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- Words: 1,495
- Pages: 4
1 2
TEAM LND Calgary, Alberta CANADA
3 4 5
Case Name:
C:\DOCUMENTS AND SETTINGS\SARMAD\DESKTOP\HEAT EXCHENGER DESI
Unit Set:
SI
Date/Time:
Mon May 25 00:53:31 2009
6
Heat Exchanger: E-100
7 8 9
PARAMETERS
10 11
Exchanger Design (End Point)
12 13
Tube Side DeltaP:
14
UA:
0.0000 kPa * 1.532e+004 kJ/C-h *
15
Shell Side DeltaP:
0.0000 kPa *
Tolerance:
1.0000e-04 *
Passes:
Tube Side Data
---
Shell Side Data
16
Heat Transfer Coefficient
17
Tube Pressure Drop
18
Fouling
19
Tube Length
20
Tube O.D.
21
Tube Thickness
22
Tube Pitch
50.0000 mm *
23
Orientation
Horizontal
24
Passes Per Shell
25
Tubes Per Shell
26
Layout Angle
27
TEMA Type
--0.00 kPa * 0.00000 C-h-m2/kJ * 6.00 m * 20.00 mm * 2.0000 mm
2* 160 * Triangular (30 degrees) AE L
28
Heat Transfer Coefficient
--0.00 kPa *
Shell Pressure Drop
0.00000 C-h-m2/kJ *
Fouling Shell Passes
1
Shell Series
1* 1*
Shell Parallel Baffle Type
Single 20.00 *
Baffle Cut(%Area) Baffle Orientation
Horizontal
Spacing
800.0000 mm *
Diameter
739.0488 mm *
Area
60.32 m2
SPECS
29 30
Specified Value
31
E-100 Heat Balance
32
E-100 UA
Current Value
Active
Estimate
-3.146e-008 kJ/h
8.740e-012
On
Off
1.532e+004 kJ/C-h
-2.845e-004
On
Off
0.0000 kJ/h 1.532e+004 kJ/C-h *
33
Relative Error
Detailed Specifications
34
E-100 Heat Balance
35 36
Type:
Duty
Pass:
Error
Spec Value:
0.0000 kJ/h
Spec Value:
1.532e+004 kJ/C-h
E-100 UA
37 38
Type:
UA
Pass:
39
Overall
RATING
40 41
Sizing
42
Overall Data
43 44
Configuration
45
# of Shells in Series
1*
Tube Passes per Shell
46
# of Shells in Parallel
1*
Exchange Orientation
47
TEMA Type:
2* Horizontal
A
48
Elevation (Base) E
Calculated Information ---
Overall U254.0 kJ/h-m2-C
Shell DP
0.0000 kPa *
Shell Vol per Shell
50
Tube HT Coeff
---
Overall UA e+004 kJ/C-h *
Tube DP
0.0000 kPa *
Tube Vol per Shell 0.1930 m3
51
Shell Data
52
Shell and Tube Bundle
53
Shell Diameter
54
# of Tubes per Shell
739.0 mm * 160 *
50.00 mm *
Tube Pitch
2.272 m3
HT Area per Shell 60.32 m2
0.0000 C-h-m2/kJ *
Shell Fouling
Tube Layout Angle
55
Triangular (30 degrees) Shell Baffles
Shell Baffle Type
Single
Shell Baffle Orientation
Horizontal
Baffle Cut (%Area)
20.00 *
Baffle Spacing
800.0 mm *
Tube Data
57 58
Dimensions 20.00 mm *
OD
16.00 mm *
ID
60 61
Counter L
Shell HT Coeff
59
0.0000 m
First Tube Pass Flow Direction
49
56
*
Tube Thickness
2.000 mm
Tube Length
---
Wall Density
6.000 m *
Tube Properties Tube Fouling
0.0000 C-h-m2/kJ *
45.00 W/m-K *
Thermal Cond.
62
Wall Cp
---
PROPERTIES
63 64
TUBE IN
65 66
Overall
67
Vapour/Phase Fraction
68
Temperature:
69
Hyprotech Ltd. Licensed to: TEAM LND
Vapour Phase
1.0000 (C)
180.0 *
1.0000 180.0
HYSYS v3.2 (Build 5029)
Page 1 of 4 * Specified by user.
1 2
TEAM LND Calgary, Alberta CANADA
3 4 5
Case Name:
C:\DOCUMENTS AND SETTINGS\SARMAD\DESKTOP\HEAT EXCHENGER DESI
Unit Set:
SI
Date/Time:
Mon May 25 00:53:31 2009
6
Heat Exchanger: E-100 (continued)
7 8 9
TUBE IN
10 11
Overall
12
Pressure:
13
Vapour Phase
(kPa)
101.3 *
Molar Flow
(kgmole/h)
876.4 *
14
Mass Flow
(kg/h)
15
Std Ideal Liq Vol Flow
16
Molar Enthalpy
17
Mass Enthalpy
18
Molar Entropy
19
Mass Entropy
(kJ/kg-C)
3.540
3.540
20
Heat Flow
(kJ/h)
-1.794e+008
-1.794e+008
21
Molar Density
(kgmole/m3)
2.819e-002
2.819e-002
22
Mass Density
(kg/m3)
3.767
3.767
23
Std Ideal Liq Mass Density
(kg/m3)
764.0
764.0
24
Liq Mass Density @Std Cond
(kg/m3)
764.4
764.4
25
Molar Heat Capacity
(kJ/kgmole-C)
300.0
300.0
26
Mass Heat Capacity
(kJ/kg-C)
2.246
2.246
27
Thermal Conductivity
(W/m-K)
2.076e-002
2.076e-002
28
Viscosity
(cP)
7.143e-003
7.143e-003
29
Surface Tension
(dyne/cm)
---
---
30
Molecular Weight
133.6
133.6
31
Z Factor
0.9539
0.9539
1.171e+005
101.3 876.4 1.171e+005
(m3/h)
153.3
153.3
(kJ/kgmole)
-2.047e+005
-2.047e+005
(kJ/kg)
-1532
-1532
(kJ/kgmole-C)
472.9
472.9
32
TUBE OUT
33 34
Overall
35
Vapour/Phase Fraction
36
Temperature:
37
Pressure:
38
Vapour Phase
1.0000
1.0000
(C)
181.0
181.0
(kPa)
101.3
101.3
Molar Flow
(kgmole/h)
876.4
876.4
39
Mass Flow
(kg/h)
1.171e+005
1.171e+005
40
Std Ideal Liq Vol Flow
41
Molar Enthalpy
42
Mass Enthalpy
43
Molar Entropy
44
Mass Entropy
(kJ/kg-C)
3.545
3.545
45
Heat Flow
(kJ/h)
-1.792e+008
-1.792e+008
46
Molar Density
(kgmole/m3)
2.812e-002
2.812e-002
47
Mass Density
(kg/m3)
3.757
3.757
48
Std Ideal Liq Mass Density
(kg/m3)
764.0
764.0
49
Liq Mass Density @Std Cond
(kg/m3)
764.4
764.4
50
Molar Heat Capacity
(kJ/kgmole-C)
300.5
300.5
51
Mass Heat Capacity
(kJ/kg-C)
2.249
2.249
52
Thermal Conductivity
(W/m-K)
2.084e-002
2.084e-002
53
Viscosity
(cP)
7.161e-003
7.161e-003
54
Surface Tension
(dyne/cm)
---
---
55
Molecular Weight
133.6
133.6
56
Z Factor
0.9542
0.9542
(m3/h)
153.3
153.3
(kJ/kgmole)
-2.044e+005
-2.044e+005
(kJ/kg)
-1530
-1530
(kJ/kgmole-C)
473.6
473.6
57
SHELL IN
58 59
Overall
60
Vapour/Phase Fraction
61
Temperature:
62
Pressure:
63
Aqueous Phase
0.0000
1.0000
(C)
198.0 *
198.0
(kPa)
1500 *
1500
Molar Flow
(kgmole/h)
4716 *
64
Mass Flow
(kg/h)
65
Std Ideal Liq Vol Flow
66
Molar Enthalpy
67
Mass Enthalpy
68
Molar Entropy
69
Hyprotech Ltd. Licensed to: TEAM LND
8.496e+004
4716 8.496e+004
(m3/h)
85.13
85.13
(kJ/kgmole)
-2.714e+005
-2.714e+005
(kJ/kg)
-1.507e+004
-1.507e+004
(kJ/kgmole-C)
90.44
90.44
HYSYS v3.2 (Build 5029)
Page 2 of 4 * Specified by user.
1 2
TEAM LND Calgary, Alberta CANADA
3 4 5
Case Name:
C:\DOCUMENTS AND SETTINGS\SARMAD\DESKTOP\HEAT EXCHENGER DESI
Unit Set:
SI
Date/Time:
Mon May 25 00:53:31 2009
6
Heat Exchanger: E-100 (continued)
7 8 9
SHELL IN
10 11
Overall
12
Mass Entropy
13
Heat Flow
14 15
Aqueous Phase
(kJ/kg-C)
5.020
5.020
(kJ/h)
-1.280e+009
-1.280e+009
Molar Density
(kgmole/m3)
47.52
47.52
Mass Density
(kg/m3)
856.0
856.0
16
Std Ideal Liq Mass Density
(kg/m3)
998.0
998.0
17
Liq Mass Density @Std Cond
(kg/m3)
1015
1015
18
Molar Heat Capacity
(kJ/kgmole-C)
87.81
87.81
19
Mass Heat Capacity
(kJ/kg-C)
4.874
4.874
20
Thermal Conductivity
(W/m-K)
0.6660
0.6660
21
Viscosity
(cP)
0.1352
0.1352
22
Surface Tension
(dyne/cm)
38.26
38.26
23
Molecular Weight
24
Z Factor
18.02
18.02
8.059e-003
8.059e-003
25
SHELL OUT
26 27
Overall
28
Vapour/Phase Fraction
29
Temperature:
30
Pressure:
31
Aqueous Phase
0.0000
1.0000
(C)
197.4
197.4
(kPa)
1500
1500
Molar Flow
(kgmole/h)
4716
4716
32
Mass Flow
(kg/h)
8.496e+004
8.496e+004
33
Std Ideal Liq Vol Flow
34
Molar Enthalpy
35
Mass Enthalpy
36
Molar Entropy
37
Mass Entropy
(kJ/kg-C)
5.014
5.014
38
Heat Flow
(kJ/h)
-1.280e+009
-1.280e+009
39
Molar Density
(kgmole/m3)
47.55
47.55
40
Mass Density
(kg/m3)
856.7
856.7
41
Std Ideal Liq Mass Density
(kg/m3)
998.0
998.0
42
Liq Mass Density @Std Cond
(kg/m3)
1015
1015
43
Molar Heat Capacity
(kJ/kgmole-C)
87.71
87.71
44
Mass Heat Capacity
(kJ/kg-C)
4.869
4.869
45
Thermal Conductivity
(W/m-K)
0.6664
0.6664
46
Viscosity
(cP)
0.1357
0.1357
47
Surface Tension
(dyne/cm)
38.41
38.41
48
Molecular Weight
49
Z Factor
(m3/h)
85.13
85.13
(kJ/kgmole)
-2.715e+005
-2.715e+005
(kJ/kg)
-1.507e+004
-1.507e+004
(kJ/kgmole-C)
90.32
90.32
18.02
18.02
8.063e-003
8.063e-003
50
Stream Properties
51 52
TUBE IN
TUBE OUT
SHELL IN
SHELL OUT
53
Vapour Fraction
54
Temperature
180.0 *
181.0
198.0 *
55
Pressure
101.3 *
101.3
1500 *
56
Enthalpy
57
Molar Flow
58
MassFlow
59
Std Ideal Liq Vol Flow
60
HeatFlow
1.0000
1.0000
-2.047e+005
0.0000
-2.044e+005
876.4 *
197.4 1500
-2.714e+005
-2.715e+005
4716 *
876.4
1.171e+005
0.0000
1.171e+005
4716
8.496e+004
8.496e+004
153.3
153.3
85.13
85.13
-1.794e+008
-1.792e+008
-1.280e+009
-1.280e+009
61
DYNAMICS
62 63
Basic Model
64 65
Model Parameters
66 67
Tube Volume
(m3)
0.1000
Shell UA
(kg/h)
---
68
Shell Volume
(m3)
0.1000
Tube UA
(kg/h)
---
69
Hyprotech Ltd. Licensed to: TEAM LND
HYSYS v3.2 (Build 5029)
Page 3 of 4 * Specified by user.
1 2
TEAM LND Calgary, Alberta CANADA
3 4 5
Case Name:
C:\DOCUMENTS AND SETTINGS\SARMAD\DESKTOP\HEAT EXCHENGER DESI
Unit Set:
SI
Date/Time:
Mon May 25 00:53:31 2009
6
Heat Exchanger: E-100 (continued)
7 8 9
Elevation
10
Overall UA
(m)
0.0000
(kJ/C-h)
1.532e+004
11
13
Shell Duty:
---
Tube Duty:
14
16
Shell Side Specification
17
Delta P
(kPa)
0.0000
19
*
Active
k
kg/hr/sqrt(kPa-kg/m3)
---
Not Active
kg/hr/sqrt(kPa-kg/m3)
---
Not Active
Tube Side Specifications
20
Delta P
(kPa)
0.0000
*
Active
22
k
Holdup
23 24
Shell Holdup
25 26
---
Pressure Flow Specifications
15
21
Phase
Accumulation (kgmole/h)
Moles (kgmole)
28
Vapour
0.0000
0.0000
*
0.0000
29
Liquid
0.0000
0.0000
*
0.0000
30
Aqueous
0.0000
0.0000
*
31
Total
0.0000
0.0000
0.0000
Volume (m3)
27
32
Volume (m3)
0.0000
Tube Holdup
33 34
*
0.0000
Summary
12
18
Minimum Flow Scale Factor *
Phase
Accumulation (kgmole/h)
Moles (kgmole)
36
Vapour
0.0000
0.0000
*
0.0000
37
Liquid
0.0000
0.0000
*
0.0000
38
Aqueous
0.0000
0.0000
*
39
Total
0.0000
0.0000
35
40
0.0000
0.0000
HTFS
41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69
Hyprotech Ltd. Licensed to: TEAM LND
HYSYS v3.2 (Build 5029)
Page 4 of 4 * Specified by user.
TEAM LND Calgary, Alberta CANADA
3 4 5
Case Name:
C:\DOCUMENTS AND SETTINGS\SARMAD\DESKTOP\HEAT EXCHENGER DESI
Unit Set:
SI
Date/Time:
Mon May 25 00:53:31 2009
6
Heat Exchanger: E-100
7 8 9
PARAMETERS
10 11
Exchanger Design (End Point)
12 13
Tube Side DeltaP:
14
UA:
0.0000 kPa * 1.532e+004 kJ/C-h *
15
Shell Side DeltaP:
0.0000 kPa *
Tolerance:
1.0000e-04 *
Passes:
Tube Side Data
---
Shell Side Data
16
Heat Transfer Coefficient
17
Tube Pressure Drop
18
Fouling
19
Tube Length
20
Tube O.D.
21
Tube Thickness
22
Tube Pitch
50.0000 mm *
23
Orientation
Horizontal
24
Passes Per Shell
25
Tubes Per Shell
26
Layout Angle
27
TEMA Type
--0.00 kPa * 0.00000 C-h-m2/kJ * 6.00 m * 20.00 mm * 2.0000 mm
2* 160 * Triangular (30 degrees) AE L
28
Heat Transfer Coefficient
--0.00 kPa *
Shell Pressure Drop
0.00000 C-h-m2/kJ *
Fouling Shell Passes
1
Shell Series
1* 1*
Shell Parallel Baffle Type
Single 20.00 *
Baffle Cut(%Area) Baffle Orientation
Horizontal
Spacing
800.0000 mm *
Diameter
739.0488 mm *
Area
60.32 m2
SPECS
29 30
Specified Value
31
E-100 Heat Balance
32
E-100 UA
Current Value
Active
Estimate
-3.146e-008 kJ/h
8.740e-012
On
Off
1.532e+004 kJ/C-h
-2.845e-004
On
Off
0.0000 kJ/h 1.532e+004 kJ/C-h *
33
Relative Error
Detailed Specifications
34
E-100 Heat Balance
35 36
Type:
Duty
Pass:
Error
Spec Value:
0.0000 kJ/h
Spec Value:
1.532e+004 kJ/C-h
E-100 UA
37 38
Type:
UA
Pass:
39
Overall
RATING
40 41
Sizing
42
Overall Data
43 44
Configuration
45
# of Shells in Series
1*
Tube Passes per Shell
46
# of Shells in Parallel
1*
Exchange Orientation
47
TEMA Type:
2* Horizontal
A
48
Elevation (Base) E
Calculated Information ---
Overall U254.0 kJ/h-m2-C
Shell DP
0.0000 kPa *
Shell Vol per Shell
50
Tube HT Coeff
---
Overall UA e+004 kJ/C-h *
Tube DP
0.0000 kPa *
Tube Vol per Shell 0.1930 m3
51
Shell Data
52
Shell and Tube Bundle
53
Shell Diameter
54
# of Tubes per Shell
739.0 mm * 160 *
50.00 mm *
Tube Pitch
2.272 m3
HT Area per Shell 60.32 m2
0.0000 C-h-m2/kJ *
Shell Fouling
Tube Layout Angle
55
Triangular (30 degrees) Shell Baffles
Shell Baffle Type
Single
Shell Baffle Orientation
Horizontal
Baffle Cut (%Area)
20.00 *
Baffle Spacing
800.0 mm *
Tube Data
57 58
Dimensions 20.00 mm *
OD
16.00 mm *
ID
60 61
Counter L
Shell HT Coeff
59
0.0000 m
First Tube Pass Flow Direction
49
56
*
Tube Thickness
2.000 mm
Tube Length
---
Wall Density
6.000 m *
Tube Properties Tube Fouling
0.0000 C-h-m2/kJ *
45.00 W/m-K *
Thermal Cond.
62
Wall Cp
---
PROPERTIES
63 64
TUBE IN
65 66
Overall
67
Vapour/Phase Fraction
68
Temperature:
69
Hyprotech Ltd. Licensed to: TEAM LND
Vapour Phase
1.0000 (C)
180.0 *
1.0000 180.0
HYSYS v3.2 (Build 5029)
Page 1 of 4 * Specified by user.
1 2
TEAM LND Calgary, Alberta CANADA
3 4 5
Case Name:
C:\DOCUMENTS AND SETTINGS\SARMAD\DESKTOP\HEAT EXCHENGER DESI
Unit Set:
SI
Date/Time:
Mon May 25 00:53:31 2009
6
Heat Exchanger: E-100 (continued)
7 8 9
TUBE IN
10 11
Overall
12
Pressure:
13
Vapour Phase
(kPa)
101.3 *
Molar Flow
(kgmole/h)
876.4 *
14
Mass Flow
(kg/h)
15
Std Ideal Liq Vol Flow
16
Molar Enthalpy
17
Mass Enthalpy
18
Molar Entropy
19
Mass Entropy
(kJ/kg-C)
3.540
3.540
20
Heat Flow
(kJ/h)
-1.794e+008
-1.794e+008
21
Molar Density
(kgmole/m3)
2.819e-002
2.819e-002
22
Mass Density
(kg/m3)
3.767
3.767
23
Std Ideal Liq Mass Density
(kg/m3)
764.0
764.0
24
Liq Mass Density @Std Cond
(kg/m3)
764.4
764.4
25
Molar Heat Capacity
(kJ/kgmole-C)
300.0
300.0
26
Mass Heat Capacity
(kJ/kg-C)
2.246
2.246
27
Thermal Conductivity
(W/m-K)
2.076e-002
2.076e-002
28
Viscosity
(cP)
7.143e-003
7.143e-003
29
Surface Tension
(dyne/cm)
---
---
30
Molecular Weight
133.6
133.6
31
Z Factor
0.9539
0.9539
1.171e+005
101.3 876.4 1.171e+005
(m3/h)
153.3
153.3
(kJ/kgmole)
-2.047e+005
-2.047e+005
(kJ/kg)
-1532
-1532
(kJ/kgmole-C)
472.9
472.9
32
TUBE OUT
33 34
Overall
35
Vapour/Phase Fraction
36
Temperature:
37
Pressure:
38
Vapour Phase
1.0000
1.0000
(C)
181.0
181.0
(kPa)
101.3
101.3
Molar Flow
(kgmole/h)
876.4
876.4
39
Mass Flow
(kg/h)
1.171e+005
1.171e+005
40
Std Ideal Liq Vol Flow
41
Molar Enthalpy
42
Mass Enthalpy
43
Molar Entropy
44
Mass Entropy
(kJ/kg-C)
3.545
3.545
45
Heat Flow
(kJ/h)
-1.792e+008
-1.792e+008
46
Molar Density
(kgmole/m3)
2.812e-002
2.812e-002
47
Mass Density
(kg/m3)
3.757
3.757
48
Std Ideal Liq Mass Density
(kg/m3)
764.0
764.0
49
Liq Mass Density @Std Cond
(kg/m3)
764.4
764.4
50
Molar Heat Capacity
(kJ/kgmole-C)
300.5
300.5
51
Mass Heat Capacity
(kJ/kg-C)
2.249
2.249
52
Thermal Conductivity
(W/m-K)
2.084e-002
2.084e-002
53
Viscosity
(cP)
7.161e-003
7.161e-003
54
Surface Tension
(dyne/cm)
---
---
55
Molecular Weight
133.6
133.6
56
Z Factor
0.9542
0.9542
(m3/h)
153.3
153.3
(kJ/kgmole)
-2.044e+005
-2.044e+005
(kJ/kg)
-1530
-1530
(kJ/kgmole-C)
473.6
473.6
57
SHELL IN
58 59
Overall
60
Vapour/Phase Fraction
61
Temperature:
62
Pressure:
63
Aqueous Phase
0.0000
1.0000
(C)
198.0 *
198.0
(kPa)
1500 *
1500
Molar Flow
(kgmole/h)
4716 *
64
Mass Flow
(kg/h)
65
Std Ideal Liq Vol Flow
66
Molar Enthalpy
67
Mass Enthalpy
68
Molar Entropy
69
Hyprotech Ltd. Licensed to: TEAM LND
8.496e+004
4716 8.496e+004
(m3/h)
85.13
85.13
(kJ/kgmole)
-2.714e+005
-2.714e+005
(kJ/kg)
-1.507e+004
-1.507e+004
(kJ/kgmole-C)
90.44
90.44
HYSYS v3.2 (Build 5029)
Page 2 of 4 * Specified by user.
1 2
TEAM LND Calgary, Alberta CANADA
3 4 5
Case Name:
C:\DOCUMENTS AND SETTINGS\SARMAD\DESKTOP\HEAT EXCHENGER DESI
Unit Set:
SI
Date/Time:
Mon May 25 00:53:31 2009
6
Heat Exchanger: E-100 (continued)
7 8 9
SHELL IN
10 11
Overall
12
Mass Entropy
13
Heat Flow
14 15
Aqueous Phase
(kJ/kg-C)
5.020
5.020
(kJ/h)
-1.280e+009
-1.280e+009
Molar Density
(kgmole/m3)
47.52
47.52
Mass Density
(kg/m3)
856.0
856.0
16
Std Ideal Liq Mass Density
(kg/m3)
998.0
998.0
17
Liq Mass Density @Std Cond
(kg/m3)
1015
1015
18
Molar Heat Capacity
(kJ/kgmole-C)
87.81
87.81
19
Mass Heat Capacity
(kJ/kg-C)
4.874
4.874
20
Thermal Conductivity
(W/m-K)
0.6660
0.6660
21
Viscosity
(cP)
0.1352
0.1352
22
Surface Tension
(dyne/cm)
38.26
38.26
23
Molecular Weight
24
Z Factor
18.02
18.02
8.059e-003
8.059e-003
25
SHELL OUT
26 27
Overall
28
Vapour/Phase Fraction
29
Temperature:
30
Pressure:
31
Aqueous Phase
0.0000
1.0000
(C)
197.4
197.4
(kPa)
1500
1500
Molar Flow
(kgmole/h)
4716
4716
32
Mass Flow
(kg/h)
8.496e+004
8.496e+004
33
Std Ideal Liq Vol Flow
34
Molar Enthalpy
35
Mass Enthalpy
36
Molar Entropy
37
Mass Entropy
(kJ/kg-C)
5.014
5.014
38
Heat Flow
(kJ/h)
-1.280e+009
-1.280e+009
39
Molar Density
(kgmole/m3)
47.55
47.55
40
Mass Density
(kg/m3)
856.7
856.7
41
Std Ideal Liq Mass Density
(kg/m3)
998.0
998.0
42
Liq Mass Density @Std Cond
(kg/m3)
1015
1015
43
Molar Heat Capacity
(kJ/kgmole-C)
87.71
87.71
44
Mass Heat Capacity
(kJ/kg-C)
4.869
4.869
45
Thermal Conductivity
(W/m-K)
0.6664
0.6664
46
Viscosity
(cP)
0.1357
0.1357
47
Surface Tension
(dyne/cm)
38.41
38.41
48
Molecular Weight
49
Z Factor
(m3/h)
85.13
85.13
(kJ/kgmole)
-2.715e+005
-2.715e+005
(kJ/kg)
-1.507e+004
-1.507e+004
(kJ/kgmole-C)
90.32
90.32
18.02
18.02
8.063e-003
8.063e-003
50
Stream Properties
51 52
TUBE IN
TUBE OUT
SHELL IN
SHELL OUT
53
Vapour Fraction
54
Temperature
180.0 *
181.0
198.0 *
55
Pressure
101.3 *
101.3
1500 *
56
Enthalpy
57
Molar Flow
58
MassFlow
59
Std Ideal Liq Vol Flow
60
HeatFlow
1.0000
1.0000
-2.047e+005
0.0000
-2.044e+005
876.4 *
197.4 1500
-2.714e+005
-2.715e+005
4716 *
876.4
1.171e+005
0.0000
1.171e+005
4716
8.496e+004
8.496e+004
153.3
153.3
85.13
85.13
-1.794e+008
-1.792e+008
-1.280e+009
-1.280e+009
61
DYNAMICS
62 63
Basic Model
64 65
Model Parameters
66 67
Tube Volume
(m3)
0.1000
Shell UA
(kg/h)
---
68
Shell Volume
(m3)
0.1000
Tube UA
(kg/h)
---
69
Hyprotech Ltd. Licensed to: TEAM LND
HYSYS v3.2 (Build 5029)
Page 3 of 4 * Specified by user.
1 2
TEAM LND Calgary, Alberta CANADA
3 4 5
Case Name:
C:\DOCUMENTS AND SETTINGS\SARMAD\DESKTOP\HEAT EXCHENGER DESI
Unit Set:
SI
Date/Time:
Mon May 25 00:53:31 2009
6
Heat Exchanger: E-100 (continued)
7 8 9
Elevation
10
Overall UA
(m)
0.0000
(kJ/C-h)
1.532e+004
11
13
Shell Duty:
---
Tube Duty:
14
16
Shell Side Specification
17
Delta P
(kPa)
0.0000
19
*
Active
k
kg/hr/sqrt(kPa-kg/m3)
---
Not Active
kg/hr/sqrt(kPa-kg/m3)
---
Not Active
Tube Side Specifications
20
Delta P
(kPa)
0.0000
*
Active
22
k
Holdup
23 24
Shell Holdup
25 26
---
Pressure Flow Specifications
15
21
Phase
Accumulation (kgmole/h)
Moles (kgmole)
28
Vapour
0.0000
0.0000
*
0.0000
29
Liquid
0.0000
0.0000
*
0.0000
30
Aqueous
0.0000
0.0000
*
31
Total
0.0000
0.0000
0.0000
Volume (m3)
27
32
Volume (m3)
0.0000
Tube Holdup
33 34
*
0.0000
Summary
12
18
Minimum Flow Scale Factor *
Phase
Accumulation (kgmole/h)
Moles (kgmole)
36
Vapour
0.0000
0.0000
*
0.0000
37
Liquid
0.0000
0.0000
*
0.0000
38
Aqueous
0.0000
0.0000
*
39
Total
0.0000
0.0000
35
40
0.0000
0.0000
HTFS
41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69
Hyprotech Ltd. Licensed to: TEAM LND
HYSYS v3.2 (Build 5029)
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