1

Case Name: Line Sizing.hsc

2 Company Name Not Available
3 Bedford, MA Unit Set: EuroSI
4 USA
Date/Time: Wed Feb 26 15:53:16 2025
5
6
Fluid Package: Basis-1
7 Material Stream: Normal-13500 kg/hr Property Package: Peng-Robinson
8
9
10
CONDITIONS
11 Overall Vapour Phase
12 Vapour / Phase Fraction 1.0000 1.0000
13 Temperature: (C) 15.00 * 15.00
14 Pressure: (bar) 24.13 * 24.13
15 Molar Flow (kgmole/h) 696.9 696.9
16 Mass Flow (kg/h) 1.350e+004 * 1.350e+004
17 Std Ideal Liq Vol Flow (m3/h) 38.95 38.95
18 Molar Enthalpy (kcal/kgmole) -1.932e+004 -1.932e+004
19 Molar Entropy (kJ/kgmole-C) 156.9 156.9
20 Heat Flow (kcal/h) -1.346e+007 -1.346e+007
21 Liq Vol Flow @Std Cond (m3/h) 1.643e+004 * 1.643e+004
22
23
PROPERTIES
24 Overall Vapour Phase
25 Molecular Weight 19.37 19.37
26 Molar Density (kgmole/m3) 1.087 1.087
27 Mass Density (kg/m3) 21.06 21.06
28 Act. Volume Flow (m3/h) 641.1 641.1
29 Mass Enthalpy (kcal/kg) -997.3 -997.3
30 Mass Entropy (kJ/kg-C) 8.100 8.100
31 Heat Capacity (kJ/kgmole-C) 41.97 41.97
32 Mass Heat Capacity (kJ/kg-C) 2.167 2.167
33 LHV Molar Basis (Std) (kcal/kgmole) 2.039e+005 2.039e+005
34 HHV Molar Basis (Std) (kcal/kgmole) 2.239e+005 2.239e+005
35 HHV Mass Basis (Std) (kcal/kg) 1.156e+004 1.156e+004
36 CO2 Loading --- ---
37 CO2 Apparent Mole Conc. (kgmole/m3) --- ---
38 CO2 Apparent Wt. Conc. (kgmol/kg) --- ---
39 LHV Mass Basis (Std) (kcal/kg) 1.053e+004 1.053e+004
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 (kcal/kg) 95.12 ---
44 Partial Pressure of CO2 (bar) 0.4344 ---
45 Cost Based on Flow (Cost/s) 0.0000 0.0000
46 Act. Gas Flow (ACT_m3/h) 641.1 641.1
47 Avg. Liq. Density (kgmole/m3) 17.89 17.89
48 Specific Heat (kJ/kgmole-C) 41.97 41.97
49 Std. Gas Flow (STD_m3/h) 1.648e+004 1.648e+004
50 Std. Ideal Liq. Mass Density (kg/m3) 346.6 346.6
51 Act. Liq. Flow (m3/s) --- ---
52 Z Factor 0.9266 0.9266
53 Watson K 17.40 17.40
54 User Property --- ---
55 Partial Pressure of H2S (bar) 0.0000 ---
56 Cp/(Cp - R) 1.247 1.247
57 Cp/Cv 1.376 1.376
58 Ideal Gas Cp/Cv 1.276 1.276
59 Ideal Gas Cp (kJ/kgmole-C) 38.44 38.44
60 Mass Ideal Gas Cp (kJ/kg-C) 1.985 1.985
61 Heat of Vap. (kcal/kgmole) 2601 ---
62 Kinematic Viscosity (cSt) 0.5541 0.5541
63 Aspen Technology Inc. Aspen HYSYS Version 14 Page 1 of 15
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Case Name: Line Sizing.hsc
2 Company Name Not Available
3 Bedford, MA Unit Set: EuroSI
4 USA
Date/Time: Wed Feb 26 15:53:16 2025
5
6
Fluid Package: Basis-1
7 Material Stream: Normal-13500 kg/hr (continued)
Property Package: Peng-Robinson
8
9
10
PROPERTIES
11 Overall Vapour Phase
12 Liq. Mass Density (Std. Cond) (kg/m3) 0.8218 0.8218
13 Liq. Vol. Flow (Std. Cond) (m3/h) 1.643e+004 1.643e+004
14 Liquid Fraction 0.0000 0.0000
15 Molar Volume (m3/kgmole) 0.9199 0.9199
16 Mass Heat of Vap. (kcal/kg) 134.3 ---
17 Phase Fraction [Molar Basis] 1.0000 1.0000
18 Surface Tension (dyne/cm) --- ---
19 Thermal Conductivity (W/m-K) 3.202e-002 3.202e-002
20 Bubble Point Pressure (bar) --- ---
21 Viscosity (cP) 1.167e-002 1.167e-002
22 Cv (Semi-Ideal) (kJ/kgmole-C) 33.65 33.65
23 Mass Cv (Semi-Ideal) (kJ/kg-C) 1.737 1.737
24 Cv (kJ/kgmole-C) 30.50 30.50
25 Mass Cv (kJ/kg-C) 1.575 1.575
26 Cv (Ent. Method) (kJ/kgmole-C) --- ---
27 Mass Cv (Ent. Method) (kJ/kg-C) --- ---
28 Cp/Cv (Ent. Method) --- ---
29 Reid VP at 37.8 C (bar) --- ---
30 True VP at 37.8 C (bar) --- ---
31 Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 1.643e+004 1.643e+004
32 Viscosity Index -40.28 ---
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 (kgmole/h) (kg/h) FLOW (m3/h) FRACTION
39 Nitrogen 31.3656 * 0.0450 * 878.6445 * 0.0651 * 1.0896 * 0.0280 *
40 CO2 12.5462 * 0.0180 * 552.1562 * 0.0409 * 0.6690 * 0.0172 *
41 Methane 598.2465 * 0.8584 * 9597.6084 * 0.7109 * 32.0568 * 0.8230 *
42 Ethane 27.8805 * 0.0400 * 838.3648 * 0.0621 * 2.3571 * 0.0605 *
43 Propane 1.4637 * 0.0021 * 64.5460 * 0.0048 * 0.1274 * 0.0033 *
44 i-Butane 4.9488 * 0.0071 * 287.6437 * 0.0213 * 0.5119 * 0.0131 *
45 n-Butane 14.0797 * 0.0202 * 818.3666 * 0.0606 * 1.4032 * 0.0360 *
46 i-Pentane 1.3940 * 0.0020 * 100.5804 * 0.0075 * 0.1613 * 0.0041 *
47 n-Pentane 5.0185 * 0.0072 * 362.0895 * 0.0268 * 0.5750 * 0.0148 *
48 Total 696.9435 1.0000 13500.0000 1.0000 38.9512 1.0000
49
50
Vapour Phase Phase Fraction 1.000

51 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
52 (kgmole/h) (kg/h) FLOW (m3/h) FRACTION
53 Nitrogen 31.3656 0.0450 878.6445 0.0651 1.0896 0.0280
54 CO2 12.5462 0.0180 552.1562 0.0409 0.6690 0.0172
55 Methane 598.2465 0.8584 9597.6084 0.7109 32.0568 0.8230
56 Ethane 27.8805 0.0400 838.3648 0.0621 2.3571 0.0605
57 Propane 1.4637 0.0021 64.5460 0.0048 0.1274 0.0033
58 i-Butane 4.9488 0.0071 287.6437 0.0213 0.5119 0.0131
59 n-Butane 14.0797 0.0202 818.3666 0.0606 1.4032 0.0360
60 i-Pentane 1.3940 0.0020 100.5804 0.0075 0.1613 0.0041
61 n-Pentane 5.0185 0.0072 362.0895 0.0268 0.5750 0.0148
62 Total 696.9435 1.0000 13500.0000 1.0000 38.9512 1.0000
63 Aspen Technology Inc. Aspen HYSYS Version 14 Page 2 of 15
Licensed to: Company Name Not Available * Specified by user.
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Case Name: Line Sizing.hsc
2 Company Name Not Available
3 Bedford, MA Unit Set: EuroSI
4 USA
Date/Time: Wed Feb 26 15:53:16 2025
5
6
Fluid Package: Basis-1
7 Material Stream: Normal-13500 kg/hr (continued)
Property Package: Peng-Robinson
8
9
10
K VALUE
11 COMPONENTS MIXED LIGHT HEAVY
12 Nitrogen --- --- ---
13 CO2 --- --- ---
14 Methane --- --- ---
15 Ethane --- --- ---
16 Propane --- --- ---
17 i-Butane --- --- ---
18 n-Butane --- --- ---
19 i-Pentane --- --- ---
20 n-Pentane --- --- ---
21
22 Line Sizing Manager: Line Sizing Manager-1
23
24
25
SIZING
26 Pipe Tag/Name Line Sizing-1
27 Calculation Type Rating
28 Stream Name Normal-13500 kg/hr @Main
29 FlowMargin (%) 0.00
30 Material Carbon Steel
31 Schedule STD
32 Nominal Diameter 250 mm
33 Inner Diameter (mm) 254.5
34 Wall Thickness (mm) 9.271
35 Roughness (mm) 4.572e-002
36 Force Single Phase Off
37 Sizing Criteria Criteria-1
38 Pressure Gradient (kPa/m) 7.194e-003
39 Velocity Gradient (m/s) 3.501
40 Rho V^2 (kg/m-s2) 258.0
41 Flow Regime Vapour Only
42 Criteria Met? Met
43 Pipe Length (m) 8.000e+004 *
44 Fitting Equivalent Length (m) 0.0000
45 Use Detailed Fittings Off
46 Total Pressure Drop (bar) 5.755
47
48
DETAILS
49 Pipe Tag/Name Line Sizing-1
50 Pressure Gradient Rating
51 Stream Name Normal-13500 kg/hr @Main
52 Upstream Unit Operation Name
53 Upstream Unit Operation Type
54 Downstream Unit Operation Name
55 Downstream Unit Operation Type
56 Vapor Mass Flow Rate (kg/h) 1.350e+004
57 Vapor Molecular Weight 19.37
58 Vapor Mass Density (kg/m3) 21.06
59 Vapor Viscosity (cP) 1.167e-002
60 Vapor Cp/Cv 1.376
61 Vapor Z Factor 0.9266
62 Liquid Mass Flow Rate (kg/h) ---
63 Aspen Technology Inc. Aspen HYSYS Version 14 Page 3 of 15
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Case Name: Line Sizing.hsc
2 Company Name Not Available
3 Bedford, MA Unit Set: EuroSI
4 USA
Date/Time: Wed Feb 26 15:53:16 2025
5
6
7 Line Sizing Manager: Line Sizing Manager-1 (continued)
8
9
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DETAILS
11 Liquid Molecular Weight 19.37
12 Liquid Mass Density (kg/m3) ---
13 Liquid Viscosity (cP) ---
14 Flow Margin (%) 0.00
15 Pipe Material Carbon Steel
16 Schedule STD
17 Pipe Nominal Diameter 250 mm
18 Pipe Inside Diameter (mm) 254.5
19 Pipe Wall Thickness (mm) 9.271
20 Pipe Roughness (mm) 4.572e-002
21 Force Single Phase Off
22 Sizing Criteria Criteria-1
23 Pressure Gradient (kPa/m) 7.194e-003
24 Criteria Pressure Gradient (kPa/m) 9.193e-003
25 Velocity (m/s) 3.501
26 Criteria Velocity (m/s) ---
27 Rho V^2 (kg/m-s2) 258.0
28 Criteria Rho V^2 (kg/m-s2) ---
29 Flow Regime Vapour Only
30 Criteria Met or Failed? Met
31 Pipe Length (m) 8.000e+004 *
32 Fitting Equivalent Length (m) 0.0000
33 Use Detailed Fittings No
34 Total Pressure Drop (bar) 5.755
35
Fluid Package: Basis-1
36 Material Stream: 13500kg/hr-With 20% Over design
Property Package: Peng-Robinson
37
38
39
CONDITIONS
40 Overall Vapour Phase
41 Vapour / Phase Fraction 1.0000 1.0000
42 Temperature: (C) 15.00 * 15.00
43 Pressure: (bar) 24.13 * 24.13
44 Molar Flow (kgmole/h) 696.9 696.9
45 Mass Flow (kg/h) 1.350e+004 * 1.350e+004
46 Std Ideal Liq Vol Flow (m3/h) 38.95 38.95
47 Molar Enthalpy (kcal/kgmole) -1.932e+004 -1.932e+004
48 Molar Entropy (kJ/kgmole-C) 156.9 156.9
49 Heat Flow (kcal/h) -1.346e+007 -1.346e+007
50 Liq Vol Flow @Std Cond (m3/h) 1.643e+004 * 1.643e+004
51
52
PROPERTIES
53 Overall Vapour Phase
54 Molecular Weight 19.37 19.37
55 Molar Density (kgmole/m3) 1.087 1.087
56 Mass Density (kg/m3) 21.06 21.06
57 Act. Volume Flow (m3/h) 641.1 641.1
58 Mass Enthalpy (kcal/kg) -997.3 -997.3
59 Mass Entropy (kJ/kg-C) 8.100 8.100
60 Heat Capacity (kJ/kgmole-C) 41.97 41.97
61 Mass Heat Capacity (kJ/kg-C) 2.167 2.167
62 LHV Molar Basis (Std) (kcal/kgmole) 2.039e+005 2.039e+005
63 Aspen Technology Inc. Aspen HYSYS Version 14 Page 4 of 15
Licensed to: Company Name Not Available * Specified by user.
1
Case Name: Line Sizing.hsc
2 Company Name Not Available
3 Bedford, MA Unit Set: EuroSI
4 USA
Date/Time: Wed Feb 26 15:53:16 2025
5
6
Fluid Package: Basis-1
7 Material Stream: 13500kg/hr-With 20% Over design (continued)
Property Package: Peng-Robinson
8
9
10
PROPERTIES
11 Overall Vapour Phase
12 HHV Molar Basis (Std) (kcal/kgmole) 2.239e+005 2.239e+005
13 HHV Mass Basis (Std) (kcal/kg) 1.156e+004 1.156e+004
14 CO2 Loading --- ---
15 CO2 Apparent Mole Conc. (kgmole/m3) --- ---
16 CO2 Apparent Wt. Conc. (kgmol/kg) --- ---
17 LHV Mass Basis (Std) (kcal/kg) 1.053e+004 1.053e+004
18 Phase Fraction [Vol. Basis] 1.000 1.000
19 Phase Fraction [Mass Basis] 1.000 1.000
20 Phase Fraction [Act. Vol. Basis] 1.000 1.000
21 Mass Exergy (kcal/kg) 95.12 ---
22 Partial Pressure of CO2 (bar) 0.4344 ---
23 Cost Based on Flow (Cost/s) 0.0000 0.0000
24 Act. Gas Flow (ACT_m3/h) 641.1 641.1
25 Avg. Liq. Density (kgmole/m3) 17.89 17.89
26 Specific Heat (kJ/kgmole-C) 41.97 41.97
27 Std. Gas Flow (STD_m3/h) 1.648e+004 1.648e+004
28 Std. Ideal Liq. Mass Density (kg/m3) 346.6 346.6
29 Act. Liq. Flow (m3/s) --- ---
30 Z Factor 0.9266 0.9266
31 Watson K 17.40 17.40
32 User Property --- ---
33 Partial Pressure of H2S (bar) 0.0000 ---
34 Cp/(Cp - R) 1.247 1.247
35 Cp/Cv 1.376 1.376
36 Ideal Gas Cp/Cv 1.276 1.276
37 Ideal Gas Cp (kJ/kgmole-C) 38.44 38.44
38 Mass Ideal Gas Cp (kJ/kg-C) 1.985 1.985
39 Heat of Vap. (kcal/kgmole) 2601 ---
40 Kinematic Viscosity (cSt) 0.5541 0.5541
41 Liq. Mass Density (Std. Cond) (kg/m3) 0.8218 0.8218
42 Liq. Vol. Flow (Std. Cond) (m3/h) 1.643e+004 1.643e+004
43 Liquid Fraction 0.0000 0.0000
44 Molar Volume (m3/kgmole) 0.9199 0.9199
45 Mass Heat of Vap. (kcal/kg) 134.3 ---
46 Phase Fraction [Molar Basis] 1.0000 1.0000
47 Surface Tension (dyne/cm) --- ---
48 Thermal Conductivity (W/m-K) 3.202e-002 3.202e-002
49 Bubble Point Pressure (bar) --- ---
50 Viscosity (cP) 1.167e-002 1.167e-002
51 Cv (Semi-Ideal) (kJ/kgmole-C) 33.65 33.65
52 Mass Cv (Semi-Ideal) (kJ/kg-C) 1.737 1.737
53 Cv (kJ/kgmole-C) 30.50 30.50
54 Mass Cv (kJ/kg-C) 1.575 1.575
55 Cv (Ent. Method) (kJ/kgmole-C) --- ---
56 Mass Cv (Ent. Method) (kJ/kg-C) --- ---
57 Cp/Cv (Ent. Method) --- ---
58 Reid VP at 37.8 C (bar) --- ---
59 True VP at 37.8 C (bar) --- ---
60 Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 1.643e+004 1.643e+004
61 Viscosity Index -40.28 ---
62
63 Aspen Technology Inc. Aspen HYSYS Version 14 Page 5 of 15
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Case Name: Line Sizing.hsc
2 Company Name Not Available
3 Bedford, MA Unit Set: EuroSI
4 USA
Date/Time: Wed Feb 26 15:53:16 2025
5
6
Fluid Package: Basis-1
7 Material Stream: 13500kg/hr-With 20% Over design (continued)
Property Package: Peng-Robinson
8
9
10
COMPOSITION
11
12
Overall Phase Vapour Fraction 1.0000

13 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
14 (kgmole/h) (kg/h) FLOW (m3/h) FRACTION
15 Nitrogen 31.3656 * 0.0450 * 878.6445 * 0.0651 * 1.0896 * 0.0280 *
16 CO2 12.5462 * 0.0180 * 552.1562 * 0.0409 * 0.6690 * 0.0172 *
17 Methane 598.2465 * 0.8584 * 9597.6084 * 0.7109 * 32.0568 * 0.8230 *
18 Ethane 27.8805 * 0.0400 * 838.3648 * 0.0621 * 2.3571 * 0.0605 *
19 Propane 1.4637 * 0.0021 * 64.5460 * 0.0048 * 0.1274 * 0.0033 *
20 i-Butane 4.9488 * 0.0071 * 287.6437 * 0.0213 * 0.5119 * 0.0131 *
21 n-Butane 14.0797 * 0.0202 * 818.3666 * 0.0606 * 1.4032 * 0.0360 *
22 i-Pentane 1.3940 * 0.0020 * 100.5804 * 0.0075 * 0.1613 * 0.0041 *
23 n-Pentane 5.0185 * 0.0072 * 362.0895 * 0.0268 * 0.5750 * 0.0148 *
24 Total 696.9435 1.0000 13500.0000 1.0000 38.9512 1.0000
25
26
Vapour Phase Phase Fraction 1.000

27 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
28 (kgmole/h) (kg/h) FLOW (m3/h) FRACTION
29 Nitrogen 31.3656 0.0450 878.6445 0.0651 1.0896 0.0280
30 CO2 12.5462 0.0180 552.1562 0.0409 0.6690 0.0172
31 Methane 598.2465 0.8584 9597.6084 0.7109 32.0568 0.8230
32 Ethane 27.8805 0.0400 838.3648 0.0621 2.3571 0.0605
33 Propane 1.4637 0.0021 64.5460 0.0048 0.1274 0.0033
34 i-Butane 4.9488 0.0071 287.6437 0.0213 0.5119 0.0131
35 n-Butane 14.0797 0.0202 818.3666 0.0606 1.4032 0.0360
36 i-Pentane 1.3940 0.0020 100.5804 0.0075 0.1613 0.0041
37 n-Pentane 5.0185 0.0072 362.0895 0.0268 0.5750 0.0148
38 Total 696.9435 1.0000 13500.0000 1.0000 38.9512 1.0000
39
40
K VALUE
41 COMPONENTS MIXED LIGHT HEAVY
42 Nitrogen --- --- ---
43 CO2 --- --- ---
44 Methane --- --- ---
45 Ethane --- --- ---
46 Propane --- --- ---
47 i-Butane --- --- ---
48 n-Butane --- --- ---
49 i-Pentane --- --- ---
50 n-Pentane --- --- ---
51
52 Line Sizing Manager: Line Sizing Manager-With Over design
53
54
55
SIZING
56 Pipe Tag/Name Line Sizing-2
57 Calculation Type Rating
58 Stream Name 13500kg/hr-With 20% Over design @Main
59 FlowMargin (%) 20.00 *
60 Material Carbon Steel
61 Schedule STD
62 Nominal Diameter 300 mm
63 Aspen Technology Inc. Aspen HYSYS Version 14 Page 6 of 15
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Case Name: Line Sizing.hsc
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4 USA
Date/Time: Wed Feb 26 15:53:16 2025
5
6
7 Line Sizing Manager: Line Sizing Manager-With Over design (continued)
8
9
10
SIZING
11 Inner Diameter (mm) 304.8
12 Wall Thickness (mm) 9.525
13 Roughness (mm) 4.572e-002
14 Force Single Phase Off
15 Sizing Criteria Criteria-1
16 Pressure Gradient (kPa/m) 4.090e-003
17 Velocity Gradient (m/s) 2.929
18 Rho V^2 (kg/m-s2) 180.6
19 Flow Regime Vapour Only
20 Criteria Met? Met
21 Pipe Length (m) 8.000e+004 *
22 Fitting Equivalent Length (m) 0.0000
23 Use Detailed Fittings Off
24 Total Pressure Drop (bar) 3.272
25
26
DETAILS
27 Pipe Tag/Name Line Sizing-2
28 Pressure Gradient Rating
29 Stream Name 13500kg/hr-With 20% Over design @Main
30 Upstream Unit Operation Name
31 Upstream Unit Operation Type
32 Downstream Unit Operation Name
33 Downstream Unit Operation Type
34 Vapor Mass Flow Rate (kg/h) 1.350e+004
35 Vapor Molecular Weight 19.37
36 Vapor Mass Density (kg/m3) 21.06
37 Vapor Viscosity (cP) 1.167e-002
38 Vapor Cp/Cv 1.376
39 Vapor Z Factor 0.9266
40 Liquid Mass Flow Rate (kg/h) ---
41 Liquid Molecular Weight 19.37
42 Liquid Mass Density (kg/m3) ---
43 Liquid Viscosity (cP) ---
44 Flow Margin (%) 20.00 *
45 Pipe Material Carbon Steel
46 Schedule STD
47 Pipe Nominal Diameter 300 mm
48 Pipe Inside Diameter (mm) 304.8
49 Pipe Wall Thickness (mm) 9.525
50 Pipe Roughness (mm) 4.572e-002
51 Force Single Phase Off
52 Sizing Criteria Criteria-1
53 Pressure Gradient (kPa/m) 4.090e-003
54 Criteria Pressure Gradient (kPa/m) 9.193e-003
55 Velocity (m/s) 2.929
56 Criteria Velocity (m/s) ---
57 Rho V^2 (kg/m-s2) 180.6
58 Criteria Rho V^2 (kg/m-s2) ---
59 Flow Regime Vapour Only
60 Criteria Met or Failed? Met
61 Pipe Length (m) 8.000e+004 *
62 Fitting Equivalent Length (m) 0.0000
63 Aspen Technology Inc. Aspen HYSYS Version 14 Page 7 of 15
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Case Name: Line Sizing.hsc
2 Company Name Not Available
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4 USA
Date/Time: Wed Feb 26 15:53:16 2025
5
6
7 Line Sizing Manager: Line Sizing Manager-With Over design (continued)
8
9
10
DETAILS
11 Use Detailed Fittings No
12 Total Pressure Drop (bar) 3.272
13
Fluid Package: Basis-1
14 Material Stream: Normal-20000 m3/hr Property Package: Peng-Robinson
15
16
17
CONDITIONS
18 Overall Vapour Phase
19 Vapour / Phase Fraction 1.0000 1.0000
20 Temperature: (C) 15.00 * 15.00
21 Pressure: (bar) 24.13 * 24.13
22 Molar Flow (kgmole/h) 2.173e+004 2.173e+004
23 Mass Flow (kg/h) 4.210e+005 * 4.210e+005
24 Std Ideal Liq Vol Flow (m3/h) 1215 1215
25 Molar Enthalpy (kcal/kgmole) -1.932e+004 -1.932e+004
26 Molar Entropy (kJ/kgmole-C) 156.9 156.9
27 Heat Flow (kcal/h) -4.198e+008 -4.198e+008
28 Liq Vol Flow @Std Cond (m3/h) 5.123e+005 * 5.123e+005
29
30
PROPERTIES
31 Overall Vapour Phase
32 Molecular Weight 19.37 19.37
33 Molar Density (kgmole/m3) 1.087 1.087
34 Mass Density (kg/m3) 21.06 21.06
35 Act. Volume Flow (m3/h) 1.999e+004 1.999e+004
36 Mass Enthalpy (kcal/kg) -997.3 -997.3
37 Mass Entropy (kJ/kg-C) 8.100 8.100
38 Heat Capacity (kJ/kgmole-C) 41.97 41.97
39 Mass Heat Capacity (kJ/kg-C) 2.167 2.167
40 LHV Molar Basis (Std) (kcal/kgmole) 2.039e+005 2.039e+005
41 HHV Molar Basis (Std) (kcal/kgmole) 2.239e+005 2.239e+005
42 HHV Mass Basis (Std) (kcal/kg) 1.156e+004 1.156e+004
43 CO2 Loading --- ---
44 CO2 Apparent Mole Conc. (kgmole/m3) --- ---
45 CO2 Apparent Wt. Conc. (kgmol/kg) --- ---
46 LHV Mass Basis (Std) (kcal/kg) 1.053e+004 1.053e+004
47 Phase Fraction [Vol. Basis] 1.000 1.000
48 Phase Fraction [Mass Basis] 1.000 1.000
49 Phase Fraction [Act. Vol. Basis] 1.000 1.000
50 Mass Exergy (kcal/kg) 95.12 ---
51 Partial Pressure of CO2 (bar) 0.4344 ---
52 Cost Based on Flow (Cost/s) 0.0000 0.0000
53 Act. Gas Flow (ACT_m3/h) 1.999e+004 1.999e+004
54 Avg. Liq. Density (kgmole/m3) 17.89 17.89
55 Specific Heat (kJ/kgmole-C) 41.97 41.97
56 Std. Gas Flow (STD_m3/h) 5.139e+005 5.139e+005
57 Std. Ideal Liq. Mass Density (kg/m3) 346.6 346.6
58 Act. Liq. Flow (m3/s) --- ---
59 Z Factor 0.9266 0.9266
60 Watson K 17.40 17.40
61 User Property --- ---
62 Partial Pressure of H2S (bar) 0.0000 ---
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Fluid Package: Basis-1
7 Material Stream: Normal-20000 m3/hr (continued)
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9
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PROPERTIES
11 Overall Vapour Phase
12 Cp/(Cp - R) 1.247 1.247
13 Cp/Cv 1.376 1.376
14 Ideal Gas Cp/Cv 1.276 1.276
15 Ideal Gas Cp (kJ/kgmole-C) 38.44 38.44
16 Mass Ideal Gas Cp (kJ/kg-C) 1.985 1.985
17 Heat of Vap. (kcal/kgmole) 2601 ---
18 Kinematic Viscosity (cSt) 0.5541 0.5541
19 Liq. Mass Density (Std. Cond) (kg/m3) 0.8218 0.8218
20 Liq. Vol. Flow (Std. Cond) (m3/h) 5.123e+005 5.123e+005
21 Liquid Fraction 0.0000 0.0000
22 Molar Volume (m3/kgmole) 0.9199 0.9199
23 Mass Heat of Vap. (kcal/kg) 134.3 ---
24 Phase Fraction [Molar Basis] 1.0000 1.0000
25 Surface Tension (dyne/cm) --- ---
26 Thermal Conductivity (W/m-K) 3.202e-002 3.202e-002
27 Bubble Point Pressure (bar) --- ---
28 Viscosity (cP) 1.167e-002 1.167e-002
29 Cv (Semi-Ideal) (kJ/kgmole-C) 33.65 33.65
30 Mass Cv (Semi-Ideal) (kJ/kg-C) 1.737 1.737
31 Cv (kJ/kgmole-C) 30.50 30.50
32 Mass Cv (kJ/kg-C) 1.575 1.575
33 Cv (Ent. Method) (kJ/kgmole-C) --- ---
34 Mass Cv (Ent. Method) (kJ/kg-C) --- ---
35 Cp/Cv (Ent. Method) --- ---
36 Reid VP at 37.8 C (bar) --- ---
37 True VP at 37.8 C (bar) --- ---
38 Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 5.123e+005 5.123e+005
39 Viscosity Index -40.28 ---
40
41
COMPOSITION
42
43
Overall Phase Vapour Fraction 1.0000

44 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
45 (kgmole/h) (kg/h) FLOW (m3/h) FRACTION
46 Nitrogen 978.1419 * 0.0450 * 27400.6903 * 0.0651 * 33.9801 * 0.0280 *
47 CO2 391.2568 * 0.0180 * 17219.0934 * 0.0409 * 20.8632 * 0.0172 *
48 Methane 18656.4270 * 0.8584 * 299303.1945 * 0.7109 * 999.6967 * 0.8230 *
49 Ethane 869.4595 * 0.0400 * 26144.5604 * 0.0621 * 73.5052 * 0.0605 *
50 Propane 45.6466 * 0.0021 * 2012.8792 * 0.0048 * 3.9727 * 0.0033 *
51 i-Butane 154.3291 * 0.0071 * 8970.2223 * 0.0213 * 15.9622 * 0.0131 *
52 n-Butane 439.0770 * 0.0202 * 25520.9143 * 0.0606 * 43.7584 * 0.0360 *
53 i-Pentane 43.4730 * 0.0020 * 3136.6186 * 0.0075 * 5.0311 * 0.0041 *
54 n-Pentane 156.5027 * 0.0072 * 11291.8271 * 0.0268 * 17.9312 * 0.0148 *
55 Total 21734.3136 1.0000 421000.0000 1.0000 1214.7009 1.0000
56
57
Vapour Phase Phase Fraction 1.000

58 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
59 (kgmole/h) (kg/h) FLOW (m3/h) FRACTION
60 Nitrogen 978.1419 0.0450 27400.6903 0.0651 33.9801 0.0280
61 CO2 391.2568 0.0180 17219.0934 0.0409 20.8632 0.0172
62 Methane 18656.4270 0.8584 299303.1945 0.7109 999.6967 0.8230
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7 Material Stream: Normal-20000 m3/hr (continued)
Property Package: Peng-Robinson
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COMPOSITION
11
12
Vapour Phase (continued) Phase Fraction 1.000

13 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
14 (kgmole/h) (kg/h) FLOW (m3/h) FRACTION
15 Ethane 869.4595 0.0400 26144.5604 0.0621 73.5052 0.0605
16 Propane 45.6466 0.0021 2012.8792 0.0048 3.9727 0.0033
17 i-Butane 154.3291 0.0071 8970.2223 0.0213 15.9622 0.0131
18 n-Butane 439.0770 0.0202 25520.9143 0.0606 43.7584 0.0360
19 i-Pentane 43.4730 0.0020 3136.6186 0.0075 5.0311 0.0041
20 n-Pentane 156.5027 0.0072 11291.8271 0.0268 17.9312 0.0148
21 Total 21734.3136 1.0000 421000.0000 1.0000 1214.7009 1.0000
22
23
K VALUE
24 COMPONENTS MIXED LIGHT HEAVY
25 Nitrogen --- --- ---
26 CO2 --- --- ---
27 Methane --- --- ---
28 Ethane --- --- ---
29 Propane --- --- ---
30 i-Butane --- --- ---
31 n-Butane --- --- ---
32 i-Pentane --- --- ---
33 n-Pentane --- --- ---
34
35 Line Sizing Manager: Line Sizing Manager-Normal-2
36
37
38
SIZING
39 Pipe Tag/Name Line Sizing-3
40 Calculation Type Rating
41 Stream Name Normal-20000 m3/hr @Main
42 FlowMargin (%) 0.00
43 Material Carbon Steel
44 Schedule STD
45 Nominal Diameter 1050 mm
46 Inner Diameter (mm) 1048
47 Wall Thickness (mm) 9.525
48 Roughness (mm) 4.572e-002
49 Force Single Phase Off
50 Sizing Criteria Criteria-1
51 Pressure Gradient (kPa/m) 4.436e-003
52 Velocity Gradient (m/s) 6.442
53 Rho V^2 (kg/m-s2) 873.7
54 Flow Regime Vapour Only
55 Criteria Met? Undetermined
56 Pipe Length (m) 8.000e+004 *
57 Fitting Equivalent Length (m) 0.0000
58 Use Detailed Fittings Off
59 Total Pressure Drop (bar) 3.549
60
61
DETAILS
62 Pipe Tag/Name Line Sizing-3
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7 Line Sizing Manager: Line Sizing Manager-Normal-2 (continued)
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DETAILS
11 Pressure Gradient Rating
12 Stream Name Normal-20000 m3/hr @Main
13 Upstream Unit Operation Name
14 Upstream Unit Operation Type
15 Downstream Unit Operation Name
16 Downstream Unit Operation Type
17 Vapor Mass Flow Rate (kg/h) 4.210e+005
18 Vapor Molecular Weight 19.37
19 Vapor Mass Density (kg/m3) 21.06
20 Vapor Viscosity (cP) 1.167e-002
21 Vapor Cp/Cv 1.376
22 Vapor Z Factor 0.9266
23 Liquid Mass Flow Rate (kg/h) ---
24 Liquid Molecular Weight 19.37
25 Liquid Mass Density (kg/m3) ---
26 Liquid Viscosity (cP) ---
27 Flow Margin (%) 0.00
28 Pipe Material Carbon Steel
29 Schedule STD
30 Pipe Nominal Diameter 1050 mm
31 Pipe Inside Diameter (mm) 1048
32 Pipe Wall Thickness (mm) 9.525
33 Pipe Roughness (mm) 4.572e-002
34 Force Single Phase Off
35 Sizing Criteria Criteria-1
36 Pressure Gradient (kPa/m) 4.436e-003
37 Criteria Pressure Gradient (kPa/m) ---
38 Velocity (m/s) 6.442
39 Criteria Velocity (m/s) ---
40 Rho V^2 (kg/m-s2) 873.7
41 Criteria Rho V^2 (kg/m-s2) ---
42 Flow Regime Vapour Only
43 Criteria Met or Failed? Undetermined
44 Pipe Length (m) 8.000e+004 *
45 Fitting Equivalent Length (m) 0.0000
46 Use Detailed Fittings No
47 Total Pressure Drop (bar) 3.549
48
Fluid Package: Basis-1
49 Material Stream: 20000 m3/hr-With 20% Over design
Property Package: Peng-Robinson
50
51
52
CONDITIONS
53 Overall Vapour Phase
54 Vapour / Phase Fraction 1.0000 1.0000
55 Temperature: (C) 15.00 * 15.00
56 Pressure: (bar) 24.13 * 24.13
57 Molar Flow (kgmole/h) 2.173e+004 2.173e+004
58 Mass Flow (kg/h) 4.210e+005 * 4.210e+005
59 Std Ideal Liq Vol Flow (m3/h) 1215 1215
60 Molar Enthalpy (kcal/kgmole) -1.932e+004 -1.932e+004
61 Molar Entropy (kJ/kgmole-C) 156.9 156.9
62 Heat Flow (kcal/h) -4.198e+008 -4.198e+008
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Fluid Package: Basis-1
7 Material Stream: 20000 m3/hr-With 20% Over design (continued)
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CONDITIONS
11 Overall Vapour Phase
12 Liq Vol Flow @Std Cond (m3/h) 5.123e+005 * 5.123e+005
13
14
PROPERTIES
15 Overall Vapour Phase
16 Molecular Weight 19.37 19.37
17 Molar Density (kgmole/m3) 1.087 1.087
18 Mass Density (kg/m3) 21.06 21.06
19 Act. Volume Flow (m3/h) 1.999e+004 1.999e+004
20 Mass Enthalpy (kcal/kg) -997.3 -997.3
21 Mass Entropy (kJ/kg-C) 8.100 8.100
22 Heat Capacity (kJ/kgmole-C) 41.97 41.97
23 Mass Heat Capacity (kJ/kg-C) 2.167 2.167
24 LHV Molar Basis (Std) (kcal/kgmole) 2.039e+005 2.039e+005
25 HHV Molar Basis (Std) (kcal/kgmole) 2.239e+005 2.239e+005
26 HHV Mass Basis (Std) (kcal/kg) 1.156e+004 1.156e+004
27 CO2 Loading --- ---
28 CO2 Apparent Mole Conc. (kgmole/m3) --- ---
29 CO2 Apparent Wt. Conc. (kgmol/kg) --- ---
30 LHV Mass Basis (Std) (kcal/kg) 1.053e+004 1.053e+004
31 Phase Fraction [Vol. Basis] 1.000 1.000
32 Phase Fraction [Mass Basis] 1.000 1.000
33 Phase Fraction [Act. Vol. Basis] 1.000 1.000
34 Mass Exergy (kcal/kg) 95.12 ---
35 Partial Pressure of CO2 (bar) 0.4344 ---
36 Cost Based on Flow (Cost/s) 0.0000 0.0000
37 Act. Gas Flow (ACT_m3/h) 1.999e+004 1.999e+004
38 Avg. Liq. Density (kgmole/m3) 17.89 17.89
39 Specific Heat (kJ/kgmole-C) 41.97 41.97
40 Std. Gas Flow (STD_m3/h) 5.139e+005 5.139e+005
41 Std. Ideal Liq. Mass Density (kg/m3) 346.6 346.6
42 Act. Liq. Flow (m3/s) --- ---
43 Z Factor 0.9266 0.9266
44 Watson K 17.40 17.40
45 User Property --- ---
46 Partial Pressure of H2S (bar) 0.0000 ---
47 Cp/(Cp - R) 1.247 1.247
48 Cp/Cv 1.376 1.376
49 Ideal Gas Cp/Cv 1.276 1.276
50 Ideal Gas Cp (kJ/kgmole-C) 38.44 38.44
51 Mass Ideal Gas Cp (kJ/kg-C) 1.985 1.985
52 Heat of Vap. (kcal/kgmole) 2601 ---
53 Kinematic Viscosity (cSt) 0.5541 0.5541
54 Liq. Mass Density (Std. Cond) (kg/m3) 0.8218 0.8218
55 Liq. Vol. Flow (Std. Cond) (m3/h) 5.123e+005 5.123e+005
56 Liquid Fraction 0.0000 0.0000
57 Molar Volume (m3/kgmole) 0.9199 0.9199
58 Mass Heat of Vap. (kcal/kg) 134.3 ---
59 Phase Fraction [Molar Basis] 1.0000 1.0000
60 Surface Tension (dyne/cm) --- ---
61 Thermal Conductivity (W/m-K) 3.202e-002 3.202e-002
62 Bubble Point Pressure (bar) --- ---
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PROPERTIES
11 Overall Vapour Phase
12 Viscosity (cP) 1.167e-002 1.167e-002
13 Cv (Semi-Ideal) (kJ/kgmole-C) 33.65 33.65
14 Mass Cv (Semi-Ideal) (kJ/kg-C) 1.737 1.737
15 Cv (kJ/kgmole-C) 30.50 30.50
16 Mass Cv (kJ/kg-C) 1.575 1.575
17 Cv (Ent. Method) (kJ/kgmole-C) --- ---
18 Mass Cv (Ent. Method) (kJ/kg-C) --- ---
19 Cp/Cv (Ent. Method) --- ---
20 Reid VP at 37.8 C (bar) --- ---
21 True VP at 37.8 C (bar) --- ---
22 Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 5.123e+005 5.123e+005
23 Viscosity Index -40.28 ---
24
25
COMPOSITION
26
27
Overall Phase Vapour Fraction 1.0000

28 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
29 (kgmole/h) (kg/h) FLOW (m3/h) FRACTION
30 Nitrogen 978.1419 * 0.0450 * 27400.6903 * 0.0651 * 33.9801 * 0.0280 *
31 CO2 391.2568 * 0.0180 * 17219.0934 * 0.0409 * 20.8632 * 0.0172 *
32 Methane 18656.4270 * 0.8584 * 299303.1945 * 0.7109 * 999.6967 * 0.8230 *
33 Ethane 869.4595 * 0.0400 * 26144.5604 * 0.0621 * 73.5052 * 0.0605 *
34 Propane 45.6466 * 0.0021 * 2012.8792 * 0.0048 * 3.9727 * 0.0033 *
35 i-Butane 154.3291 * 0.0071 * 8970.2223 * 0.0213 * 15.9622 * 0.0131 *
36 n-Butane 439.0770 * 0.0202 * 25520.9143 * 0.0606 * 43.7584 * 0.0360 *
37 i-Pentane 43.4730 * 0.0020 * 3136.6186 * 0.0075 * 5.0311 * 0.0041 *
38 n-Pentane 156.5027 * 0.0072 * 11291.8271 * 0.0268 * 17.9312 * 0.0148 *
39 Total 21734.3136 1.0000 421000.0000 1.0000 1214.7009 1.0000
40
41
Vapour Phase Phase Fraction 1.000

42 COMPONENTS MOLAR FLOW MOLE FRACTION MASS FLOW MASS FRACTION LIQUID VOLUME LIQUID VOLUME
43 (kgmole/h) (kg/h) FLOW (m3/h) FRACTION
44 Nitrogen 978.1419 0.0450 27400.6903 0.0651 33.9801 0.0280
45 CO2 391.2568 0.0180 17219.0934 0.0409 20.8632 0.0172
46 Methane 18656.4270 0.8584 299303.1945 0.7109 999.6967 0.8230
47 Ethane 869.4595 0.0400 26144.5604 0.0621 73.5052 0.0605
48 Propane 45.6466 0.0021 2012.8792 0.0048 3.9727 0.0033
49 i-Butane 154.3291 0.0071 8970.2223 0.0213 15.9622 0.0131
50 n-Butane 439.0770 0.0202 25520.9143 0.0606 43.7584 0.0360
51 i-Pentane 43.4730 0.0020 3136.6186 0.0075 5.0311 0.0041
52 n-Pentane 156.5027 0.0072 11291.8271 0.0268 17.9312 0.0148
53 Total 21734.3136 1.0000 421000.0000 1.0000 1214.7009 1.0000
54
55
K VALUE
56 COMPONENTS MIXED LIGHT HEAVY
57 Nitrogen --- --- ---
58 CO2 --- --- ---
59 Methane --- --- ---
60 Ethane --- --- ---
61 Propane --- --- ---
62 i-Butane --- --- ---
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K VALUE
11 COMPONENTS MIXED LIGHT HEAVY
12 n-Butane --- --- ---
13 i-Pentane --- --- ---
14 n-Pentane --- --- ---
15
16 Line Sizing Manager: Line Sizing Manager-Normal-20000 m3/hr-2
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18
19
SIZING
20 Pipe Tag/Name Line Sizing-4
21 Calculation Type Rating
22 Stream Name 20000 m3/hr-With 20% Over design @Main
23 FlowMargin (%) 20.00 *
24 Material Carbon Steel
25 Schedule STD
26 Nominal Diameter 1050 mm
27 Inner Diameter (mm) 1048
28 Wall Thickness (mm) 9.525
29 Roughness (mm) 4.572e-002
30 Force Single Phase Off
31 Sizing Criteria Criteria-1
32 Pressure Gradient (kPa/m) 6.358e-003
33 Velocity Gradient (m/s) 7.730
34 Rho V^2 (kg/m-s2) 1258
35 Flow Regime Vapour Only
36 Criteria Met? Undetermined
37 Pipe Length (m) 8.000e+004 *
38 Fitting Equivalent Length (m) 0.0000
39 Use Detailed Fittings Off
40 Total Pressure Drop (bar) 5.086
41
42
DETAILS
43 Pipe Tag/Name Line Sizing-4
44 Pressure Gradient Rating
45 Stream Name 20000 m3/hr-With 20% Over design @Main
46 Upstream Unit Operation Name
47 Upstream Unit Operation Type
48 Downstream Unit Operation Name
49 Downstream Unit Operation Type
50 Vapor Mass Flow Rate (kg/h) 4.210e+005
51 Vapor Molecular Weight 19.37
52 Vapor Mass Density (kg/m3) 21.06
53 Vapor Viscosity (cP) 1.167e-002
54 Vapor Cp/Cv 1.376
55 Vapor Z Factor 0.9266
56 Liquid Mass Flow Rate (kg/h) ---
57 Liquid Molecular Weight 19.37
58 Liquid Mass Density (kg/m3) ---
59 Liquid Viscosity (cP) ---
60 Flow Margin (%) 20.00 *
61 Pipe Material Carbon Steel
62 Schedule STD
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7 Line Sizing Manager: Line Sizing Manager-Normal-20000 m3/hr-2 (continued)
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DETAILS
11 Pipe Nominal Diameter 1050 mm
12 Pipe Inside Diameter (mm) 1048
13 Pipe Wall Thickness (mm) 9.525
14 Pipe Roughness (mm) 4.572e-002
15 Force Single Phase Off
16 Sizing Criteria Criteria-1
17 Pressure Gradient (kPa/m) 6.358e-003
18 Criteria Pressure Gradient (kPa/m) ---
19 Velocity (m/s) 7.730
20 Criteria Velocity (m/s) ---
21 Rho V^2 (kg/m-s2) 1258
22 Criteria Rho V^2 (kg/m-s2) ---
23 Flow Regime Vapour Only
24 Criteria Met or Failed? Undetermined
25 Pipe Length (m) 8.000e+004 *
26 Fitting Equivalent Length (m) 0.0000
27 Use Detailed Fittings No
28 Total Pressure Drop (bar) 5.086
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