1

Case Name: Gas Composition.hsc

2 PT PERTAMINA EP
3 Bedford, MA Unit Set: Field
4 USA
Date/Time: Wed Sep 27 15:22:39 2023
5
6
Fluid Package: Basis-1
7 Material Stream: To 24 Inch 46 KM Property Package: Peng-Robinson
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9
10
CONDITIONS
11 Overall Vapour Phase Aqueous Phase
12 Vapour / Phase Fraction 1.0000 1.0000 0.0000
13 Temperature: (F) 71.60 71.60 71.60
14 Pressure: (psia) 81.00 81.00 81.00
15 Molar Flow (lbmole/hr) 3310 3310 0.0000
16 Mass Flow (lb/hr) 5.383e+004 5.383e+004 0.0000
17 Std Ideal Liq Vol Flow (barrel/day) 1.211e+004 1.211e+004 0.0000
18 Molar Enthalpy (Btu/lbmole) -3.269e+004 -3.269e+004 -1.231e+005
19 Molar Entropy (Btu/lbmole-F) 40.47 40.47 12.64
20 Heat Flow (Btu/hr) -1.082e+008 -1.082e+008 0.0000
21 Liq Vol Flow @Std Cond (barrel/day) 5.345e+006 * 5.345e+006 0.0000
22
23
PROPERTIES
24 Overall Vapour Phase Aqueous Phase
25 Molecular Weight 16.26 16.26 18.02
26 Molar Density (lbmole/ft3) 1.439e-002 1.439e-002 2.948
27 Mass Density (lb/ft3) 0.2340 0.2340 53.12
28 Act. Volume Flow (barrel/day) 9.833e+005 9.833e+005 0.0000
29 Mass Enthalpy (Btu/lb) -2010 -2010 -6836
30 Mass Entropy (Btu/lb-F) 2.488 2.488 0.7015
31 Heat Capacity (Btu/lbmole-F) 8.704 8.704 18.56
32 Mass Heat Capacity (Btu/lb-F) 0.5352 0.5352 1.030
33 LHV Molar Basis (Std) (Btu/lbmole) 3.415e+005 3.415e+005 8.272e-003
34 HHV Molar Basis (Std) (Btu/lbmole) 3.764e+005 3.764e+005 1.763e+004
35 HHV Mass Basis (Std) (Btu/lb) 2.315e+004 2.315e+004 978.7
36 CO2 Loading --- --- ---
37 CO2 Apparent Mole Conc. (lbmole/ft3) --- --- ---
38 CO2 Apparent Wt. Conc. (lbmol/lb) --- --- ---
39 LHV Mass Basis (Std) (Btu/lb) 2.100e+004 2.100e+004 4.592e-004
40 Phase Fraction [Vol. Basis] 1.000 1.000 ---
41 Phase Fraction [Mass Basis] 1.000 1.000 0.0000
42 Phase Fraction [Act. Vol. Basis] 1.000 1.000 0.0000
43 Mass Exergy (Btu/lb) 111.2 --- ---
44 Partial Pressure of CO2 (psia) 0.1612 --- ---
45 Cost Based on Flow (Cost/s) 0.0000 0.0000 0.0000
46 Act. Gas Flow (ACFM) 3834 3834 ---
47 Avg. Liq. Density (lbmole/ft3) 1.169 1.169 3.458
48 Specific Heat (Btu/lbmole-F) 8.704 8.704 18.56
49 Std. Gas Flow (MMSCFD) 30.09 30.09 0.0000
50 Std. Ideal Liq. Mass Density (lb/ft3) 19.00 19.00 62.30
51 Act. Liq. Flow (USGPM) 0.0000 --- 0.0000
52 Z Factor --- 0.9873 4.818e-003
53 Watson K 19.29 19.29 8.408
54 User Property --- --- ---
55 Partial Pressure of H2S (psia) 0.0000 --- ---
56 Cp/(Cp - R) 1.296 1.296 1.120
57 Cp/Cv 1.319 1.319 1.145
58 Ideal Gas Cp/Cv 1.302 1.302 1.329
59 Ideal Gas Cp (Btu/lbmole-F) 8.570 8.570 8.016
60 Mass Ideal Gas Cp (Btu/lb-F) 0.5270 0.5270 0.4449
61 Heat of Vap. (Btu/lbmole) 5679 --- ---
62 Kinematic Viscosity (cSt) 3.007 3.007 1.122
63 Aspen Technology Inc. Aspen HYSYS Version 14 Page 1 of 4
Licensed to: PT PERTAMINA EP * Specified by user.
1
Case Name: Gas Composition.hsc
2 PT PERTAMINA EP
3 Bedford, MA Unit Set: Field
4 USA
Date/Time: Wed Sep 27 15:22:39 2023
5
6
Fluid Package: Basis-1
7 Material Stream: To 24 Inch 46 KM (continued) Property Package: Peng-Robinson
8
9
10
PROPERTIES
11 Overall Vapour Phase Aqueous Phase
12 Liq. Mass Density (Std. Cond) (lb/ft3) 4.305e-002 4.305e-002 63.35
13 Liq. Vol. Flow (Std. Cond) (barrel/day) 5.345e+006 5.345e+006 0.0000
14 Liquid Fraction 0.0000 0.0000 1.000
15 Molar Volume (ft3/lbmole) 69.50 69.50 0.3392
16 Mass Heat of Vap. (Btu/lb) 349.2 --- ---
17 Phase Fraction [Molar Basis] 1.0000 1.0000 0.0000
18 Surface Tension (dyne/cm) --- --- 72.62
19 Thermal Conductivity (Btu/hr-ft-F) 1.931e-002 1.931e-002 0.3504
20 Bubble Point Pressure (psia) --- --- ---
21 Viscosity (cP) 1.127e-002 1.127e-002 0.9548
22 Cv (Semi-Ideal) (Btu/lbmole-F) 6.718 6.718 16.57
23 Mass Cv (Semi-Ideal) (Btu/lb-F) 0.4131 0.4131 0.9200
24 Cv (Btu/lbmole-F) 6.600 6.600 16.21
25 Mass Cv (Btu/lb-F) 0.4058 0.4058 0.8997
26 Cv (Ent. Method) (Btu/lbmole-F) --- --- ---
27 Mass Cv (Ent. Method) (Btu/lb-F) --- --- ---
28 Cp/Cv (Ent. Method) --- --- ---
29 Reid VP at 37.8 C (psia) --- --- 1.589
30 True VP at 37.8 C (psia) --- --- 1.589
31 Liq. Vol. Flow - Sum(Std. Cond)
(barrel/day) 5.345e+006 5.345e+006 0.0000
32 Viscosity Index -12.12 --- ---
33
34
COMPOSITION
35
36
Overall Phase Vapour Fraction 1.0000

37 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
38 (lbmole/hr) (lb/hr) FLOW (barrel/day) FRACTION
39 Nitrogen 24.3766 0.0074 682.8700 0.0127 57.9849 0.0048
40 CO2 6.5883 0.0020 289.9513 0.0054 24.0552 0.0020
41 Methane 3247.6934 0.9812 52102.9646 0.9679 11916.0706 0.9842
42 Ethane 15.1530 0.0046 455.6554 0.0085 87.7177 0.0072
43 Propane 0.3294 0.0001 14.5263 0.0003 1.9631 0.0002
44 i-Butane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
45 n-Butane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
46 i-Pentane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
47 n-Pentane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
48 H2O 15.7329 0.0048 283.4328 0.0053 19.4464 0.0016
49 Total 3309.8737 1.0000 53829.4004 1.0000 12107.2379 1.0000
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Vapour Phase Phase Fraction 1.000

52 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
53 (lbmole/hr) (lb/hr) FLOW (barrel/day) FRACTION
54 Nitrogen 24.3766 0.0074 682.8700 0.0127 57.9849 0.0048
55 CO2 6.5883 0.0020 289.9513 0.0054 24.0552 0.0020
56 Methane 3247.6934 0.9812 52102.9646 0.9679 11916.0706 0.9842
57 Ethane 15.1530 0.0046 455.6554 0.0085 87.7177 0.0072
58 Propane 0.3294 0.0001 14.5263 0.0003 1.9631 0.0002
59 i-Butane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
60 n-Butane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
61 i-Pentane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
62 n-Pentane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
63 Aspen Technology Inc. Aspen HYSYS Version 14 Page 2 of 4
Licensed to: PT PERTAMINA EP * Specified by user.
1
Case Name: Gas Composition.hsc
2 PT PERTAMINA EP
3 Bedford, MA Unit Set: Field
4 USA
Date/Time: Wed Sep 27 15:22:39 2023
5
6
Fluid Package: Basis-1
7 Material Stream: To 24 Inch 46 KM (continued) Property Package: Peng-Robinson
8
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COMPOSITION
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Vapour Phase (continued) Phase Fraction 1.000

13 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
14 (lbmole/hr) (lb/hr) FLOW (barrel/day) FRACTION
15 H2O 15.7329 0.0048 283.4328 0.0053 19.4464 0.0016
16 Total 3309.8737 1.0000 53829.4004 1.0000 12107.2379 1.0000
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18
Aqueous Phase Phase Fraction 0.0000

19 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
20 (lbmole/hr) (lb/hr) FLOW (barrel/day) FRACTION
21 Nitrogen 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 Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
24 Ethane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
25 Propane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
26 i-Butane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
27 n-Butane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
28 i-Pentane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
29 n-Pentane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
30 H2O 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
31 Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
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K VALUE
34 COMPONENTS MIXED LIGHT HEAVY
35 Nitrogen --- --- ---
36 CO2 --- --- ---
37 Methane --- --- ---
38 Ethane --- --- ---
39 Propane --- --- ---
40 i-Butane --- --- ---
41 n-Butane --- --- ---
42 i-Pentane --- --- ---
43 n-Pentane --- --- ---
44 H2O --- --- ---
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UNIT OPERATIONS
47 FEED TO PRODUCT FROM LOGICAL CONNECTION
48 Separator: V-100
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UTILITIES
51 ( No utilities reference this stream )
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PROCESS UTILITY
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DYNAMICS
57 Pressure Specification (Inactive): 81.00 psia
58 Flow Specification (Inactive) Molar: 3310 lbmole/hr Mass: 5.383e+004 lb/hr Std Ideal Liq Volume:
1.211e+004 barrel/day
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60
User Variables
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NOTES
63 Aspen Technology Inc. Aspen HYSYS Version 14 Page 3 of 4
Licensed to: PT PERTAMINA EP * Specified by user.
1
Case Name: Gas Composition.hsc
2 PT PERTAMINA EP
3 Bedford, MA Unit Set: Field
4 USA
Date/Time: Wed Sep 27 15:22:39 2023
5
6
Fluid Package: Basis-1
7 Material Stream: To 24 Inch 46 KM (continued) Property Package: Peng-Robinson
8
9
10
11
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63 Aspen Technology Inc. Aspen HYSYS Version 14 Page 4 of 4
Licensed to: PT PERTAMINA EP * Specified by user.