btu/lbmole)
5.860e+005
5.860e+005
55
HHV Molar Basis (Std)
(Btu/lbmole)
6.477e+005
6.477e+005
56
HHV Mass Basis (Std)
1.060e+004
1.060e+004
57
CO2 Loading
58
CO2 App ML Con
59
CO2 App WT Con
60
LHV Mass Basis (Std)
61
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
61.08
61.08
1.006
1.006
61.47 2.061e+004 -1847 6.383e-002
61.47 2.061e+004 -1847 6.383e-002
43.26
43.26
0.7082
0.7082
0.0000
0.0000
(lbmole/ft3)
0.0000
0.0000
(lbmol/lb)
0.0000
0.0000
(Btu/lb)
9594
9594
Phase Fraction [Vol. Basis]
0.0000
1.000
62
Phase Fraction [Mass Basis]
0.0000
1.000
63
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
64
Mass Exergy
(Btu/lb)
1.774
---
65
Partial Pressure of CO2
(psia)
0.0000
---
66
Cost Based on Flow
(Cost/s)
0.0000
0.0000
67
Act. Gas Flow
68
Avg. Liq. Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
(ACFM)
---
---
(lbmole/ft3)
1.039
1.039
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 320 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Liquid Phase
12
Specific Heat
(Btu/lbmole-F)
43.26
43.26
13
Std. Gas Flow
(MMSCFD)
44.10
44.10
14
Std. Ideal Liq. Mass Density
(lb/ft3)
63.49
63.49
15
Act. Liq. Flow
(USGPS)
10.02
16
Z Factor
17
Watson K
18
User Property
19
Partial Pressure of H2S
20
Cp/(Cp - R)
21
Cp/Cv
22
Heat of Vap.
23
Kinematic Viscosity
24
Liq. Mass Density (Std. Cond)
25
Liq. Vol. Flow (Std. Cond)
26
Liquid Fraction
27
Molar Volume
28
Mass Heat of Vap.
29
Phase Fraction [Molar Basis]
30
Surface Tension
31
Thermal Conductivity
32
Viscosity
33
Cv (Semi-Ideal)
34
Mass Cv (Semi-Ideal)
35
Cv
36
Mass Cv
37
Cv (Ent. Method)
38
Mass Cv (Ent. Method)
39
Cp/Cv (Ent. Method)
40
Reid VP at 37.8 C
(psia)
41
True VP at 37.8 C
(psia)
42
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
43
Viscosity Index
3.977e-002
(psia)
(Btu/lbmole) (cSt)
9.103
9.103
---
---
0.0000
---
1.048
1.048
2.950
2.950
1.404e+004 11.05
(lb/ft3)
63.53
(barrel/day) (ft3/lbmole) (Btu/lb)
10.02 3.977e-002
1.994e+004
--11.05 63.53 1.994e+004
1.000
1.000
0.9937
0.9937
229.9
---
0.0000
1.0000
(dyne/cm)
46.52
46.52
(Btu/hr-ft-F)
0.1091
0.1091
10.88
10.88
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
41.28
41.28
0.6757
0.6757
14.67
14.67
0.2401
0.2401
---
---
---
---
---
---
2.125e-002
2.125e-002
2.125e-002
2.125e-002
1.994e+004
1.994e+004
24.13
44
---
COMPOSITION
45 46
Overall Phase
47 48
COMPONENTS
49
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
50
CO
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
51
H2O
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
52
Oxygen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
53
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
54
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
55
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
56
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
57
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
58
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
59
Nitrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
60
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
61
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
62
MEAmine
63
Ammonia
64
Total
* 4851.3340 * 0.0000
4851.3340
* 1.0000 * 0.0000
1.0000
* 296338.4030 * 0.0000
296338.4030
* 1.0000 * 0.0000
1.0000
* 19952.5350 * 0.0000
19952.5350
* 1.0000 * 0.0000
1.0000
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 321 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Liquid Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
4851.3340
1.0000
28
Ammonia
0.0000
0.0000
29
Total
4851.3340
1.0000
296338.4030 0.0000 296338.4030
30
1.0000
19952.5350
0.0000
1.0000
0.0000
1.0000
0.0000
19952.5350
1.0000
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
0.0000
0.0000
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Absorber:
LOGICAL CONNECTION
T-100
51
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Active):
60
Flow Specification
(Active)
61
* 244.7 psia
Molar:
4851 lbmole/hrMass:
* 2.963e+005 lb/hrStd Ideal Liq Volume: 1.995e+004 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 322 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA RICA
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10 11
Overall
Liquid Phase
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Molar Flow
16
Mass Flow
17
Std Ideal Liq Vol Flow
(barrel/day)
2.043e+004
2.043e+004
18
Molar Enthalpy
(Btu/lbmole)
-1.133e+005
-1.133e+005
19
Molar Entropy
(Btu/lbmole-F)
20
Heat Flow
21
Liq Vol Flow @Std Cond
0.0000
1.0000
(F)
113.3
113.3
(psia)
229.7
229.7
(lbmole/hr) (lb/hr)
4995 3.015e+005
5.022
4995 3.015e+005
5.022
(Btu/hr)
-5.657e+008
-5.657e+008
(barrel/day)
* 2.036e+004
2.036e+004
22
PROPERTIES
23 24
Overall
Liquid Phase
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Act. Volume Flow
29
Mass Enthalpy
(Btu/lb)
30
Mass Entropy
(Btu/lb-F)
31
Heat Capacity
32
Mass Heat Capacity
33
LHV Molar Basis (Std)
(Btu/lbmole)
5.707e+005
5.707e+005
34
HHV Molar Basis (Std)
(Btu/lbmole)
6.309e+005
6.309e+005
35
HHV Mass Basis (Std)
1.045e+004
1.045e+004
36
CO2 Loading
1.992e-002
1.992e-002
37
CO2 App ML Con
(lbmole/ft3)
1.958e-002
1.958e-002
38
CO2 App WT Con
(lbmol/lb)
3.205e-004
3.205e-004
39
LHV Mass Basis (Std)
40
(lbmole/ft3) (lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
60.37
60.37
1.012
1.012
61.10 2.110e+004 -1876 8.319e-002
61.10 2.110e+004 -1876 8.319e-002
42.61
42.61
0.7058
0.7058
9455
9455
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Mass Exergy
(Btu/lb)
2.134
---
44
Partial Pressure of CO2
(psia)
0.0000
---
45
Cost Based on Flow
(Cost/s)
0.0000
0.0000
46
Act. Gas Flow
47
Avg. Liq. Density
48 49 50
Std. Ideal Liq. Mass Density
51
Act. Liq. Flow
52
Z Factor
53
Watson K
54
User Property
55
Partial Pressure of H2S
56
Cp/(Cp - R)
57
Cp/Cv
58
Heat of Vap.
59
Kinematic Viscosity
60
Liq. Mass Density (Std. Cond)
61
Liq. Vol. Flow (Std. Cond)
62
Liquid Fraction
63
Molar Volume
64
Mass Heat of Vap.
65
Phase Fraction [Molar Basis]
66
Surface Tension
67
Thermal Conductivity
68
Viscosity
69
Aspen Technology Inc.
(ACFM)
---
---
(lbmole/ft3)
1.045
1.045
Specific Heat
(Btu/lbmole-F)
42.61
42.61
Std. Gas Flow
(MMSCFD)
45.40
45.40
(lb/ft3)
63.08
63.08
(USGPS)
10.25
Licensed to: LEGENDS
3.691e-002
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day) (ft3/lbmole) (Btu/lb)
10.25 3.691e-002
9.109
9.109
---
---
0.0000
---
1.049
1.049
2.803
2.803
2.061e+004 9.896 63.32 2.036e+004
--9.896 63.32 2.036e+004
1.000
1.000
0.9880
0.9880
341.4
---
0.0000
1.0000
(dyne/cm)
45.05
45.05
(Btu/hr-ft-F)
0.1060
0.1060
9.685
9.685
(cP)
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 323 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA RICA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Liquid Phase
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
(psia)
20
True VP at 37.8 C
(psia)
236.3
21
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
22
Viscosity Index
(Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
40.62
40.62
0.6729
0.6729
15.20
15.20
0.2518
0.2518
18.88
18.88
0.3128
0.3128
2.256
2.256
21.56
21.56 236.3
2.036e+004
2.036e+004
23.52
---
23
COMPOSITION
24 25
Overall Phase
26 27
COMPONENTS
28
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
29
CO
0.6790
0.0001
19.0190
0.0001
1.6291
0.0001
30
H2O
14.4510
0.0029
260.3363
0.0009
17.8619
0.0009
31
Oxygen
4.1931
0.0008
134.1791
0.0004
8.0757
0.0004
32
Methane
3.6632
0.0007
58.7686
0.0002
13.4407
0.0007
33
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
34
Hydrogen
8.4386
0.0017
17.0122
0.0001
16.6746
0.0008
35
Ethane
9.4564
0.0019
284.3530
0.0009
54.7410
0.0027
36
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
CO2
96.6394
0.0193
4253.0720
0.0141
352.8505
0.0173
38
Nitrogen
6.3500
0.0013
177.8814
0.0006
15.1047
0.0007
39
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
MEAmine
4850.9181
0.9712
42
Ammonia
0.0000
0.0000
43
Total
4994.7887
1.0000
44
296312.9955 0.0000 301517.6171
0.9827
19950.8243
0.0000 1.0000
46
COMPONENTS
47
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
0.0000
20431.2026
Liquid Phase
45
0.9765
0.0000
1.0000
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
48
CO
0.6790
0.0001
19.0190
0.0001
1.6291
0.0001
49
H2O
14.4510
0.0029
260.3363
0.0009
17.8619
0.0009
50
Oxygen
4.1931
0.0008
134.1791
0.0004
8.0757
0.0004
51
Methane
3.6632
0.0007
58.7686
0.0002
13.4407
0.0007
52
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
Hydrogen
8.4386
0.0017
17.0122
0.0001
16.6746
0.0008
54
Ethane
9.4564
0.0019
284.3530
0.0009
54.7410
0.0027
55
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
56
CO2
96.6394
0.0193
4253.0720
0.0141
352.8505
0.0173
57
Nitrogen
6.3500
0.0013
177.8814
0.0006
15.1047
0.0007
58
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
MEAmine
4850.9181
0.9712
61
Ammonia
0.0000
0.0000
62
Total
4994.7887
1.0000
63
0.0000 301517.6171
0.9827
19950.8243
0.0000
0.9765
0.0000
1.0000
0.0000
20431.2026
1.0000
K VALUE
64 65
296312.9955
COMPONENTS
MIXED
LIGHT
HEAVY
66
CO
0.0000
0.0000
---
67
H2O
0.0000
0.0000
---
68
Oxygen
0.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
---
Page 324 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA RICA (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
12
Methane
13
H2S
LIGHT
HEAVY
0.0000
0.0000
---
---
---
---
14
Hydrogen
0.0000
0.0000
---
15
Ethane
0.0000
0.0000
---
16
Propane
---
---
---
17
CO2
0.0000
0.0000
---
18
Nitrogen
0.0000
0.0000
---
---
---
---
19
Air
20
Mercury
---
---
---
21
MEAmine
0.0000
0.0000
---
22
Ammonia
---
---
---
23
UNIT OPERATIONS
24 25 26
FEED TO
PRODUCT FROM
Mixer:
MIX-101 Absorber:
27
LOGICAL CONNECTION T-100
UTILITIES
28 29
( No utilities reference this stream )
30
PROCESS UTILITY
31 32 33
DYNAMICS
34 35
Pressure Specification
(Inactive):
36
Flow Specification
(Inactive) Molar:
229.7 psia 4995 lbmole/hrMass:
37
3.015e+005 lb/hrStd Ideal Liq Volume: 2.043e+004 barrel/day
User Variables
38 39
NOTES
40 41 42
Description
43 44 45
Material Stream: MEA.
46 47 48
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
49 50
Overall
Vapour Phase
51
Vapour / Phase Fraction
52
Temperature:
53
Pressure:
54
Molar Flow
55
Mass Flow
56
Std Ideal Liq Vol Flow
(barrel/day)
2.054e+004
57
Molar Enthalpy
(Btu/lbmole)
-1.007e+005
58
Molar Entropy
(Btu/lbmole-F)
59
Heat Flow
60
Liq Vol Flow @Std Cond
Liquid Phase
0.2258
0.2258
0.7742
(F)
322.8
322.8
322.8
(psia)
15.00*
15.00
15.00
5020
1134
(lbmole/hr) (lb/hr)
3.033e+005
24.98
(Btu/hr)
-5.054e+008
(barrel/day)
* 2.041e+004
61
6.608e+004 4566 -9.243e+004 46.97 -1.048e+008 4441
3886 2.372e+005 1.597e+004 -1.031e+005 18.57 -4.006e+008 1.596e+004
PROPERTIES
62 63
Overall
64
Molecular Weight
65
Molar Density
66
Mass Density
67
Act. Volume Flow
68
Mass Enthalpy
69
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 60.42
(lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb)
8.043e-003 0.4860 2.668e+006 -1666
58.30 1.830e-003 0.1067 2.648e+006 -1586
Liquid Phase 61.04 0.8532 52.08 1.947e+004 -1689
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 325 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Entropy
13
Heat Capacity
14
Mass Heat Capacity
15
LHV Molar Basis (Std)
(Btu/lbmole)
5.668e+005
5.033e+005
5.853e+005
16
HHV Molar Basis (Std)
(Btu/lbmole)
6.265e+005
5.564e+005
6.469e+005
17
HHV Mass Basis (Std)
18
CO2 Loading
19
CO2 App ML Con
20
CO2 App WT Con
21
LHV Mass Basis (Std)
22
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.4134
0.8057
43.96
24.14
49.75
0.7276
0.4141
0.8149
1.037e+004
0.3041
9544
1.060e+004
---
---
5.268e-004
(lbmole/ft3)
---
---
4.489e-004
(lbmol/lb)
---
---
8.619e-006
(Btu/lb)
9380
8633
9588
Phase Fraction [Vol. Basis]
0.2223
0.2223
0.7777
23
Phase Fraction [Mass Basis]
0.2179
0.2179
24
Phase Fraction [Act. Vol. Basis]
0.9927
0.9927
25
Mass Exergy
(Btu/lb)
54.07
---
26
Partial Pressure of CO2
(psia)
1.965
---
---
27
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
28
Act. Gas Flow
29
Avg. Liq. Density
30 31 32
Std. Ideal Liq. Mass Density
33
Act. Liq. Flow
34
Z Factor
35
Watson K
36
User Property
37
Partial Pressure of H2S
38
Cp/(Cp - R)
39
Cp/Cv
40
Heat of Vap.
41
Kinematic Viscosity
42
Liq. Mass Density (Std. Cond)
43
Liq. Vol. Flow (Std. Cond)
44
Liquid Fraction
45
Molar Volume
46
Mass Heat of Vap.
47
Phase Fraction [Molar Basis]
48
Surface Tension
49
Thermal Conductivity
50
Viscosity
51
Cv (Semi-Ideal)
52
Mass Cv (Semi-Ideal)
53
Cv
54
Mass Cv
55
Cv (Ent. Method)
56
Mass Cv (Ent. Method)
57
Cp/Cv (Ent. Method)
58
Reid VP at 37.8 C
(psia)
59
True VP at 37.8 C
(psia)
60
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
61
Viscosity Index
(ACFM)
1.033e+004
1.033e+004
0.7821 7.298e-003 ---
---
(lbmole/ft3)
1.045
1.061
1.040
Specific Heat
(Btu/lbmole-F)
43.96
24.14
49.75
Std. Gas Flow
(MMSCFD)
45.63
10.30
35.33
(lb/ft3)
63.12
61.86
63.48
(USGPS)
9.464
---
---
0.9762
9.099
9.081
9.103
---
---
---
0.0000
---
---
1.047
1.090
1.042
1.012
1.101
1.042
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
3.497e+004
9.464 2.094e-003
---
---
---
4.347
1.665
63.54
63.61
2.041e+004
4441
63.52 1.596e+004
0.7742
0.0000
1.000
(ft3/lbmole)
124.3
546.5
1.172
(Btu/lb)
578.8
---
---
0.2258
0.2258
0.7742
(dyne/cm)
25.58
(Btu/hr-ft-F)
---
1.246e-002
---
7.427e-003
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
25.58 8.386e-002 1.389
41.98
22.15
47.76
0.6947
0.3800
0.7824
43.46
21.93
47.76
0.7193
0.3762
0.7824
---
---
---
---
---
---
---
---
---
21.16
98.38
0.3874
37.71
170.0
2.040e+004 8.787
62
4441 ---
0.6833 1.596e+004 ---
COMPOSITION
63 64
Overall Phase
65 66
COMPONENTS
67 68
CO
69
Aspen Technology Inc. Licensed to: LEGENDS
MOLAR FLOW (lbmole/hr) 0.0000
MOLE FRACTION 0.0000
MASS FLOW (lb/hr) 0.0011
Vapour Fraction MASS FRACTION 0.0000
Aspen HYSYS Version 8.8 (34.0.0.8909)
LIQUID VOLUME FLOW (barrel/day) 0.0001
0.2258
LIQUID VOLUME FRACTION 0.0000
Page 326 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase (continued)
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2258
LIQUID VOLUME FRACTION
15
H2O
14.4510
0.0029
260.3363
0.0009
17.8619
0.0009
16
Oxygen
0.0005
0.0000
0.0151
0.0000
0.0009
0.0000
17
Methane
0.0046
0.0000
0.0743
0.0000
0.0170
0.0000
18
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Ethane
3.8453
0.0008
115.6287
0.0004
22.2598
0.0011
21
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
CO2
150.5434
0.0300
6625.3710
0.0218
549.6652
0.0268
23
Nitrogen
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
24
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
MEAmine
4850.9181
0.9664
27
Ammonia
0.0000
0.0000
28
Total
5019.7630
1.0000
29
296312.9955 0.0000 303314.4222
0.9769 0.0000 1.0000
Vapour Phase
30 31
COMPONENTS
32
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
MASS FRACTION
19950.8243 0.0000
0.9713 0.0000
20540.6292
1.0000
Phase Fraction
0.2258
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
33
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
34
H2O
11.7701
0.0104
212.0396
0.0032
14.5482
0.0032
35
Oxygen
0.0005
0.0000
0.0150
0.0000
0.0009
0.0000
36
Methane
0.0046
0.0000
0.0739
0.0000
0.0169
0.0000
37
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Ethane
3.7836
0.0033
113.7731
0.0017
21.9026
0.0048
40
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
CO2
148.4988
0.1310
6535.3880
0.0989
542.1998
0.1187
42
Nitrogen
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
43
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
MEAmine
969.5452
0.8553
0.8962
3987.5394
0.8733
46
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
47
Total
1133.6029
1.0000
1.0000
4566.2079
1.0000
48
59223.6049 0.0000 66084.8957
Liquid Phase
49 50
COMPONENTS
51
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7742 LIQUID VOLUME FRACTION
52
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53
H2O
2.6809
0.0007
48.2968
0.0002
3.3137
0.0002
54
Oxygen
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
55
Methane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
56
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
57
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Ethane
0.0617
0.0000
1.8556
0.0000
0.3572
0.0000
59
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
CO2
2.0446
0.0005
89.9830
0.0004
7.4653
0.0005
61
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
MEAmine
3881.3728
0.9988
65
Ammonia
0.0000
0.0000
66
Total
3886.1601
1.0000
237089.3906 0.0000 237229.5265
0.9994 0.0000 1.0000
15963.2850 0.0000 15974.4213
0.9993 0.0000 1.0000
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 327 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
1620
1620
---
13
H2O
15.05
15.05
---
14
Oxygen
874.3
874.3
---
15
Methane
625.2
625.2
---
---
---
---
16
H2S
17
Hydrogen
1984
1984
---
18
Ethane
210.2
210.2
---
19
Propane
---
---
---
20
CO2
249.0
249.0
---
21
Nitrogen
1484
1484
---
---
---
---
22
Air
23
Mercury
---
---
---
24
MEAmine
0.8563
0.8563
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28 29
FEED TO
PRODUCT FROM
Recycle:
RCY-5
Valve:
LOGICAL CONNECTION VLV-104
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Active):
39
Flow Specification
(Inactive) Molar:
* 15.00 psia
5020 lbmole/hrMass:
40
3.033e+005 lb/hrStd Ideal Liq Volume: 2.054e+004 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: MEA..
49 50 51
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
Vapour Phase
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
(barrel/day)
2.054e+004
60
Molar Enthalpy
(Btu/lbmole)
-1.007e+005
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Liquid Phase
0.2258
0.2258
0.7742
(F)
322.8*
322.8
322.8
(psia)
15.00*
15.00
15.00
5020*
1134
(lbmole/hr) (lb/hr)
3.033e+005
24.98
(Btu/hr)
-5.054e+008
(barrel/day)
* 2.041e+004
64
6.608e+004 4566 -9.243e+004 46.97 -1.048e+008 4441
3886 2.372e+005 1.597e+004 -1.031e+005 18.57 -4.006e+008 1.596e+004
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Fluid Package:
Aspen Technology Inc. Licensed to: LEGENDS
Vapour Phase 60.42
(lbmole/ft3)
8.043e-003
58.30 1.830e-003
Liquid Phase 61.04 0.8532
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 328 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA.. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
Vapour Phase
Liquid Phase
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
(Btu/lb)
-1666
-1586
-1689
15
Mass Entropy
(Btu/lb-F)
0.4134
0.8057
0.3041
16
Heat Capacity
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
5.668e+005
5.033e+005
5.853e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
6.265e+005
5.564e+005
6.469e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
23
CO2 App WT Con
24
LHV Mass Basis (Std)
25
(lb/ft3) (barrel/day)
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
0.4860 2.668e+006
0.1067 2.648e+006
52.08 1.947e+004
43.96
24.14
49.75
0.7276
0.4141
0.8149
9544
1.060e+004
---
---
5.268e-004
(lbmole/ft3)
---
---
4.489e-004
(lbmol/lb)
---
---
8.619e-006
(Btu/lb)
9380
8633
9588
Phase Fraction [Vol. Basis]
0.2223
0.2223
0.7777
26
Phase Fraction [Mass Basis]
0.2179
0.2179
27
Phase Fraction [Act. Vol. Basis]
0.9927
0.9927
28
Mass Exergy
(Btu/lb)
54.07
---
29
Partial Pressure of CO2
(psia)
1.965
---
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
(psia)
62
True VP at 37.8 C
(psia)
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(ACFM)
1.037e+004
1.033e+004
1.033e+004
0.7821 7.298e-003 ---
---
(lbmole/ft3)
1.045
1.061
1.040
Specific Heat
(Btu/lbmole-F)
43.96
24.14
49.75
Std. Gas Flow
(MMSCFD)
45.63
10.30
35.33
(lb/ft3)
63.12
61.86
63.48
(USGPS)
9.464
---
---
0.9762
9.099
9.081
9.103
---
---
---
0.0000
---
---
1.047
1.090
1.042
1.012
1.101
1.042
(psia)
(Btu/lbmole) (cSt) (lb/ft3) (barrel/day)
3.497e+004
9.464 2.094e-003
---
---
---
4.347
1.665
63.54
63.61
2.041e+004
4441
63.52 1.596e+004
0.7742
0.0000
1.000
(ft3/lbmole)
124.3
546.5
1.172
(Btu/lb)
578.8
---
---
0.2258
0.2258
0.7742
(dyne/cm)
25.58
(Btu/hr-ft-F)
---
1.246e-002
---
7.427e-003
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
---
25.58 8.386e-002 1.389
41.98
22.15
47.76
0.6947
0.3800
0.7824
43.46
21.93
47.76
0.7193
0.3762
0.7824
---
---
---
---
---
---
---
---
---
21.16
98.38
0.3874
37.71
170.0
2.040e+004 8.787
4441 ---
0.6833 1.596e+004 ---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 329 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA.. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14 15
CO
16
H2O
17
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.2258
LIQUID VOLUME FRACTION
* 0.0000
* 0.0000
* 0.0011
* 0.0000
* 0.0001
* 0.0000
* 14.4510
* 0.0029
* 260.3363
* 0.0009
* 17.8619
* 0.0009
Oxygen
* 0.0005
* 0.0000
* 0.0151
* 0.0000
* 0.0009
* 0.0000
18
Methane
* 0.0046
* 0.0000
* 0.0743
* 0.0000
* 0.0170
* 0.0000
19
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
20
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
21
Ethane
* 3.8453
* 0.0008
* 115.6287
* 0.0004
* 22.2598
* 0.0011
22
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
23
CO2
* 150.5434
* 0.0300
* 0.0218
* 549.6652
* 0.0268
24
Nitrogen
* 0.0000
* 0.0000
* 0.0002
* 0.0000
* 0.0000
* 0.0000
25
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
26
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
27
MEAmine
28
Ammonia
29
Total
* 4850.9181 * 0.0000
5019.7630
* 0.9664 * 0.0000
1.0000
30
* 6625.3710
* 296312.9955 * 0.0000
303314.4222
* 0.9769 * 0.0000
1.0000
Vapour Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
MASS FRACTION
* 19950.8243 * 0.0000
* 0.9713 * 0.0000
20540.6292
1.0000
Phase Fraction
0.2258
LIQUID VOLUME FLOW (barrel/day)
LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
35
H2O
11.7701
0.0104
212.0395
0.0032
14.5482
0.0032
36
Oxygen
0.0005
0.0000
0.0150
0.0000
0.0009
0.0000
37
Methane
0.0046
0.0000
0.0739
0.0000
0.0169
0.0000
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
Ethane
3.7836
0.0033
113.7731
0.0017
21.9026
0.0048
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
148.4988
0.1310
6535.3879
0.0989
542.1998
0.1187
43
Nitrogen
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
969.5446
0.8553
0.8962
3987.5367
0.8733
47
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
1133.6022
1.0000
1.0000
4566.2052
1.0000
49
59223.5645 0.0000 66084.8553
Liquid Phase
50 51
COMPONENTS
52
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.7742 LIQUID VOLUME FRACTION
53
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
H2O
2.6809
0.0007
48.2968
0.0002
3.3137
0.0002
55
Oxygen
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
56
Methane
0.0000
0.0000
0.0004
0.0000
0.0001
0.0000
57
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
58
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Ethane
0.0617
0.0000
1.8556
0.0000
0.3572
0.0000
60
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
CO2
2.0446
0.0005
89.9831
0.0004
7.4653
0.0005
62
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
63
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
64
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
65
MEAmine
3881.3735
0.9988
66
Ammonia
0.0000
0.0000
67
Total
3886.1607
1.0000
237089.4310 0.0000 237229.5669
0.9994 0.0000 1.0000
15963.2877 0.0000 15974.4240
0.9993 0.0000 1.0000
68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 330 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: MEA.. (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10 11
COMPONENTS
MIXED
LIGHT
HEAVY
12
CO
1620
1620
---
13
H2O
15.05
15.05
---
14
Oxygen
874.3
874.3
---
15
Methane
625.2
625.2
---
---
---
---
16
H2S
17
Hydrogen
1984
1984
---
18
Ethane
210.2
210.2
---
19
Propane
---
---
---
20
CO2
249.0
249.0
---
21
Nitrogen
1484
1484
---
---
---
---
22
Air
23
Mercury
---
---
---
24
MEAmine
0.8563
0.8563
---
25
Ammonia
---
---
---
26
UNIT OPERATIONS
27 28
FEED TO
PRODUCT FROM
29
Recycle:
LOGICAL CONNECTION RCY-5
30
UTILITIES
31 32
( No utilities reference this stream )
33
PROCESS UTILITY
34 35 36
DYNAMICS
37 38
Pressure Specification
(Inactive):
39
Flow Specification
(Inactive) Molar:
* 15.00 psia * Mass: 5020 lbmole/hr
40
3.033e+005 lb/hrStd Ideal Liq Volume: 2.054e+004 barrel/day
User Variables
41 42
NOTES
43 44 45
Description
46 47 48
Material Stream: NH3
49 50 51
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
52 53
Overall
54
Vapour / Phase Fraction
55
Temperature:
56
Pressure:
57
Molar Flow
58
Mass Flow
59
Std Ideal Liq Vol Flow
60
Molar Enthalpy
(Btu/lbmole)
61
Molar Entropy
(Btu/lbmole-F)
62
Heat Flow
63
Liq Vol Flow @Std Cond
Liquid Phase 0.0000
1.0000
(F)
79.29
79.29
(psia)
229.7
229.7
250.4
250.4
(lbmole/hr) (lb/hr) (barrel/day)
(Btu/hr)
4339
4339
483.2
483.2
-3.038e+004 19.86 -7.606e+006 482.5*
(barrel/day)
64
-3.038e+004 19.86 -7.606e+006 482.5
PROPERTIES
65 66
Overall
67
Molecular Weight
68
Molar Density
69
Aspen Technology Inc. Licensed to: LEGENDS
(lbmole/ft3)
Liquid Phase 17.33
17.33
2.161
2.161
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 331 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: NH3 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Mass Density
13
Act. Volume Flow
14
(lb/ft3)
Liquid Phase 37.47
37.47
(barrel/day)
495.1
495.1
Mass Enthalpy
(Btu/lb)
-1753
-1753
15
Mass Entropy
(Btu/lb-F)
1.146
1.146
16
Heat Capacity
20.45
20.45
17
Mass Heat Capacity
18
LHV Molar Basis (Std)
(Btu/lbmole)
1.380e+005
1.380e+005
19
HHV Molar Basis (Std)
(Btu/lbmole)
1.644e+005
1.644e+005
20
HHV Mass Basis (Std)
21
CO2 Loading
22
CO2 App ML Con
(lbmole/ft3)
1.336e-002
1.336e-002
23
CO2 App WT Con
(lbmol/lb)
3.567e-004
3.567e-004
24
LHV Mass Basis (Std)
25
(Btu/lbmole-F) (Btu/lb-F)
(Btu/lb)
(Btu/lb)
1.180
1.180
9487
9487
14.19
14.19
7964
7964
Phase Fraction [Vol. Basis]
0.0000
1.000
26
Phase Fraction [Mass Basis]
0.0000
1.000
27
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
28
Mass Exergy
(Btu/lb)
135.7
---
29
Partial Pressure of CO2
(psia)
0.0000
---
30
Cost Based on Flow
(Cost/s)
0.0000
0.0000
31
Act. Gas Flow
32
Avg. Liq. Density
33 34 35
Std. Ideal Liq. Mass Density
36
Act. Liq. Flow
37
Z Factor
38
Watson K
39
User Property
40
Partial Pressure of H2S
41
Cp/(Cp - R)
42
Cp/Cv
43
Heat of Vap.
44
Kinematic Viscosity
45
Liq. Mass Density (Std. Cond)
46
Liq. Vol. Flow (Std. Cond)
47
Liquid Fraction
48
Molar Volume
49
Mass Heat of Vap.
50
Phase Fraction [Molar Basis]
51
Surface Tension
52
Thermal Conductivity
53
Viscosity
54
Cv (Semi-Ideal)
55
Mass Cv (Semi-Ideal)
56
Cv
57
Mass Cv
58
Cv (Ent. Method)
59
Mass Cv (Ent. Method)
60
Cp/Cv (Ent. Method)
61
Reid VP at 37.8 C
62
True VP at 37.8 C
63
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
64
Viscosity Index
(ACFM)
---
---
(lbmole/ft3)
2.215
2.215
Specific Heat
(Btu/lbmole-F)
20.45
20.45
Std. Gas Flow
(MMSCFD)
2.276
2.276
(lb/ft3)
38.39
38.39
(USGPS)
0.2407
0.2407
1.837e-002
(psia)
(Btu/lbmole)
1.837e-002
12.27
12.27
---
---
0.0000
---
1.108
1.108
2.319
2.319
9450
---
(cSt)
0.2063
0.2063
(lb/ft3)
38.45
38.45
482.5
482.5
(barrel/day) (ft3/lbmole) (Btu/lb)
1.000
1.000
0.4626
0.4626
545.2
---
0.0000
1.0000
(dyne/cm)
25.66
25.66
(Btu/hr-ft-F)
0.2688
0.2688
0.1238
0.1238
18.47
18.47
1.065
1.065
(cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
8.820
8.820
0.5088
0.5088
5.954
---
0.3435
---
3.435
---
(psia)
234.0
234.0
(psia)
287.9
287.9
482.5
482.5
-62.73
---
65 66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 332 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: NH3 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Overall Phase
12 13
COMPONENTS
14
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
0.0000
LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
16
H2O
1.8304
0.0073
32.9751
0.0076
2.2625
0.0047
17
Oxygen
0.3767
0.0015
12.0553
0.0028
0.7256
0.0015
18
Methane
0.4555
0.0018
7.3074
0.0017
1.6712
0.0035
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0215
0.0001
0.0433
0.0000
0.0425
0.0001
21
Ethane
1.7337
0.0069
52.1314
0.0120
10.0359
0.0208
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
1.5480
0.0062
68.1279
0.0157
5.6521
0.0117
24
Nitrogen
0.0074
0.0000
0.2077
0.0000
0.0176
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.1091
0.0004
6.6643
0.0015
0.4487
0.0009
28
Ammonia
244.2724
0.9757
4159.9584
0.9586
462.3567
0.9568
29
Total
250.3547
1.0000
4339.4720
1.0000
483.2129
1.0000
30
Liquid Phase
31 32
COMPONENTS
33
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
34
CO
0.0000
0.0000
0.0011
0.0000
0.0001
0.0000
35
H2O
1.8304
0.0073
32.9751
0.0076
2.2625
0.0047
36
Oxygen
0.3767
0.0015
12.0553
0.0028
0.7256
0.0015
37
Methane
0.4555
0.0018
7.3074
0.0017
1.6712
0.0035
38
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Hydrogen
0.0215
0.0001
0.0433
0.0000
0.0425
0.0001
40
Ethane
1.7337
0.0069
52.1314
0.0120
10.0359
0.0208
41
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
CO2
1.5480
0.0062
68.1279
0.0157
5.6521
0.0117
43
Nitrogen
0.0074
0.0000
0.2077
0.0000
0.0176
0.0000
44
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
MEAmine
0.1091
0.0004
6.6643
0.0015
0.4487
0.0009
47
Ammonia
244.2724
0.9757
4159.9584
0.9586
462.3567
0.9568
48
Total
250.3547
1.0000
4339.4720
1.0000
483.2129
1.0000
49
K VALUE
50 51
COMPONENTS
MIXED
LIGHT
HEAVY
52
CO
0.0000
0.0000
---
53
H2O
0.0000
0.0000
---
54
Oxygen
0.0000
0.0000
---
55
Methane
0.0000
0.0000
---
---
---
---
56
H2S
57
Hydrogen
0.0000
0.0000
---
58
Ethane
0.0000
0.0000
---
59
Propane
---
---
---
60
CO2
0.0000
0.0000
---
61
Nitrogen
0.0000
0.0000
---
---
---
---
62
Air
63
Mercury
---
---
---
64
MEAmine
0.0000
0.0000
---
65
Ammonia
0.0000
0.0000
---
66 67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 333 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: NH3 (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10 11
FEED TO
PRODUCT FROM
12
Mixer:
LOGICAL CONNECTION MIX-108
13
UTILITIES
14 15
( No utilities reference this stream )
16
PROCESS UTILITY
17 18 19
DYNAMICS
20 21
Pressure Specification
(Inactive):
22
Flow Specification
(Inactive) Molar:
229.7 psia 250.4 lbmole/hrMass:
23
4339 lb/hr Std Ideal Liq Volume:
483.2 barrel/day
User Variables
24 25
NOTES
26 27 28
Description
29 30 31
Material Stream: Vapor de agua
32 33 34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35 36
Overall
Vapour Phase
37
Vapour / Phase Fraction
38
Temperature:
39
Pressure:
40
Molar Flow
41
Mass Flow
42
Std Ideal Liq Vol Flow
(barrel/day)
43
Molar Enthalpy
(Btu/lbmole)
3041
3041
44
Molar Entropy
(Btu/lbmole-F)
32.72
32.72
45
Heat Flow
(Btu/hr)
0.0000
0.0000
46
Liq Vol Flow @Std Cond
(barrel/day)
* 0.0000
0.0000
1.0000
1.0000
(F)
500.0*
500.0
(psia)
314.7*
314.7
* 0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
(lbmole/hr) (lb/hr)
47
PROPERTIES
48 49
Overall
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Act. Volume Flow
54
Vapour Phase 32.00
(lbmole/ft3) (lb/ft3)
3.047e-002
32.00 3.047e-002
0.9751
0.9751
(barrel/day)
0.0000
0.0000
Mass Enthalpy
(Btu/lb)
95.04
95.04
55
Mass Entropy
(Btu/lb-F)
1.022
1.022
56
Heat Capacity
57
Mass Heat Capacity
58 59 60
HHV Mass Basis (Std)
61
CO2 Loading
62
CO2 App ML Con
63
CO2 App WT Con
64
LHV Mass Basis (Std)
65 66 67
Phase Fraction [Act. Vol. Basis]
68
Mass Exergy
69
Aspen Technology Inc.
7.588
7.588
(Btu/lb-F)
0.2371
0.2371
LHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
HHV Molar Basis (Std)
(Btu/lbmole)
0.0000
0.0000
0.0000
0.0000
---
---
(lbmole/ft3)
---
---
(lbmol/lb)
---
---
(Btu/lb)
0.0000
0.0000
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
---
---
Licensed to: LEGENDS
(Btu/lbmole-F)
(Btu/lb)
(Btu/lb)
127.3
---
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 334 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Vapor de agua (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10 11
Overall
12
Partial Pressure of CO2
13
Cost Based on Flow
14
Act. Gas Flow
15
Avg. Liq. Density
16
Vapour Phase
(psia)
0.0000
---
(Cost/s)
0.0000
0.0000 0.0000
(ACFM)
0.0000
(lbmole/ft3)
---
---
Specific Heat
(Btu/lbmole-F)
7.588
7.588
17
Std. Gas Flow
(MMSCFD)
18
Std. Ideal Liq. Mass Density
19
Act. Liq. Flow
20
0.0000
0.0000
(lb/ft3)
71.02
71.02
(USGPS)
---
---
Z Factor
1.003
1.003
21
Watson K
4.786
4.786
22
User Property
---
---
23
Partial Pressure of H2S
24
Cp/(Cp - R)
25
Cp/Cv
26
Heat of Vap.
27
Kinematic Viscosity
28
Liq. Mass Density (Std. Cond)
29
Liq. Vol. Flow (Std. Cond)
30
Liquid Fraction
31
Molar Volume
32
Mass Heat of Vap.
33
Phase Fraction [Molar Basis]
34
Surface Tension
35
Thermal Conductivity
36
Viscosity
37
Cv (Semi-Ideal)
38
Mass Cv (Semi-Ideal)
39
Cv
40
Mass Cv
41
Cv (Ent. Method)
42
Mass Cv (Ent. Method)
43
Cp/Cv (Ent. Method)
44
Reid VP at 37.8 C
45
True VP at 37.8 C
46 47
(psia)
(Btu/lbmole) (cSt) (lb/ft3)
0.0000
---
1.354
1.354
1.369
1.369
1935
---
2.075
2.075
8.458e-002
(barrel/day)
8.458e-002
0.0000
0.0000
0.0000
0.0000
(ft3/lbmole)
32.82
32.82
(Btu/lb)
60.48
---
1.0000
1.0000
(dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F)
---
---
2.537e-002
2.537e-002
3.241e-002
3.241e-002
5.602
5.602
0.1751
0.1751
5.543
5.543
0.1732
0.1732
---
---
---
---
---
---
(psia)
---
---
(psia)
---
---
Liq. Vol. Flow - Sum(Std. Cond) (barrel/day)
0.0000
0.0000
Viscosity Index
-20.27
---
(Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F)
48
COMPOSITION
49 50
Overall Phase
51 52
COMPONENTS
53
MOLAR FLOW (lbmole/hr)
MOLE FRACTION
MASS FLOW (lb/hr)
Vapour Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.0000
LIQUID VOLUME FRACTION
54
CO
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
55
H2O
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
56
Oxygen
* 0.0000
* 1.0000
* 0.0000
* 1.0000
* 0.0000
* 1.0000
57
Methane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
58
H2S
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
59
Hydrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
60
Ethane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
61
Propane
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
62
CO2
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
63
Nitrogen
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
64
Air
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
65
Mercury
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
66
MEAmine
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
67
Ammonia
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
* 0.0000
68
Total
0.0000
1.0000
0.0000
1.0000
0.0000
69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
1.0000
Page 335 of 336 * Specified by user.
1 2
LEGENDS Bedford, MA USA
3 4 5
Case Name:
Jose maria ayala.hsc
Unit Set:
NewUser4
Date/Time:
Fri Dec 21 15:56:41 2018
6
Material Stream: Vapor de agua (continued)
7 8 9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10 11
Vapour Phase
12 13
COMPONENTS
MOLAR FLOW (lbmole/hr)
14
MOLE FRACTION
MASS FLOW (lb/hr)
Phase Fraction MASS FRACTION
LIQUID VOLUME FLOW (barrel/day)
1.000 LIQUID VOLUME FRACTION
15
CO
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
Oxygen
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
H2S
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
21
Ethane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Propane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
CO2
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
24
Nitrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Air
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Mercury
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
MEAmine
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ammonia
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Total
0.0000
1.0000
0.0000
1.0000
0.0000
1.0000
30
K VALUE
31 32
COMPONENTS
MIXED
LIGHT
HEAVY
33
CO
---
---
---
34
H2O
---
---
---
35
Oxygen
---
---
---
36
Methane
---
---
---
---
---
---
37
H2S
38
Hydrogen
---
---
---
39
Ethane
---
---
---
40
Propane
---
---
---
41
CO2
---
---
---
42
Nitrogen
---
---
---
---
---
---
43
Air
44
Mercury
---
---
---
45
MEAmine
---
---
---
46
Ammonia
---
---
---
47
UNIT OPERATIONS
48 49 50
FEED TO
PRODUCT FROM
Distillation:
LOGICAL CONNECTION
T-7
51
UTILITIES
52 53
( No utilities reference this stream )
54
PROCESS UTILITY
55 56 57
DYNAMICS
58 59
Pressure Specification
(Active):
60
Flow Specification
(Active)
61
* 314.7 psia
Molar:
* Mass: 0.0000 lbmole/hr
0.0000 lb/hr Std Ideal Liq Volume:
0.0000 barrel/day
User Variables
62 63
NOTES
64 65 66
Description
67 68 69
Aspen Technology Inc. Licensed to: LEGENDS
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 336 of 336 * Specified by user.
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