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Lampiran I Data Perhitungan Data Komposisi Desain Absorber 201-E Tabel 27.Komposisi Natural Gas Inlet Absorber (201-E) Secara Desain Komponen CO2 CH4 C2H6 C3H8 C4H10
Parameter
Hasil 140,61 1076,89 75,71 47,28 14,91 2869,23 96,00 27,73 19,69
Mass Flow Temperatur (T) Tekanan (P) Densitas (ρ)
Satuan Kmol/hr Kmol/hr Kmol/hr Kmol/hr Kmol/hr Kg/hr o C Bar Kg/m3
Sumber : Data Ammonia Optimisation Project, Absorber Plant Feed Treating P – III, 1990
Tabel 28.Komposisi Natural Gas Outlet Absorber (201-E) Secara Desain Komponen CO2 CH4 C2H6 C3H8 C4H10
Parameter
Hasil 3,63 1075,50 75,60 47,21 14,89 22687,36 35,00 27,00 20,76
Mass Flow Temperatur (T) Tekanan (P) Densitas (ρ)
Satuan Kmol/hr Kmol/hr Kmol/hr Kmol/hr Kmol/hr Kg/hr o C Bar Kg/m3
Sumber : Data Ammonia Optimisation Project, Absorber Plant Feed Treating P – III, 1990
Tabel 29.Komposisi Lean Benfield Inlet Absorber (201-E) Secara Desain Komponen K2CO3 V2O5 DEA H2O
Parameter
Hasil 30 0,5 3 66,5 179535 129 27,3 1173
Mass Flow Temperatur (T) Tekanan (P) Densitas (ρ)
Satuan %Wt %Wt %Wt %Wt Kg/hr o C Kg/Cm2 Kg/m3
Sumber : Data Ammonia Optimisation Project, Absorber Plant Feed Treating P – III, 1990
89
Data Komposisi Aktual Absorber 201-E Tabel 30.Gas Alam GMS PERTAMINA PUSRI III ( 1 JUNI2017 ) Parameter H2S Ar N2 H2 CO2 CH4 C2H6 C3H8 Iso-C4H10 n- C4H10 Iso-C5H12 n- C5H12 C6H14 Plus Specific Gravity Calculation Gross Heating Value
Metoda Volumetri
Hasil 8,85 0,28
GPA-Standard P, 2261 – 86 P, 2172 – 86
7,03 84,26 5,88 1,45 0,30 0,33 0,13 0,08 0,26 0,6774 1023,4103
Satuan Ppm %vol %vol %vol %vol %vol %vol %vol %vol %vol %vol %vol %vol BTU/Cuft
Sumber : Teknik Proses P – III, 2017
Tabel 31.Data Analisis Laboratorium Kandungan Lean Benfield
K2CO3
Komponen V2O5 DEA
1Juni 2017
20,95%
0,89%
1,46%
76,70%
2
5Juni 2017
16,55%
0,87%
1,46%
81,12%
3
8Juni 2017
15,84%
0,89%
1,49%
81,78%
4
12Juni 2017
17,04%
0,86%
1,60%
80,50%
5
15 Juni 2017
16,15%
0,83%
1,58%
81,44%
No.
Tanggal
1
H2O
Sumber : Data Analisis komposisi Benfield input Absorber Plant Feed Treating P – III, 2017
Tabel 32.Data Laju Alir Natural Gas Inlet Absorber No. 1 2 3 4 5
Tanggal 1Juni 2017 5Juni 2017 8Juni 2017 12Juni 2017 15Juni 2017
Laju Alir (Nm3/hr) 212,32 212,33 212,32 212,33 212,33
Sumber : Log sheet data harian jumlah flow fluida, pada Absorber Plant Feed Treating P – III
90
Tabel 33.Data Laju Alir Lean Benfield Inlet Absorber No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Laju Alir (Nm3/hr) 165,99 165,99 165,98 165,99 165,98
Sumber : Log sheet data harian jumlah flow fluida, pada Absorber Plant Feed Treating P – III
Tabel 34.Data Analisis Laboratorium Spesific Gravity (SG) Benfield No. 1 2 3 4 5
Tanggal 1 Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
SG Larutan Benfield 1,230 1,226 1,234 1,230 1,220
Sumber : Teknik Proses P – III, 2017
Tabel 35. Data Suhu Inlet Natural Gas Absorber No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Suhu(℃) 37,78 37,78 37,78 37,78 37,78
Sumber : Log sheet data harian suhu inlet natural gas pada Absorber Plant Feed Treating P – III
91
Tabel 36.Data Suhu Outlet Natural Gas Absorber No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Suhu(℃) 54,45 55,00 56,11 55,56 55,00
Sumber : Log sheet data harian suhu outlet natural gas pada Absorber Plant Feed Treating P – III
Tabel 37. Data Suhu Inlet Lean Benfield Tengah No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Suhu(℃) 77 81 81 83 82
Sumber : Log sheet dataharian suhu inlet lean Benfield tengah, pada Absorber Plant Feed Treating P – III
Tabel 38.Data Suhu Inlet Lean Benfield Atas No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Suhu(℃) 100 100 100 100 100
Sumber : Log sheet data harian suhu inlet lean Benfield bawah, pada Absorber Plant Feed Treating P – III
92
Tabel 39.Data Suhu Output Lean Benfield No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Suhu(℃) 117 116 117 118 117
Sumber : Log sheet data harian suhu lean Benfield , pada Absorber Plant Feed Treating P – III
Mengetahui, Asisten Superintenden Amonia P – III
M.RioRinaldi Badge No.11.2516
93
Parameter
Hasil 140,61 1076,89 75,71 47,28 14,91 2869,23 96,00 27,73 19,69
Mass Flow Temperatur (T) Tekanan (P) Densitas (ρ)
Satuan Kmol/hr Kmol/hr Kmol/hr Kmol/hr Kmol/hr Kg/hr o C Bar Kg/m3
Sumber : Data Ammonia Optimisation Project, Absorber Plant Feed Treating P – III, 1990
Tabel 28.Komposisi Natural Gas Outlet Absorber (201-E) Secara Desain Komponen CO2 CH4 C2H6 C3H8 C4H10
Parameter
Hasil 3,63 1075,50 75,60 47,21 14,89 22687,36 35,00 27,00 20,76
Mass Flow Temperatur (T) Tekanan (P) Densitas (ρ)
Satuan Kmol/hr Kmol/hr Kmol/hr Kmol/hr Kmol/hr Kg/hr o C Bar Kg/m3
Sumber : Data Ammonia Optimisation Project, Absorber Plant Feed Treating P – III, 1990
Tabel 29.Komposisi Lean Benfield Inlet Absorber (201-E) Secara Desain Komponen K2CO3 V2O5 DEA H2O
Parameter
Hasil 30 0,5 3 66,5 179535 129 27,3 1173
Mass Flow Temperatur (T) Tekanan (P) Densitas (ρ)
Satuan %Wt %Wt %Wt %Wt Kg/hr o C Kg/Cm2 Kg/m3
Sumber : Data Ammonia Optimisation Project, Absorber Plant Feed Treating P – III, 1990
89
Data Komposisi Aktual Absorber 201-E Tabel 30.Gas Alam GMS PERTAMINA PUSRI III ( 1 JUNI2017 ) Parameter H2S Ar N2 H2 CO2 CH4 C2H6 C3H8 Iso-C4H10 n- C4H10 Iso-C5H12 n- C5H12 C6H14 Plus Specific Gravity Calculation Gross Heating Value
Metoda Volumetri
Hasil 8,85 0,28
GPA-Standard P, 2261 – 86 P, 2172 – 86
7,03 84,26 5,88 1,45 0,30 0,33 0,13 0,08 0,26 0,6774 1023,4103
Satuan Ppm %vol %vol %vol %vol %vol %vol %vol %vol %vol %vol %vol %vol BTU/Cuft
Sumber : Teknik Proses P – III, 2017
Tabel 31.Data Analisis Laboratorium Kandungan Lean Benfield
K2CO3
Komponen V2O5 DEA
1Juni 2017
20,95%
0,89%
1,46%
76,70%
2
5Juni 2017
16,55%
0,87%
1,46%
81,12%
3
8Juni 2017
15,84%
0,89%
1,49%
81,78%
4
12Juni 2017
17,04%
0,86%
1,60%
80,50%
5
15 Juni 2017
16,15%
0,83%
1,58%
81,44%
No.
Tanggal
1
H2O
Sumber : Data Analisis komposisi Benfield input Absorber Plant Feed Treating P – III, 2017
Tabel 32.Data Laju Alir Natural Gas Inlet Absorber No. 1 2 3 4 5
Tanggal 1Juni 2017 5Juni 2017 8Juni 2017 12Juni 2017 15Juni 2017
Laju Alir (Nm3/hr) 212,32 212,33 212,32 212,33 212,33
Sumber : Log sheet data harian jumlah flow fluida, pada Absorber Plant Feed Treating P – III
90
Tabel 33.Data Laju Alir Lean Benfield Inlet Absorber No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Laju Alir (Nm3/hr) 165,99 165,99 165,98 165,99 165,98
Sumber : Log sheet data harian jumlah flow fluida, pada Absorber Plant Feed Treating P – III
Tabel 34.Data Analisis Laboratorium Spesific Gravity (SG) Benfield No. 1 2 3 4 5
Tanggal 1 Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
SG Larutan Benfield 1,230 1,226 1,234 1,230 1,220
Sumber : Teknik Proses P – III, 2017
Tabel 35. Data Suhu Inlet Natural Gas Absorber No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Suhu(℃) 37,78 37,78 37,78 37,78 37,78
Sumber : Log sheet data harian suhu inlet natural gas pada Absorber Plant Feed Treating P – III
91
Tabel 36.Data Suhu Outlet Natural Gas Absorber No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Suhu(℃) 54,45 55,00 56,11 55,56 55,00
Sumber : Log sheet data harian suhu outlet natural gas pada Absorber Plant Feed Treating P – III
Tabel 37. Data Suhu Inlet Lean Benfield Tengah No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Suhu(℃) 77 81 81 83 82
Sumber : Log sheet dataharian suhu inlet lean Benfield tengah, pada Absorber Plant Feed Treating P – III
Tabel 38.Data Suhu Inlet Lean Benfield Atas No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Suhu(℃) 100 100 100 100 100
Sumber : Log sheet data harian suhu inlet lean Benfield bawah, pada Absorber Plant Feed Treating P – III
92
Tabel 39.Data Suhu Output Lean Benfield No. 1 2 3 4 5
Tanggal 1Juni 2017 5 Juni 2017 8 Juni 2017 12 Juni 2017 15 Juni 2017
Suhu(℃) 117 116 117 118 117
Sumber : Log sheet data harian suhu lean Benfield , pada Absorber Plant Feed Treating P – III
Mengetahui, Asisten Superintenden Amonia P – III
M.RioRinaldi Badge No.11.2516
93
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