PROYECTO Material Stream: 1 Fluid Package: Basis-1 Property Package
68
PROYECTO RIO GRANDE Santa Cruz Bolivia Case Name: PROYECTO FINAL.HSC Unit Set: NewUser Date/Time: Tue Jul 17 11:57:47 2012 Material Stream: 1 Fluid Package: Basis-1 Property Package: Peng Robinson CONDITIONS Vapour / Phase Fraction Temperature: (F) Pressure: (psia) Molar Flow (MMSCFD) Mass Flow (lb/hr) Std Ideal Liq Vol Flow (barrel/day) Molar Enthalpy (Btu/lbmole) Molar Entropy (Btu/lbmole-F) Heat Flow (Btu/hr) Liq Vol Flow @Std Cond (barrel/day) Overall 1.0000 109.5 * 905.0 * 200.0 * 4.110e+005 8.547e+004 -3.575e+004 36.44 -7.853e+008 --- Vapour Phase 1.0000 109.5 905.0 200.0 4.110e+005 8.547e+004 -3.575e+004 36.44 -7.853e+008 --- PROPERTIES Molecular Weight Molar Density Mass Density Act. Volume Flow Mass Enthalpy Mass Entropy Heat Capacity Mass Heat Capacity Lower Heating Value Mass Lower Heating Value Phase Fraction [Vol. Basis] Phase Fraction [Mass Basis] Partial Pressure of CO2 Cost Based on Flow Act. Gas Flow Avg. Liq. Density Specific Heat Std. Gas Flow Std. Ideal Liq. Mass Density Act. Liq. Flow Z Factor Watson K User Property Cp/(Cp - R) Cp/Cv Heat of Vap. Kinematic Viscosity Liq. Mass Density (Std. Cond) Liq. Vol. Flow (Std. Cond) Liquid Fraction Molar Volume Mass Heat of Vap. Phase Fraction [Molar Basis] Surface Tension Thermal Conductivity Viscosity Cv (Semi-Ideal) Mass Cv (Semi-Ideal) Cv Mass Cv Cv (Ent. Method) Mass Cv (Ent. Method) Cp/Cv (Ent. Method) Liq. Vol. Flow - Sum(Std. Cond) (lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole) (Btu/lb) (psia) (Cost/s) (ACFM) (lbmole/ft3) (Btu/lbmole-F) (MMSCFD) (lb/ft3) (USGPM) (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) (barrel/day) Overall 18.71 0.1704 3.189 5.510e+005 -1911 1.947 11.44 0.6111 3.766e+005 2.012e+004 --- 4.941e-324 17.10 0.0000 2148 1.099 11.44 200.0 20.56 --- 0.8696 18.36 --- 1.210 1.487 2275 0.2636 --- --- 0.0000 5.869 121.5 1.0000 --- 2.303e-002 1.346e-002 9.450 0.5050 7.692 0.4110 7.692 0.4110 1.487 0.0000 Vapour Phase 18.71 0.1704 3.189 5.510e+005 -1911 1.947 11.44 0.6111 3.766e+005 2.012e+004 1.000 1.000 --- 0.0000 2148 1.099 11.44 200.0 20.56 --- 0.8696 18.36 --- 1.210 1.487 --- 0.2636 --- --- 0.0000 5.869 --- 1.0000 --- 2.303e-002 1.346e-002 9.450 0.5050 7.692 0.4110 7.692 0.4110 1.487 0.0000 Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 1 of 68 * Specified by user. Licensed to: LEGENDS
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Transcript of PROYECTO Material Stream: 1 Fluid Package: Basis-1 Property Package
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 1Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
109.5 *
905.0 *
200.0 *
4.110e+005
8.547e+004
-3.575e+004
36.44
-7.853e+008
---
Vapour Phase
1.0000
109.5
905.0
200.0
4.110e+005
8.547e+004
-3.575e+004
36.44
-7.853e+008
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
Overall
18.71
0.1704
3.189
5.510e+005
-1911
1.947
11.44
0.6111
3.766e+005
2.012e+004
---
4.941e-324
17.10
0.0000
2148
1.099
11.44
200.0
20.56
---
0.8696
18.36
---
1.210
1.487
2275
0.2636
---
---
0.0000
5.869
121.5
1.0000
---
2.303e-002
1.346e-002
9.450
0.5050
7.692
0.4110
7.692
0.4110
1.487
0.0000
Vapour Phase
18.71
0.1704
3.189
5.510e+005
-1911
1.947
11.44
0.6111
3.766e+005
2.012e+004
1.000
1.000
---
0.0000
2148
1.099
11.44
200.0
20.56
---
0.8696
18.36
---
1.210
1.487
---
0.2636
---
---
0.0000
5.869
---
1.0000
---
2.303e-002
1.346e-002
9.450
0.5050
7.692
0.4110
7.692
0.4110
1.487
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 1 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 1 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
Higher Heating Value[Gas]
(psia)
(psia)
(psia)
(MMBtu/gal)
Overall
0.0000
---
---
1.475e-004
Vapour Phase
---
---
---
1.475e-004
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
107.8380 *
415.0990 *
19293.3260 *
1386.8600 *
502.9510 *
79.7250 *
103.8850 *
31.8460 *
20.2060 *
22.1830 *
MOLE FRACTION
0.0049 *
0.0189 *
0.8784 *
0.0631 *
0.0229 *
0.0036 *
0.0047 *
0.0014 *
0.0009 *
0.0010 *
MASS FLOW
(lb/hr)
3020.8659 *
18268.3828 *
309520.9013 *
41702.7422 *
22178.6303 *
4633.9359 *
6038.2118 *
2297.7208 *
1457.8831 *
1911.6844 *
MASS FRACTION
0.0073 *
0.0444 *
0.7530 *
0.1015 *
0.0540 *
0.0113 *
0.0147 *
0.0056 *
0.0035 *
0.0047 *
LIQUID VOLUME
FLOW (barrel/day)
256.5153 *
1515.6122 *
70788.8970 *
8028.2292 *
2997.2360 *
564.6226 *
708.9114 *
252.3594 *
158.5212 *
197.5337 *
LIQUID VOLUME
FRACTION
0.0030 *
0.0177 *
0.8282 *
0.0939 *
0.0351 *
0.0066 *
0.0083 *
0.0030 *
0.0019 *
0.0023 *
Total 21963.9190 1.0000 411030.9586 1.0000 85468.4379 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
107.8380
415.0990
19293.3260
1386.8600
502.9510
79.7250
103.8850
31.8460
20.2060
22.1830
MOLE FRACTION
0.0049
0.0189
0.8784
0.0631
0.0229
0.0036
0.0047
0.0014
0.0009
0.0010
MASS FLOW
(lb/hr)
3020.8659
18268.3828
309520.9013
41702.7422
22178.6303
4633.9359
6038.2118
2297.7208
1457.8831
1911.6844
MASS FRACTION
0.0073
0.0444
0.7530
0.1015
0.0540
0.0113
0.0147
0.0056
0.0035
0.0047
LIQUID VOLUME
FLOW (barrel/day)
256.5153
1515.6122
70788.8970
8028.2292
2997.2360
564.6226
708.9114
252.3594
158.5212
197.5337
LIQUID VOLUME
FRACTION
0.0030
0.0177
0.8282
0.0939
0.0351
0.0066
0.0083
0.0030
0.0019
0.0023
Total 21963.9190 1.0000 411030.9586 1.0000 85468.4379 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Tee: TEE-100
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 2 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 1 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROCESS UTILITY
DYNAMICS
Pressure Specification (Active): 905.0 psia *
Flow Specification (Active) Molar: 200.0 MMSCFD * Mass: 4.110e+005 lb/hr Std Ideal Liq Volume:47e+004 barrel/day
User Variables
NOTES
Description
Material Stream: 2Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.0000
-29.00
895.0
5.844
2.045e+004
3209
-4.949e+004
25.37
-3.176e+007
5166 *
Vapour Phase
0.0000
-29.00
895.0
0.0000
0.0000
0.0000
-3.723e+004
32.93
0.0000
0.0000
Liquid Phase
1.0000
-29.00
895.0
5.844
2.045e+004
3209
-4.949e+004
25.37
-3.176e+007
5166
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(Btu/lbmole)
Overall
31.86
0.8998
28.67
3049
-1553
0.7964
21.23
0.6662
6.237e+005
1.957e+004
---
2.122e-314
0.0000
0.0000
---
0.8549
21.23
5.845
27.24
88.92
---
15.69
---
1.103
1.103
6914
Vapour Phase
18.32
0.3009
5.512
0.0000
-2033
1.798
16.40
0.8952
3.692e+005
2.015e+004
---
0.0000
---
0.0000
---
1.108
16.40
0.0000
20.30
---
0.6436
18.51
---
1.138
2.361
---
Liquid Phase
31.86
0.8998
28.67
3049
-1553
0.7964
21.23
0.6662
6.237e+005
1.957e+004
1.000
1.000
---
0.0000
---
0.8549
21.23
5.845
27.24
88.92
0.2152
15.69
---
1.103
1.103
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 3 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 2 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
0.2048
16.92
5166
1.000
1.111
217.0
0.0000
7.167
5.377e-002
9.405e-002
19.24
0.6039
19.24
0.6039
20.31
0.6373
1.045
5166
0.0000
---
1591
Vapour Phase
0.1389
---
0.0000
0.0000
3.324
---
0.0000
---
2.004e-002
1.226e-002
14.41
0.7868
6.945
0.3791
6.944
0.3791
2.361
0.0000
---
---
---
Liquid Phase
0.2048
16.92
5166
1.000
1.111
---
1.0000
7.167
5.377e-002
9.405e-002
19.24
0.6039
19.24
0.6039
---
---
---
5166
---
---
1591
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.6825
15.5411
322.0192
97.2335
91.2475
25.3554
40.5099
18.1363
12.8456
18.1800
MOLE FRACTION
0.0011
0.0242
0.5018
0.1515
0.1422
0.0395
0.0631
0.0283
0.0200
0.0283
MASS FLOW
(lb/hr)
19.1178
683.9570
5166.1211
2923.8031
4023.7423
1473.7545
2354.5978
1308.5531
926.8265
1566.7108
MASS FRACTION
0.0009
0.0334
0.2527
0.1430
0.1968
0.0721
0.1152
0.0640
0.0453
0.0766
LIQUID VOLUME
FLOW (barrel/day)
1.6234
56.7436
1181.5164
562.8637
543.7714
179.5698
276.4397
143.7188
100.7774
161.8877
LIQUID VOLUME
FRACTION
0.0005
0.0177
0.3682
0.1754
0.1695
0.0560
0.0861
0.0448
0.0314
0.0504
Total 641.7509 1.0000 20447.1840 1.0000 3208.9118 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0050
0.0187
0.8897
0.0605
0.0193
0.0025
0.0030
0.0006
0.0003
0.0002
MASS FLOW
(lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0077
0.0450
0.7792
0.0993
0.0465
0.0081
0.0094
0.0025
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.0031
0.0177
0.8462
0.0908
0.0298
0.0047
0.0053
0.0013
0.0007
0.0004
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 4 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 2 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Liquid Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.6825
15.5411
322.0192
97.2335
91.2475
25.3554
40.5099
18.1363
12.8456
18.1800
MOLE FRACTION
0.0011
0.0242
0.5018
0.1515
0.1422
0.0395
0.0631
0.0283
0.0200
0.0283
MASS FLOW
(lb/hr)
19.1178
683.9570
5166.1211
2923.8031
4023.7423
1473.7545
2354.5978
1308.5531
926.8265
1566.7108
MASS FRACTION
0.0009
0.0334
0.2527
0.1430
0.1968
0.0721
0.1152
0.0640
0.0453
0.0766
LIQUID VOLUME
FLOW (barrel/day)
1.6234
56.7436
1181.5164
562.8637
543.7714
179.5698
276.4397
143.7188
100.7774
161.8877
LIQUID VOLUME
FRACTION
0.0005
0.0177
0.3682
0.1754
0.1695
0.0560
0.0861
0.0448
0.0314
0.0504
Total 641.7509 1.0000 20447.1840 1.0000 3208.9118 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
4.726
0.7738
1.773
0.3992
0.1358
6.454e-002
4.709e-002
2.275e-002
1.725e-002
6.627e-003
LIGHT
4.726
0.7738
1.773
0.3992
0.1358
6.454e-002
4.709e-002
2.275e-002
1.725e-002
6.627e-003
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Valve: VLV-101
PRODUCT FROM
Separator: V-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 895.0 psia
Flow Specification (Inactive) Molar: 5.844 MMSCFD Mass: 2.045e+004 lb/hr Std Ideal Liq Volume: 3209 barrel/day
User Variables
NOTES
Description
Material Stream: 3Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Overall
1.0000
-29.00
Vapour Phase
1.0000
-29.00
Liquid Phase
0.0000
-29.00
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 5 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 3 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
895.0
194.2
3.906e+005
8.226e+004
-3.723e+004
32.93
-7.939e+008
---
Vapour Phase
895.0
194.2
3.906e+005
8.226e+004
-3.723e+004
32.93
-7.939e+008
---
Liquid Phase
895.0
0.0000
0.0000
0.0000
-4.949e+004
25.37
0.0000
0.0000
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
Overall
18.32
0.3009
5.512
3.029e+005
-2033
1.798
16.40
0.8952
3.692e+005
2.015e+004
---
2.122e-314
16.77
0.0000
1181
1.108
16.40
194.2
20.30
---
---
18.51
---
1.138
2.361
1639
0.1389
---
---
0.0000
3.324
89.47
1.0000
---
2.004e-002
1.226e-002
14.41
0.7868
6.945
0.3791
6.944
0.3791
2.361
0.0000
0.0000
---
Vapour Phase
18.32
0.3009
5.512
3.029e+005
-2033
1.798
16.40
0.8952
3.692e+005
2.015e+004
1.000
1.000
---
0.0000
1181
1.108
16.40
194.2
20.30
---
0.6436
18.51
---
1.138
2.361
---
0.1389
---
---
0.0000
3.324
---
1.0000
---
2.004e-002
1.226e-002
14.41
0.7868
6.945
0.3791
6.944
0.3791
2.361
0.0000
---
---
Liquid Phase
31.86
0.8998
28.67
0.0000
-1553
0.7964
21.23
0.6662
6.237e+005
1.957e+004
---
0.0000
---
0.0000
---
0.8549
21.23
0.0000
27.24
---
0.2152
15.69
---
1.103
1.103
---
0.2048
16.92
0.0000
1.000
1.111
---
0.0000
7.167
5.377e-002
9.405e-002
19.24
0.6039
19.24
0.6039
---
---
---
0.0000
---
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 6 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 3 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
True VP at 37.8 C (psia)
Overall
---
Vapour Phase
---
Liquid Phase
1591
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
107.1555
399.5579
18971.3068
1289.6265
411.7035
54.3696
63.3751
13.7097
7.3604
4.0030
MOLE FRACTION
0.0050
0.0187
0.8897
0.0605
0.0193
0.0025
0.0030
0.0006
0.0003
0.0002
MASS FLOW
(lb/hr)
3001.7482
17584.4258
304354.7802
38778.9391
18154.8880
3160.1815
3683.6140
989.1677
531.0567
344.9736
MASS FRACTION
0.0077
0.0450
0.7792
0.0993
0.0465
0.0081
0.0094
0.0025
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
254.8919
1458.8686
69607.3806
7465.3655
2453.4646
385.0528
432.4717
108.6406
57.7438
35.6460
LIQUID VOLUME
FRACTION
0.0031
0.0177
0.8462
0.0908
0.0298
0.0047
0.0053
0.0013
0.0007
0.0004
Total 21322.1681 1.0000 390583.7747 1.0000 82259.5261 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
107.1555
399.5579
18971.3068
1289.6265
411.7035
54.3696
63.3751
13.7097
7.3604
4.0030
MOLE FRACTION
0.0050
0.0187
0.8897
0.0605
0.0193
0.0025
0.0030
0.0006
0.0003
0.0002
MASS FLOW
(lb/hr)
3001.7482
17584.4258
304354.7802
38778.9391
18154.8880
3160.1815
3683.6140
989.1677
531.0567
344.9736
MASS FRACTION
0.0077
0.0450
0.7792
0.0993
0.0465
0.0081
0.0094
0.0025
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
254.8919
1458.8686
69607.3806
7465.3655
2453.4646
385.0528
432.4717
108.6406
57.7438
35.6460
LIQUID VOLUME
FRACTION
0.0031
0.0177
0.8462
0.0908
0.0298
0.0047
0.0053
0.0013
0.0007
0.0004
Total 21322.1681 1.0000 390583.7747 1.0000 82259.5261 1.0000
Liquid Phase Phase Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0011
0.0242
0.5018
0.1515
0.1422
0.0395
0.0631
0.0283
0.0200
0.0283
MASS FLOW
(lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0009
0.0334
0.2527
0.1430
0.1968
0.0721
0.1152
0.0640
0.0453
0.0766
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.0005
0.0177
0.3682
0.1754
0.1695
0.0560
0.0861
0.0448
0.0314
0.0504
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
MIXED
4.726
0.7738
1.773
0.3992
0.1358
6.454e-002
LIGHT
4.726
0.7738
1.773
0.3992
0.1358
6.454e-002
HEAVY
---
---
---
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 7 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 3 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
K VALUE
COMPONENTS
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
4.709e-002
2.275e-002
1.725e-002
6.627e-003
LIGHT
4.709e-002
2.275e-002
1.725e-002
6.627e-003
HEAVY
---
---
---
---
UNIT OPERATIONS
FEED TO
Tee: TEE-101
PRODUCT FROM
Separator: V-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 895.0 psia
Flow Specification (Inactive) Molar: 194.2 MMSCFD Mass: 3.906e+005 lb/hr Std Ideal Liq Volume:26e+004 barrel/day
User Variables
NOTES
Description
Material Stream: 4Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
-29.00
895.0
49.00 *
9.856e+004
2.076e+004
-3.723e+004
32.93
-2.003e+008
---
Vapour Phase
1.0000
-29.00
895.0
49.00
9.856e+004
2.076e+004
-3.723e+004
32.93
-2.003e+008
---
Liquid Phase
0.0000
-29.00
895.0
0.0000
0.0000
0.0000
-4.949e+004
25.37
0.0000
0.0000
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
Overall
18.32
0.3009
5.512
7.644e+004
-2033
1.798
16.40
0.8952
3.692e+005
2.015e+004
---
2.122e-314
Vapour Phase
18.32
0.3009
5.512
7.644e+004
-2033
1.798
16.40
0.8952
3.692e+005
2.015e+004
1.000
1.000
Liquid Phase
31.86
0.8998
28.67
0.0000
-1553
0.7964
21.23
0.6662
6.237e+005
1.957e+004
---
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 8 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 4 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
16.77
0.0000
298.0
1.108
16.40
49.00
20.30
---
---
18.51
---
1.138
2.361
1639
0.1389
---
---
0.0000
3.324
89.47
1.0000
---
2.004e-002
1.226e-002
14.41
0.7868
6.945
0.3791
6.944
0.3791
2.361
0.0000
0.0000
---
---
Vapour Phase
---
0.0000
298.0
1.108
16.40
49.00
20.30
---
0.6436
18.51
---
1.138
2.361
---
0.1389
---
---
0.0000
3.324
---
1.0000
---
2.004e-002
1.226e-002
14.41
0.7868
6.945
0.3791
6.944
0.3791
2.361
0.0000
---
---
---
Liquid Phase
---
0.0000
---
0.8549
21.23
0.0000
27.24
---
0.2152
15.69
---
1.103
1.103
---
0.2048
16.92
0.0000
1.000
1.111
---
0.0000
7.167
5.377e-002
9.405e-002
19.24
0.6039
19.24
0.6039
---
---
---
0.0000
---
---
1591
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
27.0396
100.8243
4787.2143
325.4240
103.8891
13.7196
15.9921
3.4595
1.8573
1.0101
MOLE FRACTION
0.0050
0.0187
0.8897
0.0605
0.0193
0.0025
0.0030
0.0006
0.0003
0.0002
MASS FLOW
(lb/hr)
757.4603
4437.2491
76800.8008
9785.4667
4581.1994
797.4393
929.5221
249.6063
134.0067
87.0505
MASS FRACTION
0.0077
0.0450
0.7792
0.0993
0.0465
0.0081
0.0094
0.0025
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
64.3193
368.1305
17564.7071
1883.8083
619.1066
97.1641
109.1298
27.4143
14.5711
8.9949
LIQUID VOLUME
FRACTION
0.0031
0.0177
0.8462
0.0908
0.0298
0.0047
0.0053
0.0013
0.0007
0.0004
Total 5380.4300 1.0000 98559.8014 1.0000 20757.3460 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
MOLAR FLOW
(lbmole/hr)
27.0396
MOLE FRACTION
0.0050
MASS FLOW
(lb/hr)
757.4603
MASS FRACTION
0.0077
LIQUID VOLUME
FLOW (barrel/day)
64.3193
LIQUID VOLUME
FRACTION
0.0031
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 9 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 4 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
100.8243
4787.2143
325.4240
103.8891
13.7196
15.9921
3.4595
1.8573
1.0101
MOLE FRACTION
0.0187
0.8897
0.0605
0.0193
0.0025
0.0030
0.0006
0.0003
0.0002
MASS FLOW
(lb/hr)
4437.2491
76800.8008
9785.4667
4581.1994
797.4393
929.5221
249.6063
134.0067
87.0505
MASS FRACTION
0.0450
0.7792
0.0993
0.0465
0.0081
0.0094
0.0025
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
368.1305
17564.7071
1883.8083
619.1066
97.1641
109.1298
27.4143
14.5711
8.9949
LIQUID VOLUME
FRACTION
0.0177
0.8462
0.0908
0.0298
0.0047
0.0053
0.0013
0.0007
0.0004
Total 5380.4300 1.0000 98559.8014 1.0000 20757.3460 1.0000
Liquid Phase Phase Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0011
0.0242
0.5018
0.1515
0.1422
0.0395
0.0631
0.0283
0.0200
0.0283
MASS FLOW
(lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0009
0.0334
0.2527
0.1430
0.1968
0.0721
0.1152
0.0640
0.0453
0.0766
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.0005
0.0177
0.3682
0.1754
0.1695
0.0560
0.0861
0.0448
0.0314
0.0504
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
4.726
0.7738
1.773
0.3992
0.1358
6.454e-002
4.709e-002
2.275e-002
1.725e-002
6.627e-003
LIGHT
4.726
0.7738
1.773
0.3992
0.1358
6.454e-002
4.709e-002
2.275e-002
1.725e-002
6.627e-003
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Heat Exchanger: E-101
PRODUCT FROM
Tee: TEE-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 895.0 psia
Flow Specification (Active) Molar: 49.00 MMSCFD * Mass: 9.856e+004 lb/hr Std Ideal Liq Volume:76e+004 barrel/day
User Variables
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 10 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 4 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
NOTES
Description
Material Stream: 5Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
-29.00
895.0
145.2
2.920e+005
6.150e+004
-3.723e+004
32.93
-5.935e+008
---
Vapour Phase
1.0000
-29.00
895.0
145.2
2.920e+005
6.150e+004
-3.723e+004
32.93
-5.935e+008
---
Liquid Phase
0.0000
-29.00
895.0
0.0000
0.0000
0.0000
-4.949e+004
25.37
0.0000
0.0000
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
Overall
18.32
0.3009
5.512
2.265e+005
-2033
1.798
16.40
0.8952
3.692e+005
2.015e+004
---
2.122e-314
16.77
0.0000
883.1
1.108
16.40
145.2
20.30
---
---
18.51
---
1.138
2.361
1639
0.1389
---
---
0.0000
3.324
89.47
1.0000
---
2.004e-002
Vapour Phase
18.32
0.3009
5.512
2.265e+005
-2033
1.798
16.40
0.8952
3.692e+005
2.015e+004
1.000
1.000
---
0.0000
883.1
1.108
16.40
145.2
20.30
---
0.6436
18.51
---
1.138
2.361
---
0.1389
---
---
0.0000
3.324
---
1.0000
---
2.004e-002
Liquid Phase
31.86
0.8998
28.67
0.0000
-1553
0.7964
21.23
0.6662
6.237e+005
1.957e+004
---
0.0000
---
0.0000
---
0.8549
21.23
0.0000
27.24
---
0.2152
15.69
---
1.103
1.103
---
0.2048
16.92
0.0000
1.000
1.111
---
0.0000
7.167
5.377e-002
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 11 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 5 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(cP)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(barrel/day)
(psia)
(psia)
(psia)
Overall
1.226e-002
14.41
0.7868
6.945
0.3791
6.944
0.3791
2.361
0.0000
0.0000
---
---
Vapour Phase
1.226e-002
14.41
0.7868
6.945
0.3791
6.944
0.3791
2.361
0.0000
---
---
---
Liquid Phase
9.405e-002
19.24
0.6039
19.24
0.6039
---
---
---
0.0000
---
---
1591
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
80.1159
298.7336
14184.0925
964.2025
307.8143
40.6500
47.3830
10.2502
5.5030
2.9929
MOLE FRACTION
0.0050
0.0187
0.8897
0.0605
0.0193
0.0025
0.0030
0.0006
0.0003
0.0002
MASS FLOW
(lb/hr)
2244.2879
13147.1766
227553.9794
28993.4724
13573.6886
2362.7422
2754.0919
739.5614
397.0500
257.9230
MASS FRACTION
0.0077
0.0450
0.7792
0.0993
0.0465
0.0081
0.0094
0.0025
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
190.5725
1090.7381
52042.6735
5581.5572
1834.3580
287.8887
323.3419
81.2263
43.1728
26.6511
LIQUID VOLUME
FRACTION
0.0031
0.0177
0.8462
0.0908
0.0298
0.0047
0.0053
0.0013
0.0007
0.0004
Total 15941.7381 1.0000 292023.9733 1.0000 61502.1801 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
80.1159
298.7336
14184.0925
964.2025
307.8143
40.6500
47.3830
10.2502
5.5030
2.9929
MOLE FRACTION
0.0050
0.0187
0.8897
0.0605
0.0193
0.0025
0.0030
0.0006
0.0003
0.0002
MASS FLOW
(lb/hr)
2244.2879
13147.1766
227553.9794
28993.4724
13573.6886
2362.7422
2754.0919
739.5614
397.0500
257.9230
MASS FRACTION
0.0077
0.0450
0.7792
0.0993
0.0465
0.0081
0.0094
0.0025
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
190.5725
1090.7381
52042.6735
5581.5572
1834.3580
287.8887
323.3419
81.2263
43.1728
26.6511
LIQUID VOLUME
FRACTION
0.0031
0.0177
0.8462
0.0908
0.0298
0.0047
0.0053
0.0013
0.0007
0.0004
Total 15941.7381 1.0000 292023.9733 1.0000 61502.1801 1.0000
Liquid Phase Phase Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0011
0.0242
0.5018
0.1515
0.1422
0.0395
0.0631
0.0283
0.0200
MASS FLOW
(lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0009
0.0334
0.2527
0.1430
0.1968
0.0721
0.1152
0.0640
0.0453
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.0005
0.0177
0.3682
0.1754
0.1695
0.0560
0.0861
0.0448
0.0314
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 12 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 5 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.0000
COMPONENTS
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
MOLE FRACTION
0.0283
MASS FLOW
(lb/hr)
0.0000
MASS FRACTION
0.0766
LIQUID VOLUME
FLOW (barrel/day)
0.0000
LIQUID VOLUME
FRACTION
0.0504
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
4.726
0.7738
1.773
0.3992
0.1358
6.454e-002
4.709e-002
2.275e-002
1.725e-002
6.627e-003
LIGHT
4.726
0.7738
1.773
0.3992
0.1358
6.454e-002
4.709e-002
2.275e-002
1.725e-002
6.627e-003
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Expander: K-100
PRODUCT FROM
Tee: TEE-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 895.0 psia
Flow Specification (Inactive) Molar: 145.2 MMSCFD Mass: 2.920e+005 lb/hr Std Ideal Liq Volume:50e+004 barrel/day
User Variables
NOTES
Description
Material Stream: 9Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
-130.9
160.0
193.2
3.730e+005
8.063e+004
-3.696e+004
35.41
-7.840e+008
---
Vapour Phase
1.0000
-130.9
160.0
193.2
3.730e+005
8.063e+004
-3.696e+004
35.41
-7.840e+008
---
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PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 9 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
Higher Heating Value[Gas]
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
(MMBtu/gal)
Overall
17.58
5.166e-002
0.9084
1.755e+006
-2102
2.013
9.172
0.5216
3.545e+005
2.016e+004
---
4.941e-324
3.131
0.0000
6843
1.124
9.172
193.2
19.77
---
0.8777
18.83
---
1.276
1.494
3603
0.5138
---
---
0.0000
19.36
204.9
1.0000
---
1.074e-002
7.477e-003
7.186
0.4086
6.139
0.3491
5.811
0.3305
1.578
0.0000
0.0000
---
---
1.390e-004
Vapour Phase
17.58
5.166e-002
0.9084
1.755e+006
-2102
2.013
9.172
0.5216
3.545e+005
2.016e+004
1.000
1.000
---
0.0000
6843
1.124
9.172
193.2
19.77
---
0.8777
18.83
---
1.276
1.494
---
0.5138
---
---
0.0000
19.36
---
1.0000
---
1.074e-002
7.477e-003
7.186
0.4086
6.139
0.3491
5.811
0.3305
1.578
0.0000
---
---
---
1.390e-004
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
MOLAR FLOW
(lbmole/hr)
107.8380
415.0990
19293.3260
MOLE FRACTION
0.0051
0.0196
0.9096
MASS FLOW
(lb/hr)
3020.8659
18268.3819
309520.9013
MASS FRACTION
0.0081
0.0490
0.8299
LIQUID VOLUME
FLOW (barrel/day)
256.5153
1515.6122
70788.8970
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 14 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 9 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000
COMPONENTS
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
1377.1300
16.4568
0.3384
0.1913
0.0082
0.0023
0.0002
MOLE FRACTION
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
41410.1612
725.6967
19.6666
11.1211
0.5944
0.1667
0.0130
MASS FRACTION
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
7971.9042
98.0712
2.3963
1.3057
0.0653
0.0181
0.0013
LIQUID VOLUME
FRACTION
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 21210.3902 1.0000 372977.5689 1.0000 80634.7865 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
107.8380
415.0990
19293.3260
1377.1300
16.4568
0.3384
0.1913
0.0082
0.0023
0.0002
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
3020.8659
18268.3819
309520.9013
41410.1612
725.6967
19.6666
11.1211
0.5944
0.1667
0.0130
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
256.5153
1515.6122
70788.8970
7971.9042
98.0712
2.3963
1.3057
0.0653
0.0181
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 21210.3902 1.0000 372977.5689 1.0000 80634.7865 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Heat Exchanger: E-101
PRODUCT FROM
Reboiled Absorber: Deetanizadora
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 160.0 psia
Flow Specification (Inactive) Molar: 193.2 MMSCFD Mass: 3.730e+005 lb/hr Std Ideal Liq Volume:63e+004 barrel/day
User Variables
NOTES
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 15 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 9 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
Description
Material Stream: 10Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.0000
110.1
160.0
6.862
3.805e+004
4834
-5.632e+004
23.65
-4.244e+007
4787 *
Liquid Phase
1.0000
110.1
160.0
6.862
3.805e+004
4834
-5.632e+004
23.65
-4.244e+007
4787
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
Overall
50.50
0.6245
31.54
5158
-1115
0.4682
33.74
0.6682
9.993e+005
1.979e+004
---
2.122e-314
0.0000
0.0000
---
0.6664
33.74
6.863
33.65
150.4
4.190e-002
14.16
---
1.063
1.063
7957
0.2132
33.98
4787
1.000
1.601
157.6
0.0000
6.641
4.927e-002
0.1077
31.76
Liquid Phase
50.50
0.6245
31.54
5158
-1115
0.4682
33.74
0.6682
9.993e+005
1.979e+004
1.000
1.000
---
0.0000
---
0.6664
33.74
6.863
33.65
150.4
4.190e-002
14.16
---
1.063
1.063
---
0.2132
33.98
4787
1.000
1.601
---
1.0000
6.641
4.927e-002
0.1077
31.76
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 16 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 10 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
Higher Heating Value[Gas]
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(barrel/day)
(psia)
(psia)
(psia)
(MMBtu/gal)
Overall
0.6288
31.76
0.6288
32.25
0.6386
1.046
4787
0.0000
134.3
140.9
3.922e-004
Liquid Phase
0.6288
31.76
0.6288
---
---
---
4787
---
134.3
140.9
3.922e-004
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
9.7300
486.4942
79.3866
103.6937
31.8378
20.2037
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0129
0.6456
0.1054
0.1376
0.0423
0.0268
0.0294
MASS FLOW
(lb/hr)
0.0000
0.0009
0.0000
292.5811
21452.9336
4614.2693
6027.0907
2297.1263
1457.7164
1911.6714
MASS FRACTION
0.0000
0.0000
0.0000
0.0077
0.5638
0.1213
0.1584
0.0604
0.0383
0.0502
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0001
0.0000
56.3250
2899.1648
562.2263
707.6057
252.2941
158.5031
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0117
0.5998
0.1163
0.1464
0.0522
0.0328
0.0409
Total 753.5288 1.0000 38053.3897 1.0000 4833.6514 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
9.7300
486.4942
79.3866
103.6937
31.8378
20.2037
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0129
0.6456
0.1054
0.1376
0.0423
0.0268
0.0294
MASS FLOW
(lb/hr)
0.0000
0.0009
0.0000
292.5811
21452.9336
4614.2693
6027.0907
2297.1263
1457.7164
1911.6714
MASS FRACTION
0.0000
0.0000
0.0000
0.0077
0.5638
0.1213
0.1584
0.0604
0.0383
0.0502
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0001
0.0000
56.3250
2899.1648
562.2263
707.6057
252.2941
158.5031
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0117
0.5998
0.1163
0.1464
0.0522
0.0328
0.0409
Total 753.5288 1.0000 38053.3897 1.0000 4833.6514 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
---
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 17 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 10 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
UNIT OPERATIONS
FEED TO
Pump: P-100
PRODUCT FROM
Reboiled Absorber: Deetanizadora
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 160.0 psia
Flow Specification (Inactive) Molar: 6.862 MMSCFD Mass: 3.805e+004 lb/hr Std Ideal Liq Volume: 4834 barrel/day
User Variables
NOTES
Description
Material Stream: 13Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.0000
-115.0 *
885.0
49.00
9.856e+004
2.076e+004
-3.984e+004
26.15
-2.144e+008
---
Liquid Phase
1.0000
-115.0
885.0
49.00
9.856e+004
2.076e+004
-3.984e+004
26.15
-2.144e+008
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
Overall
18.32
1.121
20.54
2.051e+004
-2175
1.428
20.84
1.138
3.692e+005
2.015e+004
---
2.122e-314
0.0000
0.0000
---
1.108
20.84
49.00
20.30
Liquid Phase
18.32
1.121
20.54
2.051e+004
-2175
1.428
20.84
1.138
3.692e+005
2.015e+004
1.000
1.000
---
0.0000
---
1.108
20.84
49.00
20.30
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 18 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 13 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
598.2
0.2134
18.51
---
1.105
3.286
1698
0.1183
---
---
1.000
0.8918
92.68
0.0000
1.995
4.489e-002
3.891e-002
18.86
1.029
6.343
0.3463
---
---
---
0.0000
0.0000
---
---
Liquid Phase
598.2
0.2134
18.51
---
1.105
3.286
---
0.1183
---
---
1.000
0.8918
---
1.0000
1.995
4.489e-002
3.891e-002
18.86
1.029
6.343
0.3463
---
---
---
0.0000
---
---
---
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
27.0396
100.8243
4787.2143
325.4240
103.8891
13.7196
15.9921
3.4595
1.8573
1.0101
MOLE FRACTION
0.0050
0.0187
0.8897
0.0605
0.0193
0.0025
0.0030
0.0006
0.0003
0.0002
MASS FLOW
(lb/hr)
757.4603
4437.2491
76800.8008
9785.4667
4581.1994
797.4393
929.5221
249.6063
134.0067
87.0505
MASS FRACTION
0.0077
0.0450
0.7792
0.0993
0.0465
0.0081
0.0094
0.0025
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
64.3193
368.1305
17564.7071
1883.8083
619.1066
97.1641
109.1298
27.4143
14.5711
8.9949
LIQUID VOLUME
FRACTION
0.0031
0.0177
0.8462
0.0908
0.0298
0.0047
0.0053
0.0013
0.0007
0.0004
Total 5380.4300 1.0000 98559.8014 1.0000 20757.3460 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
MOLAR FLOW
(lbmole/hr)
27.0396
100.8243
4787.2143
325.4240
103.8891
13.7196
15.9921
3.4595
MOLE FRACTION
0.0050
0.0187
0.8897
0.0605
0.0193
0.0025
0.0030
0.0006
MASS FLOW
(lb/hr)
757.4603
4437.2491
76800.8008
9785.4667
4581.1994
797.4393
929.5221
249.6063
MASS FRACTION
0.0077
0.0450
0.7792
0.0993
0.0465
0.0081
0.0094
0.0025
LIQUID VOLUME
FLOW (barrel/day)
64.3193
368.1305
17564.7071
1883.8083
619.1066
97.1641
109.1298
27.4143
LIQUID VOLUME
FRACTION
0.0031
0.0177
0.8462
0.0908
0.0298
0.0047
0.0053
0.0013
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 19 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 13 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 1.000
COMPONENTS
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
1.8573
1.0101
MOLE FRACTION
0.0003
0.0002
MASS FLOW
(lb/hr)
134.0067
87.0505
MASS FRACTION
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
14.5711
8.9949
LIQUID VOLUME
FRACTION
0.0007
0.0004
Total 5380.4300 1.0000 98559.8014 1.0000 20757.3460 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Valve: VLV-100
PRODUCT FROM
Heat Exchanger: E-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 885.0 psia
Flow Specification (Inactive) Molar: 49.00 MMSCFD Mass: 9.856e+004 lb/hr Std Ideal Liq Volume:76e+004 barrel/day
User Variables
NOTES
Description
Material Stream: 14Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.3975
-178.9
165.0 *
49.00
9.856e+004
2.076e+004
-3.984e+004
26.90
-2.144e+008
---
Vapour Phase
0.3975
-178.9
165.0
19.48
3.489e+004
7832
-3.467e+004
33.31
-7.415e+007
---
Liquid Phase
0.6025
-178.9
165.0
29.52
6.367e+004
1.293e+004
-4.326e+004
22.67
-1.402e+008
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 20 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 14 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
18.32
0.1562
2.861
1.473e+005
-2175
1.469
13.19
0.7202
3.692e+005
2.015e+004
0.3773
0.3540
0.5531
0.0000
---
1.108
13.19
49.00
20.30
295.7
---
18.51
---
1.177
1.133
4537
---
---
---
0.6025
6.404
247.7
0.3975
7.996
---
---
11.21
0.6118
11.65
0.6358
---
---
---
0.0000
0.0000
---
---
Vapour Phase
16.31
6.667e-002
1.087
1.371e+005
-2126
2.042
9.670
0.5928
3.411e+005
2.091e+004
0.3773
0.3540
---
0.0000
534.7
1.167
9.670
19.48
19.04
---
0.8213
19.18
---
1.258
1.613
---
0.3796
---
---
0.0000
15.00
---
0.3975
---
9.563e-003
6.612e-003
7.684
0.4711
5.993
0.3674
6.003
0.3680
1.611
0.0000
---
---
---
Liquid Phase
19.64
1.367
26.85
1.014e+004
-2202
1.154
15.52
0.7900
3.877e+005
1.974e+004
0.6227
0.6460
---
0.0000
---
1.072
15.52
29.52
21.06
295.7
4.006e-002
18.15
---
1.147
1.147
---
0.1909
---
---
1.000
0.7317
---
0.6025
7.996
7.962e-002
8.211e-002
13.53
0.6889
13.53
0.6889
---
---
---
0.0000
---
---
---
COMPOSITION
Overall Phase Vapour Fraction 0.3975
COMPONENTS
Nitrogen
CO2
Methane
Ethane
MOLAR FLOW
(lbmole/hr)
27.0396
100.8243
4787.2143
325.4240
MOLE FRACTION
0.0050
0.0187
0.8897
0.0605
MASS FLOW
(lb/hr)
757.4603
4437.2491
76800.8008
9785.4667
MASS FRACTION
0.0077
0.0450
0.7792
0.0993
LIQUID VOLUME
FLOW (barrel/day)
64.3193
368.1305
17564.7071
1883.8083
LIQUID VOLUME
FRACTION
0.0031
0.0177
0.8462
0.0908
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 21 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 14 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.3975
COMPONENTS
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
103.8891
13.7196
15.9921
3.4595
1.8573
1.0101
MOLE FRACTION
0.0193
0.0025
0.0030
0.0006
0.0003
0.0002
MASS FLOW
(lb/hr)
4581.1994
797.4393
929.5221
249.6063
134.0067
87.0505
MASS FRACTION
0.0465
0.0081
0.0094
0.0025
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
619.1066
97.1641
109.1298
27.4143
14.5711
8.9949
LIQUID VOLUME
FRACTION
0.0298
0.0047
0.0053
0.0013
0.0007
0.0004
Total 5380.4300 1.0000 98559.8014 1.0000 20757.3460 1.0000
Vapour Phase Phase Fraction 0.3975
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
22.9853
7.1699
2101.9739
6.6032
0.1450
0.0028
0.0016
0.0001
0.0000
0.0000
MOLE FRACTION
0.0107
0.0034
0.9827
0.0031
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
643.8873
315.5436
33721.7568
198.5564
6.3963
0.1656
0.0923
0.0039
0.0010
0.0001
MASS FRACTION
0.0185
0.0090
0.9666
0.0057
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
54.6754
26.1787
7712.3256
38.2243
0.8644
0.0202
0.0108
0.0004
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.0070
0.0033
0.9847
0.0049
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
Total 2138.8818 1.0000 34886.4033 1.0000 7832.2998 1.0000
Liquid Phase Phase Fraction 0.6025
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
4.0543
93.6545
2685.2404
318.8208
103.7441
13.7168
15.9905
3.4594
1.8573
1.0101
MOLE FRACTION
0.0013
0.0289
0.8284
0.0984
0.0320
0.0042
0.0049
0.0011
0.0006
0.0003
MASS FLOW
(lb/hr)
113.5730
4121.7056
43079.0441
9586.9103
4574.8031
797.2737
929.4298
249.6024
134.0057
87.0505
MASS FRACTION
0.0018
0.0647
0.6766
0.1506
0.0718
0.0125
0.0146
0.0039
0.0021
0.0014
LIQUID VOLUME
FLOW (barrel/day)
9.6440
341.9519
9852.3815
1845.5840
618.2422
97.1439
109.1190
27.4139
14.5709
8.9949
LIQUID VOLUME
FRACTION
0.0007
0.0265
0.7623
0.1428
0.0478
0.0075
0.0084
0.0021
0.0011
0.0007
Total 3241.5482 1.0000 63673.3981 1.0000 12925.0462 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
8.592
0.1160
1.186
3.139e-002
2.119e-003
3.148e-004
1.505e-004
2.367e-005
1.158e-005
1.000e-006
LIGHT
8.592
0.1160
1.186
3.139e-002
2.119e-003
3.148e-004
1.505e-004
2.367e-005
1.158e-005
1.000e-006
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Reboiled Absorber: Deetanizadora
PRODUCT FROM
Valve: VLV-100
LOGICAL CONNECTION
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 22 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 14 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Active): 165.0 psia *
Flow Specification (Inactive) Molar: 49.00 MMSCFD Mass: 9.856e+004 lb/hr Std Ideal Liq Volume:76e+004 barrel/day
User Variables
NOTES
Description
Material Stream: 16Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
-57.54
155.0
193.2
3.730e+005
8.063e+004
-3.630e+004
37.28
-7.700e+008
---
Vapour Phase
1.0000
-57.54
155.0
193.2
3.730e+005
8.063e+004
-3.630e+004
37.28
-7.700e+008
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
Overall
17.58
3.842e-002
0.6756
2.360e+006
-2064
2.120
8.837
0.5025
3.545e+005
2.016e+004
---
4.941e-324
3.033
0.0000
9201
1.124
8.837
193.2
19.77
---
0.9348
18.83
---
Vapour Phase
17.58
3.842e-002
0.6756
2.360e+006
-2064
2.120
8.837
0.5025
3.545e+005
2.016e+004
1.000
1.000
---
0.0000
9201
1.124
8.837
193.2
19.77
---
0.9348
18.83
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 23 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 16 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
1.290
1.400
3623
0.8212
---
---
0.0000
26.03
206.0
1.0000
---
1.343e-002
8.887e-003
6.851
0.3896
6.311
0.3589
6.128
0.3485
1.442
0.0000
0.0000
---
---
Vapour Phase
1.290
1.400
---
0.8212
---
---
0.0000
26.03
---
1.0000
---
1.343e-002
8.887e-003
6.851
0.3896
6.311
0.3589
6.128
0.3485
1.442
0.0000
---
---
---
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
107.8380
415.0990
19293.3260
1377.1300
16.4568
0.3384
0.1913
0.0082
0.0023
0.0002
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
3020.8659
18268.3819
309520.9013
41410.1612
725.6967
19.6666
11.1211
0.5944
0.1667
0.0130
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
256.5153
1515.6122
70788.8970
7971.9042
98.0712
2.3963
1.3057
0.0653
0.0181
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 21210.3902 1.0000 372977.5689 1.0000 80634.7865 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
107.8380
415.0990
19293.3260
1377.1300
16.4568
0.3384
0.1913
0.0082
0.0023
0.0002
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
3020.8659
18268.3819
309520.9013
41410.1612
725.6967
19.6666
11.1211
0.5944
0.1667
0.0130
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
256.5153
1515.6122
70788.8970
7971.9042
98.0712
2.3963
1.3057
0.0653
0.0181
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 21210.3902 1.0000 372977.5689 1.0000 80634.7865 1.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 24 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 16 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Heat Exchanger: E-100
PRODUCT FROM
Heat Exchanger: E-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 155.0 psia
Flow Specification (Inactive) Molar: 193.2 MMSCFD Mass: 3.730e+005 lb/hr Std Ideal Liq Volume:63e+004 barrel/day
User Variables
NOTES
Description
Material Stream: 21Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.4604
-90.36
165.0
5.844
2.045e+004
3209
-4.949e+004
26.48
-3.176e+007
5166 *
Vapour Phase
0.4604
-90.36
165.0
2.691
5321
1133
-3.754e+004
36.42
-1.109e+007
---
Liquid Phase
0.5396
-90.36
165.0
3.154
1.513e+004
2076
-5.968e+004
18.00
-2.067e+007
2065
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
Overall
31.86
9.399e-002
2.995
2.919e+004
-1553
0.8312
Vapour Phase
18.01
4.592e-002
0.8268
2.751e+004
-2085
2.023
Liquid Phase
43.68
0.8807
38.47
1681
-1366
0.4121
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 25 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 21 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
15.61
0.4899
6.237e+005
1.957e+004
0.3529
0.2602
4.047
0.0000
---
0.8549
15.61
5.845
27.24
49.02
---
15.69
---
1.146
1.093
9367
---
16.92
5166
0.5396
10.64
294.0
0.4604
16.27
---
---
13.62
0.4276
14.29
0.4484
20.05
0.6292
0.7786
2065
0.0000
---
1591
Vapour Phase
9.062
0.5032
3.598e+005
1.998e+004
0.3529
0.2602
---
0.0000
107.2
1.115
9.062
2.691
20.08
---
0.9067
18.64
---
1.281
1.440
---
0.6236
---
---
0.0000
21.78
---
0.4604
---
1.210e-002
8.260e-003
7.076
0.3930
6.293
0.3494
6.261
0.3477
1.447
0.0000
---
---
---
Liquid Phase
21.20
0.4852
8.488e+005
1.943e+004
0.6471
0.7398
---
0.0000
---
0.7129
21.20
3.154
31.14
49.02
4.727e-002
14.77
---
1.103
1.103
---
0.4327
31.32
2065
1.000
1.136
---
0.5396
16.27
7.192e-002
0.2667
19.21
0.4397
19.21
0.4397
---
---
---
2065
---
373.0
705.8
COMPOSITION
Overall Phase Vapour Fraction 0.4604
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.6825
15.5411
322.0192
97.2335
91.2475
25.3554
40.5099
18.1363
12.8456
18.1800
MOLE FRACTION
0.0011
0.0242
0.5018
0.1515
0.1422
0.0395
0.0631
0.0283
0.0200
0.0283
MASS FLOW
(lb/hr)
19.1178
683.9570
5166.1211
2923.8031
4023.7423
1473.7545
2354.5978
1308.5531
926.8265
1566.7108
MASS FRACTION
0.0009
0.0334
0.2527
0.1430
0.1968
0.0721
0.1152
0.0640
0.0453
0.0766
LIQUID VOLUME
FLOW (barrel/day)
1.6234
56.7436
1181.5164
562.8637
543.7714
179.5698
276.4397
143.7188
100.7774
161.8877
LIQUID VOLUME
FRACTION
0.0005
0.0177
0.3682
0.1754
0.1695
0.0560
0.0861
0.0448
0.0314
0.0504
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 26 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 21 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.4604
Total 641.7509 1.0000 20447.1840 1.0000 3208.9118 1.0000
Vapour Phase Phase Fraction 0.4604
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.6600
7.2473
264.7009
19.7556
2.7448
0.1812
0.1576
0.0171
0.0069
0.0015
MOLE FRACTION
0.0022
0.0245
0.8959
0.0669
0.0093
0.0006
0.0005
0.0001
0.0000
0.0000
MASS FLOW
(lb/hr)
18.4886
318.9515
4246.5700
594.0498
121.0358
10.5304
9.1598
1.2360
0.4987
0.1275
MASS FRACTION
0.0035
0.0599
0.7981
0.1116
0.0227
0.0020
0.0017
0.0002
0.0001
0.0000
LIQUID VOLUME
FLOW (barrel/day)
1.5699
26.4614
971.2107
114.3610
16.3569
1.2831
1.0754
0.1357
0.0542
0.0132
LIQUID VOLUME
FRACTION
0.0014
0.0234
0.8576
0.1010
0.0144
0.0011
0.0009
0.0001
0.0000
0.0000
Total 295.4729 1.0000 5320.6479 1.0000 1132.5215 1.0000
Liquid Phase Phase Fraction 0.5396
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0225
8.2938
57.3183
77.4779
88.5028
25.1742
40.3523
18.1192
12.8387
18.1785
MOLE FRACTION
0.0001
0.0240
0.1655
0.2237
0.2556
0.0727
0.1165
0.0523
0.0371
0.0525
MASS FLOW
(lb/hr)
0.6292
365.0055
919.5511
2329.7533
3902.7065
1463.2241
2345.4380
1307.3171
926.3278
1566.5833
MASS FRACTION
0.0000
0.0241
0.0608
0.1540
0.2580
0.0967
0.1551
0.0864
0.0612
0.1036
LIQUID VOLUME
FLOW (barrel/day)
0.0534
30.2822
210.3057
448.5027
527.4146
178.2868
275.3643
143.5830
100.7231
161.8745
LIQUID VOLUME
FRACTION
0.0000
0.0146
0.1013
0.2160
0.2540
0.0859
0.1326
0.0692
0.0485
0.0780
Total 346.2781 1.0000 15126.5360 1.0000 2076.3903 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
34.44
1.024
5.412
0.2988
3.635e-002
8.434e-003
4.577e-003
1.108e-003
6.309e-004
9.538e-005
LIGHT
34.44
1.024
5.412
0.2988
3.635e-002
8.434e-003
4.577e-003
1.108e-003
6.309e-004
9.538e-005
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Reboiled Absorber: Deetanizadora
PRODUCT FROM
Valve: VLV-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 27 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 21 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
DYNAMICS
Pressure Specification (Inactive) 165.0 psia
Flow Specification (Inactive) Molar: 5.844 MMSCFD Mass: 2.045e+004 lb/hr Std Ideal Liq Volume: 3209 barrel/day
User Variables
NOTES
Description
Material Stream: 22Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.9067
-138.5
165.0 *
145.2
2.920e+005
6.150e+004
-3.788e+004
33.61
-6.038e+008
---
Vapour Phase
0.9067
-138.5
165.0
131.6
2.462e+005
5.394e+004
-3.636e+004
34.88
-5.255e+008
---
Liquid Phase
0.0933
-138.5
165.0
13.55
4.578e+004
7566
-5.263e+004
21.32
-7.831e+007
1.094e+004
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
Overall
18.32
6.022e-002
1.103
1.132e+006
-2068
1.835
9.877
0.5392
3.692e+005
2.015e+004
0.8770
0.8432
2.623
0.0000
---
1.108
9.877
145.2
20.30
162.9
---
18.51
---
1.252
1.397
4537
---
---
---
Vapour Phase
17.04
5.487e-002
0.9349
1.126e+006
-2134
2.047
9.155
0.5374
3.470e+005
2.037e+004
0.8770
0.8432
---
0.0000
4390
1.146
9.155
131.6
19.52
---
0.8724
18.91
---
1.277
1.509
---
0.4920
---
---
Liquid Phase
30.77
1.138
35.03
5587
-1711
0.6929
16.89
0.5488
5.849e+005
1.901e+004
0.1230
0.1568
---
0.0000
---
0.8406
16.89
13.55
25.86
162.9
4.205e-002
16.49
---
1.133
1.851
---
0.3191
17.89
1.094e+004
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 28 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 22 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
9.334e-002
16.60
247.7
0.9067
13.99
---
---
7.891
0.4308
7.068
0.3858
14.53
0.7934
0.6796
1.094e+004
0.0000
---
---
Vapour Phase
0.0000
18.22
---
0.9067
---
1.069e-002
7.368e-003
7.170
0.4208
6.067
0.3561
6.058
0.3556
1.511
0.0000
---
---
---
Liquid Phase
1.000
0.8784
---
0.0933
13.99
7.744e-002
0.1790
14.90
0.4843
9.125
0.2966
---
---
---
1.094e+004
---
---
1166
COMPOSITION
Overall Phase Vapour Fraction 0.9067
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
80.1159
298.7336
14184.0925
964.2025
307.8143
40.6500
47.3830
10.2502
5.5030
2.9929
MOLE FRACTION
0.0050
0.0187
0.8897
0.0605
0.0193
0.0025
0.0030
0.0006
0.0003
0.0002
MASS FLOW
(lb/hr)
2244.2879
13147.1766
227553.9794
28993.4724
13573.6886
2362.7422
2754.0919
739.5614
397.0500
257.9230
MASS FRACTION
0.0077
0.0450
0.7792
0.0993
0.0465
0.0081
0.0094
0.0025
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
190.5725
1090.7381
52042.6735
5581.5572
1834.3580
287.8887
323.3419
81.2263
43.1728
26.6511
LIQUID VOLUME
FRACTION
0.0031
0.0177
0.8462
0.0908
0.0298
0.0047
0.0053
0.0013
0.0007
0.0004
Total 15941.7381 1.0000 292023.9733 1.0000 61502.1801 1.0000
Vapour Phase Phase Fraction 0.9067
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
79.7205
229.7835
13669.7373
452.2437
21.4515
0.5487
0.3130
0.0132
0.0036
0.0002
MOLE FRACTION
0.0055
0.0159
0.9458
0.0313
0.0015
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
2233.2099
10112.7024
219302.2291
13598.9223
945.9447
31.8898
18.1920
0.9490
0.2580
0.0184
MASS FRACTION
0.0091
0.0411
0.8906
0.0552
0.0038
0.0001
0.0001
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
189.6318
838.9870
50155.4591
2617.9397
127.8356
3.8856
2.1358
0.1042
0.0281
0.0019
LIQUID VOLUME
FRACTION
0.0035
0.0156
0.9299
0.0485
0.0024
0.0001
0.0000
0.0000
0.0000
0.0000
Total 14453.8149 1.0000 246244.3155 1.0000 53936.0089 1.0000
Liquid Phase Phase Fraction 9.334e-002
COMPONENTS
Nitrogen
CO2
Methane
MOLAR FLOW
(lbmole/hr)
0.3955
68.9501
514.3553
MOLE FRACTION
0.0003
0.0463
0.3457
MASS FLOW
(lb/hr)
11.0780
3034.4743
8251.7502
MASS FRACTION
0.0002
0.0663
0.1802
LIQUID VOLUME
FLOW (barrel/day)
0.9407
251.7511
1887.2144
LIQUID VOLUME
FRACTION
0.0001
0.0333
0.2494
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 29 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 22 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 9.334e-002
COMPONENTS
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
511.9588
286.3629
40.1014
47.0701
10.2370
5.4995
2.9927
MOLE FRACTION
0.3441
0.1925
0.0270
0.0316
0.0069
0.0037
0.0020
MASS FLOW
(lb/hr)
15394.5501
12627.7439
2330.8524
2735.8998
738.6124
396.7920
257.9046
MASS FRACTION
0.3363
0.2758
0.0509
0.0598
0.0161
0.0087
0.0056
LIQUID VOLUME
FLOW (barrel/day)
2963.6175
1706.5224
284.0030
321.2061
81.1220
43.1447
26.6492
LIQUID VOLUME
FRACTION
0.3917
0.2255
0.0375
0.0425
0.0107
0.0057
0.0035
Total 1487.9232 1.0000 45779.6577 1.0000 7566.1712 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
20.75
0.3431
2.736
9.094e-002
7.711e-003
1.408e-003
6.845e-004
1.323e-004
6.693e-005
7.359e-006
LIGHT
20.75
0.3431
2.736
9.094e-002
7.711e-003
1.408e-003
6.845e-004
1.323e-004
6.693e-005
7.359e-006
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Reboiled Absorber: Deetanizadora
PRODUCT FROM
Expander: K-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Active): 165.0 psia *
Flow Specification (Inactive) Molar: 145.2 MMSCFD Mass: 2.920e+005 lb/hr Std Ideal Liq Volume:50e+004 barrel/day
User Variables
NOTES
Description
Material Stream: 30Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Overall
1.0000
151.6
150.0
193.2
3.730e+005
Vapour Phase
1.0000
151.6
150.0
193.2
3.730e+005
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 30 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 30 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
8.063e+004
-3.440e+004
41.14
-7.297e+008
---
Vapour Phase
8.063e+004
-3.440e+004
41.14
-7.297e+008
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
17.58
2.325e-002
0.4088
3.900e+006
-1956
2.340
9.520
0.5414
3.545e+005
2.016e+004
---
4.941e-324
2.936
0.0000
1.521e+004
1.124
9.520
193.2
19.77
---
0.9836
18.83
---
1.264
1.294
3643
1.954
---
---
0.0000
43.01
207.2
1.0000
---
2.253e-002
1.280e-002
7.534
0.4285
7.358
0.4184
7.146
0.4064
1.332
0.0000
0.0000
---
---
Vapour Phase
17.58
2.325e-002
0.4088
3.900e+006
-1956
2.340
9.520
0.5414
3.545e+005
2.016e+004
1.000
1.000
---
0.0000
1.521e+004
1.124
9.520
193.2
19.77
---
0.9836
18.83
---
1.264
1.294
---
1.954
---
---
0.0000
43.01
---
1.0000
---
2.253e-002
1.280e-002
7.534
0.4285
7.358
0.4184
7.146
0.4064
1.332
0.0000
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 31 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 30 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
107.8380
415.0990
19293.3260
1377.1300
16.4568
0.3384
0.1913
0.0082
0.0023
0.0002
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
3020.8659
18268.3819
309520.9013
41410.1612
725.6967
19.6666
11.1211
0.5944
0.1667
0.0130
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
256.5153
1515.6122
70788.8970
7971.9042
98.0712
2.3963
1.3057
0.0653
0.0181
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 21210.3902 1.0000 372977.5689 1.0000 80634.7865 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
107.8380
415.0990
19293.3260
1377.1300
16.4568
0.3384
0.1913
0.0082
0.0023
0.0002
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
3020.8659
18268.3819
309520.9013
41410.1612
725.6967
19.6666
11.1211
0.5944
0.1667
0.0130
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
256.5153
1515.6122
70788.8970
7971.9042
98.0712
2.3963
1.3057
0.0653
0.0181
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 21210.3902 1.0000 372977.5689 1.0000 80634.7865 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Tee: TEE-102
PRODUCT FROM
Heat Exchanger: E-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 150.0 psia
Flow Specification (Inactive) Molar: 193.2 MMSCFD Mass: 3.730e+005 lb/hr Std Ideal Liq Volume:63e+004 barrel/day
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 32 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 30 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
User Variables
NOTES
Description
Material Stream: 31Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
151.6
150.0
189.1
3.651e+005
7.893e+004
-3.440e+004
41.14
-7.142e+008
---
Vapour Phase
1.0000
151.6
150.0
189.1
3.651e+005
7.893e+004
-3.440e+004
41.14
-7.142e+008
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
Overall
17.58
2.325e-002
0.4088
3.818e+006
-1956
2.340
9.520
0.5414
3.545e+005
2.016e+004
---
4.941e-324
2.936
0.0000
1.488e+004
1.124
9.520
189.1
19.77
---
0.9836
18.83
---
1.264
1.294
3643
1.954
---
---
0.0000
43.01
207.2
1.0000
Vapour Phase
17.58
2.325e-002
0.4088
3.818e+006
-1956
2.340
9.520
0.5414
3.545e+005
2.016e+004
1.000
1.000
---
0.0000
1.488e+004
1.124
9.520
189.1
19.77
---
0.9836
18.83
---
1.264
1.294
---
1.954
---
---
0.0000
43.01
---
1.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 33 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 31 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
---
2.253e-002
1.280e-002
7.534
0.4285
7.358
0.4184
7.146
0.4064
1.332
0.0000
0.0000
---
---
Vapour Phase
---
2.253e-002
1.280e-002
7.534
0.4285
7.358
0.4184
7.146
0.4064
1.332
0.0000
---
---
---
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
105.5603
406.3313
18885.8148
1348.0424
16.1092
0.3312
0.1873
0.0081
0.0023
0.0001
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
2957.0596
17882.5195
302983.2404
40535.5010
710.3686
19.2512
10.8862
0.5819
0.1632
0.0127
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
251.0972
1483.5996
69293.7030
7803.5226
95.9997
2.3457
1.2781
0.0639
0.0177
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 20762.3870 1.0000 365099.5844 1.0000 78931.6289 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
105.5603
406.3313
18885.8148
1348.0424
16.1092
0.3312
0.1873
0.0081
0.0023
0.0001
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
2957.0596
17882.5195
302983.2404
40535.5010
710.3686
19.2512
10.8862
0.5819
0.1632
0.0127
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
251.0972
1483.5996
69293.7030
7803.5226
95.9997
2.3457
1.2781
0.0639
0.0177
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 20762.3870 1.0000 365099.5844 1.0000 78931.6289 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
MIXED
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 34 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 31 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
K VALUE
COMPONENTS
n-Pentane
n-Hexane
MIXED
---
---
LIGHT
---
---
HEAVY
---
---
UNIT OPERATIONS
FEED TO
Compressor: K-101
PRODUCT FROM
Tee: TEE-102
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 150.0 psia
Flow Specification (Inactive) Molar: 189.1 MMSCFD Mass: 3.651e+005 lb/hr Std Ideal Liq Volume:93e+004 barrel/day
User Variables
NOTES
Description
Material Stream: 33Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
205.0
202.7
189.1
3.651e+005
7.893e+004
-3.391e+004
41.33
-7.040e+008
---
Vapour Phase
1.0000
205.0
202.7
189.1
3.651e+005
7.893e+004
-3.391e+004
41.33
-7.040e+008
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
Overall
17.58
2.888e-002
0.5079
3.073e+006
-1928
2.350
9.908
0.5634
3.545e+005
2.016e+004
---
4.941e-324
3.967
0.0000
Vapour Phase
17.58
2.888e-002
0.5079
3.073e+006
-1928
2.350
9.908
0.5634
3.545e+005
2.016e+004
1.000
1.000
---
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 35 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 33 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
1.198e+004
1.124
9.908
189.1
19.77
---
0.9840
18.83
---
1.251
1.282
3436
1.693
---
---
0.0000
34.62
195.4
1.0000
---
2.524e-002
1.377e-002
7.922
0.4505
7.727
0.4394
7.707
0.4383
1.286
0.0000
0.0000
---
---
Vapour Phase
1.198e+004
1.124
9.908
189.1
19.77
---
0.9840
18.83
---
1.251
1.282
---
1.693
---
---
0.0000
34.62
---
1.0000
---
2.524e-002
1.377e-002
7.922
0.4505
7.727
0.4394
7.707
0.4383
1.286
0.0000
---
---
---
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
105.5603
406.3313
18885.8148
1348.0424
16.1092
0.3312
0.1873
0.0081
0.0023
0.0001
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
2957.0596
17882.5195
302983.2404
40535.5010
710.3686
19.2512
10.8862
0.5819
0.1632
0.0127
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
251.0972
1483.5996
69293.7030
7803.5226
95.9997
2.3457
1.2781
0.0639
0.0177
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 20762.3870 1.0000 365099.5844 1.0000 78931.6289 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
MOLAR FLOW
(lbmole/hr)
105.5603
406.3313
18885.8148
MOLE FRACTION
0.0051
0.0196
0.9096
MASS FLOW
(lb/hr)
2957.0596
17882.5195
302983.2404
MASS FRACTION
0.0081
0.0490
0.8299
LIQUID VOLUME
FLOW (barrel/day)
251.0972
1483.5996
69293.7030
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 36 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 33 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
1348.0424
16.1092
0.3312
0.1873
0.0081
0.0023
0.0001
MOLE FRACTION
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
40535.5010
710.3686
19.2512
10.8862
0.5819
0.1632
0.0127
MASS FRACTION
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
7803.5226
95.9997
2.3457
1.2781
0.0639
0.0177
0.0013
LIQUID VOLUME
FRACTION
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 20762.3870 1.0000 365099.5844 1.0000 78931.6289 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Air cooler: AC-101
PRODUCT FROM
Compressor: K-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 202.7 psia
Flow Specification (Inactive) Molar: 189.1 MMSCFD Mass: 3.651e+005 lb/hr Std Ideal Liq Volume:93e+004 barrel/day
User Variables
NOTES
Description
Material Stream: 34Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Overall
1.0000
120.0 *
213.0 *
189.1
3.651e+005
Vapour Phase
1.0000
120.0
213.0
189.1
3.651e+005
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 37 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 34 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
7.893e+004
-3.473e+004
39.90
-7.211e+008
---
Vapour Phase
7.893e+004
-3.473e+004
39.90
-7.211e+008
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
17.58
3.523e-002
0.6195
2.519e+006
-1975
2.269
9.447
0.5372
3.545e+005
2.016e+004
---
4.941e-324
4.169
0.0000
9823
1.124
9.447
189.1
19.77
---
0.9721
18.83
---
1.266
1.317
3397
1.241
---
---
0.0000
28.39
193.2
1.0000
---
2.125e-002
1.232e-002
7.461
0.4243
7.171
0.4078
7.170
0.4078
1.317
0.0000
0.0000
---
---
Vapour Phase
17.58
3.523e-002
0.6195
2.519e+006
-1975
2.269
9.447
0.5372
3.545e+005
2.016e+004
1.000
1.000
---
0.0000
9823
1.124
9.447
189.1
19.77
---
0.9721
18.83
---
1.266
1.317
---
1.241
---
---
0.0000
28.39
---
1.0000
---
2.125e-002
1.232e-002
7.461
0.4243
7.171
0.4078
7.170
0.4078
1.317
0.0000
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 38 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 34 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
105.5603
406.3313
18885.8148
1348.0424
16.1092
0.3312
0.1873
0.0081
0.0023
0.0001
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
2957.0596
17882.5195
302983.2404
40535.5010
710.3686
19.2512
10.8862
0.5819
0.1632
0.0127
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
251.0972
1483.5996
69293.7030
7803.5226
95.9997
2.3457
1.2781
0.0639
0.0177
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 20762.3870 1.0000 365099.5844 1.0000 78931.6289 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
105.5603
406.3313
18885.8148
1348.0424
16.1092
0.3312
0.1873
0.0081
0.0023
0.0001
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
2957.0596
17882.5195
302983.2404
40535.5010
710.3686
19.2512
10.8862
0.5819
0.1632
0.0127
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
251.0972
1483.5996
69293.7030
7803.5226
95.9997
2.3457
1.2781
0.0639
0.0177
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 20762.3870 1.0000 365099.5844 1.0000 78931.6289 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Compressor: K-102
PRODUCT FROM
Air cooler: AC-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Active): 213.0 psia *
Flow Specification (Inactive) Molar: 189.1 MMSCFD Mass: 3.651e+005 lb/hr Std Ideal Liq Volume:93e+004 barrel/day
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 39 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 34 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
User Variables
NOTES
Description
Material Stream: 40Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
248.0
440.0 *
189.1
3.651e+005
7.893e+004
-3.356e+004
40.33
-6.968e+008
---
Vapour Phase
1.0000
248.0
440.0
189.1
3.651e+005
7.893e+004
-3.356e+004
40.33
-6.968e+008
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
Overall
17.58
5.944e-002
1.045
1.493e+006
-1908
2.293
10.42
0.5927
3.545e+005
2.016e+004
---
4.941e-324
8.611
0.0000
5821
1.124
10.42
189.1
19.77
---
0.9747
18.83
---
1.235
1.292
2559
0.8796
---
---
0.0000
16.82
145.5
1.0000
Vapour Phase
17.58
5.944e-002
1.045
1.493e+006
-1908
2.293
10.42
0.5927
3.545e+005
2.016e+004
1.000
1.000
---
0.0000
5821
1.124
10.42
189.1
19.77
---
0.9747
18.83
---
1.235
1.292
---
0.8796
---
---
0.0000
16.82
---
1.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 40 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 40 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
---
2.797e-002
1.473e-002
8.436
0.4797
8.068
0.4588
8.068
0.4588
1.292
0.0000
0.0000
---
---
Vapour Phase
---
2.797e-002
1.473e-002
8.436
0.4797
8.068
0.4588
8.068
0.4588
1.292
0.0000
---
---
---
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
105.5603
406.3313
18885.8148
1348.0424
16.1092
0.3312
0.1873
0.0081
0.0023
0.0001
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
2957.0596
17882.5195
302983.2404
40535.5010
710.3686
19.2512
10.8862
0.5819
0.1632
0.0127
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
251.0972
1483.5996
69293.7030
7803.5226
95.9997
2.3457
1.2781
0.0639
0.0177
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 20762.3870 1.0000 365099.5844 1.0000 78931.6289 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
105.5603
406.3313
18885.8148
1348.0424
16.1092
0.3312
0.1873
0.0081
0.0023
0.0001
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
2957.0596
17882.5195
302983.2404
40535.5010
710.3686
19.2512
10.8862
0.5819
0.1632
0.0127
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
251.0972
1483.5996
69293.7030
7803.5226
95.9997
2.3457
1.2781
0.0639
0.0177
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 20762.3870 1.0000 365099.5844 1.0000 78931.6289 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
MIXED
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 41 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 40 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
K VALUE
COMPONENTS
n-Pentane
n-Hexane
MIXED
---
---
LIGHT
---
---
HEAVY
---
---
UNIT OPERATIONS
FEED TO
Air cooler: AC-102
PRODUCT FROM
Compressor: K-102
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Active): 440.0 psia *
Flow Specification (Inactive) Molar: 189.1 MMSCFD Mass: 3.651e+005 lb/hr Std Ideal Liq Volume:93e+004 barrel/day
User Variables
NOTES
Description
Material Stream: 61Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.0000
310.6
220.0
0.6356
5346
573.2
-6.755e+004
33.72
-4.714e+006
570.8 *
Liquid Phase
1.0000
310.6
220.0
0.6356
5346
573.2
-6.755e+004
33.72
-4.714e+006
570.8
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
Overall
76.61
0.3814
29.22
782.1
-881.8
0.4402
62.57
0.8167
1.490e+006
1.945e+004
---
2.122e-314
0.0000
0.0000
Liquid Phase
76.61
0.3814
29.22
782.1
-881.8
0.4402
62.57
0.8167
1.490e+006
1.945e+004
1.000
1.000
---
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 42 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 61 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
---
0.5205
62.57
0.6356
39.87
22.81
6.977e-002
12.96
---
1.033
1.033
7669
0.1775
40.04
570.8
1.000
2.622
100.1
0.0000
3.310
3.480e-002
8.306e-002
60.58
0.7908
60.58
0.7908
---
---
---
570.8
0.0000
13.97
14.03
Liquid Phase
---
0.5205
62.57
0.6356
39.87
22.81
6.977e-002
12.96
---
1.033
1.033
---
0.1775
40.04
570.8
1.000
2.622
---
1.0000
3.310
3.480e-002
8.306e-002
60.58
0.7908
60.58
0.7908
---
---
---
570.8
---
13.97
14.03
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0041
27.5055
20.0949
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.3941
0.2879
0.3179
MASS FLOW
(lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0118
0.2368
1984.5529
1449.8645
1911.6713
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3712
0.2712
0.3576
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0014
0.0278
217.9641
157.6493
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3803
0.2750
0.3446
Total 69.7875 1.0000 5346.3373 1.0000 573.1749 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 43 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 61 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 1.000
COMPONENTS
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0002
0.0041
27.5055
20.0949
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0001
0.3941
0.2879
0.3179
MASS FLOW
(lb/hr)
0.0000
0.0000
0.0118
0.2368
1984.5529
1449.8645
1911.6713
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.3712
0.2712
0.3576
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0014
0.0278
217.9641
157.6493
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0000
0.3803
0.2750
0.3446
Total 69.7875 1.0000 5346.3373 1.0000 573.1749 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
---
---
---
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Heat Exchanger: E-102
PRODUCT FROM
Distillation: Debutanizadora
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 220.0 psia
Flow Specification (Inactive) Molar: 0.6356 MMSCFD Mass: 5346 lb/hr Std Ideal Liq Volume:573.2 barrel/day
User Variables
NOTES
Description
Material Stream: 61bFluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Overall
0.0000
167.8
210.0
0.6356
5346
Liquid Phase
1.0000
167.8
210.0
0.6356
5346
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 44 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 61b (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
573.2
-7.506e+004
23.00
-5.238e+006
570.8 *
Liquid Phase
573.2
-7.506e+004
23.00
-5.238e+006
570.8
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
76.61
0.4734
36.27
630.2
-979.8
0.3002
46.12
0.6020
1.490e+006
1.945e+004
---
2.122e-314
0.0000
0.0000
---
0.5205
46.12
0.6356
39.87
18.38
6.588e-002
12.96
---
1.045
1.329
7842
0.2697
40.04
570.8
1.000
2.112
102.4
0.0000
10.48
5.276e-002
0.1567
44.13
0.5761
34.70
0.4529
---
---
---
570.8
0.0000
13.97
14.03
Liquid Phase
76.61
0.4734
36.27
630.2
-979.8
0.3002
46.12
0.6020
1.490e+006
1.945e+004
1.000
1.000
---
0.0000
---
0.5205
46.12
0.6356
39.87
18.38
6.588e-002
12.96
---
1.045
1.329
---
0.2697
40.04
570.8
1.000
2.112
---
1.0000
10.48
5.276e-002
0.1567
44.13
0.5761
34.70
0.4529
---
---
---
570.8
---
13.97
14.03
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 45 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 61b (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0041
27.5055
20.0949
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.3941
0.2879
0.3179
MASS FLOW
(lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0118
0.2368
1984.5529
1449.8645
1911.6713
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3712
0.2712
0.3576
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0014
0.0278
217.9641
157.6493
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3803
0.2750
0.3446
Total 69.7875 1.0000 5346.3373 1.0000 573.1749 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0041
27.5055
20.0949
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.3941
0.2879
0.3179
MASS FLOW
(lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0118
0.2368
1984.5529
1449.8645
1911.6713
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3712
0.2712
0.3576
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0014
0.0278
217.9641
157.6493
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3803
0.2750
0.3446
Total 69.7875 1.0000 5346.3373 1.0000 573.1749 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
---
---
---
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Air cooler: AC-100
PRODUCT FROM
Heat Exchanger: E-102
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 210.0 psia
Flow Specification (Inactive) Molar: 0.6356 MMSCFD Mass: 5346 lb/hr Std Ideal Liq Volume:573.2 barrel/day
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 46 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 61b (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
User Variables
NOTES
Description
Material Stream: 71Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.0000
111.4
250.0
6.862
3.805e+004
4834
-5.628e+004
23.66
-4.241e+007
4787 *
Liquid Phase
1.0000
111.4
250.0
6.862
3.805e+004
4834
-5.628e+004
23.66
-4.241e+007
4787
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
Overall
50.50
0.6253
31.58
5151
-1114
0.4686
33.51
0.6636
9.993e+005
1.979e+004
---
2.122e-314
0.0000
0.0000
---
0.6664
33.51
6.863
33.65
150.2
6.524e-002
14.16
---
1.063
1.527
6990
0.2120
33.98
4787
1.000
1.599
138.4
0.0000
Liquid Phase
50.50
0.6253
31.58
5151
-1114
0.4686
33.51
0.6636
9.993e+005
1.979e+004
1.000
1.000
---
0.0000
---
0.6664
33.51
6.863
33.65
150.2
6.524e-002
14.16
---
1.063
1.527
---
0.2120
33.98
4787
1.000
1.599
---
1.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 47 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 71 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
6.566
4.907e-002
0.1073
31.53
0.6243
21.95
0.4346
---
---
---
4787
0.0000
134.3
140.9
Liquid Phase
6.566
4.907e-002
0.1073
31.53
0.6243
21.95
0.4346
---
---
---
4787
---
134.3
140.9
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
9.7300
486.4942
79.3866
103.6937
31.8378
20.2037
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0129
0.6456
0.1054
0.1376
0.0423
0.0268
0.0294
MASS FLOW
(lb/hr)
0.0000
0.0009
0.0000
292.5811
21452.9336
4614.2693
6027.0907
2297.1263
1457.7164
1911.6714
MASS FRACTION
0.0000
0.0000
0.0000
0.0077
0.5638
0.1213
0.1584
0.0604
0.0383
0.0502
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0001
0.0000
56.3250
2899.1648
562.2263
707.6057
252.2941
158.5031
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0117
0.5998
0.1163
0.1464
0.0522
0.0328
0.0409
Total 753.5288 1.0000 38053.3897 1.0000 4833.6514 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
9.7300
486.4942
79.3866
103.6937
31.8378
20.2037
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0129
0.6456
0.1054
0.1376
0.0423
0.0268
0.0294
MASS FLOW
(lb/hr)
0.0000
0.0009
0.0000
292.5811
21452.9336
4614.2693
6027.0907
2297.1263
1457.7164
1911.6714
MASS FRACTION
0.0000
0.0000
0.0000
0.0077
0.5638
0.1213
0.1584
0.0604
0.0383
0.0502
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0001
0.0000
56.3250
2899.1648
562.2263
707.6057
252.2941
158.5031
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0117
0.5998
0.1163
0.1464
0.0522
0.0328
0.0409
Total 753.5288 1.0000 38053.3897 1.0000 4833.6514 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
MIXED
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 48 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 71 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
K VALUE
COMPONENTS
n-Pentane
n-Hexane
MIXED
0.0000
0.0000
LIGHT
0.0000
0.0000
HEAVY
---
---
UNIT OPERATIONS
FEED TO
Heat Exchanger: E-102
PRODUCT FROM
Pump: P-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 250.0 psia
Flow Specification (Inactive) Molar: 6.862 MMSCFD Mass: 3.805e+004 lb/hr Std Ideal Liq Volume: 4834 barrel/day
User Variables
NOTES
Description
Material Stream: 72Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.0000
131.5 *
245.0
6.862
3.805e+004
4834
-5.558e+004
24.86
-4.188e+007
4787 *
Liquid Phase
1.0000
131.5
245.0
6.862
3.805e+004
4834
-5.558e+004
24.86
-4.188e+007
4787
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
Overall
50.50
0.6021
30.40
5350
-1101
0.4923
35.62
0.7054
9.993e+005
1.979e+004
---
2.122e-314
0.0000
0.0000
Liquid Phase
50.50
0.6021
30.40
5350
-1101
0.4923
35.62
0.7054
9.993e+005
1.979e+004
1.000
1.000
---
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 49 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 72 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
---
0.6664
35.62
6.863
33.65
156.0
6.414e-002
14.16
---
1.059
1.551
7043
0.1985
33.98
4787
1.000
1.661
139.5
0.0000
5.388
4.583e-002
9.666e-002
33.64
0.6661
22.97
0.4548
---
---
---
4787
0.0000
134.3
140.9
Liquid Phase
---
0.6664
35.62
6.863
33.65
156.0
6.414e-002
14.16
---
1.059
1.551
---
0.1985
33.98
4787
1.000
1.661
---
1.0000
5.388
4.583e-002
9.666e-002
33.64
0.6661
22.97
0.4548
---
---
---
4787
---
134.3
140.9
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
9.7300
486.4942
79.3866
103.6937
31.8378
20.2037
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0129
0.6456
0.1054
0.1376
0.0423
0.0268
0.0294
MASS FLOW
(lb/hr)
0.0000
0.0009
0.0000
292.5811
21452.9336
4614.2693
6027.0907
2297.1263
1457.7164
1911.6714
MASS FRACTION
0.0000
0.0000
0.0000
0.0077
0.5638
0.1213
0.1584
0.0604
0.0383
0.0502
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0001
0.0000
56.3250
2899.1648
562.2263
707.6057
252.2941
158.5031
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0117
0.5998
0.1163
0.1464
0.0522
0.0328
0.0409
Total 753.5288 1.0000 38053.3897 1.0000 4833.6514 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
0.0000
0.0009
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 50 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 72 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 1.000
COMPONENTS
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
9.7300
486.4942
79.3866
103.6937
31.8378
20.2037
22.1828
MOLE FRACTION
0.0129
0.6456
0.1054
0.1376
0.0423
0.0268
0.0294
MASS FLOW
(lb/hr)
292.5811
21452.9336
4614.2693
6027.0907
2297.1263
1457.7164
1911.6714
MASS FRACTION
0.0077
0.5638
0.1213
0.1584
0.0604
0.0383
0.0502
LIQUID VOLUME
FLOW (barrel/day)
56.3250
2899.1648
562.2263
707.6057
252.2941
158.5031
197.5323
LIQUID VOLUME
FRACTION
0.0117
0.5998
0.1163
0.1464
0.0522
0.0328
0.0409
Total 753.5288 1.0000 38053.3897 1.0000 4833.6514 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Heater: E-103
PRODUCT FROM
Heat Exchanger: E-102
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 245.0 psia
Flow Specification (Inactive) Molar: 6.862 MMSCFD Mass: 3.805e+004 lb/hr Std Ideal Liq Volume: 4834 barrel/day
User Variables
NOTES
Description
Material Stream: 72bFluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Overall
0.5387
160.0 *
240.0
6.862
3.805e+004
Vapour Phase
0.5387
160.0
240.0
3.697
1.946e+004
Liquid Phase
0.4613
160.0
240.0
3.165
1.859e+004
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 51 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 72b (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
4834
-5.157e+004
31.44
-3.886e+007
4787 *
Vapour Phase
2534
-4.689e+004
35.94
-1.904e+007
2515
Liquid Phase
2299
-5.704e+004
26.19
-1.983e+007
2275
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
50.50
8.318e-002
4.200
3.872e+004
-1021
0.6227
31.88
0.6312
9.993e+005
1.979e+004
0.5243
0.5114
1.049e-005
0.0000
---
0.6664
31.88
6.863
33.65
77.47
---
14.16
---
1.066
1.114
7096
---
33.98
4787
0.4613
12.02
140.5
0.5387
4.654
---
---
29.89
0.5919
28.62
0.5667
---
---
---
4790
0.0000
134.3
140.9
Vapour Phase
47.94
4.811e-002
2.306
3.607e+004
-978.2
0.7498
25.58
0.5335
9.511e+005
1.984e+004
0.5243
0.5114
---
0.0000
140.6
0.6847
25.58
3.697
32.82
---
0.7502
14.38
---
1.084
1.280
---
0.2775
33.08
2515
0.0000
20.79
---
0.5387
---
1.386e-002
1.025e-002
23.59
0.4921
19.97
0.4167
19.88
0.4148
1.286
2515
---
154.2
160.2
Liquid Phase
53.50
0.5594
29.92
2656
-1066
0.4896
39.24
0.7335
1.056e+006
1.973e+004
0.4757
0.4886
---
0.0000
---
0.6461
39.24
3.166
34.57
77.47
6.452e-002
13.94
---
1.053
1.053
---
0.1928
34.93
2275
1.000
1.788
---
0.4613
4.654
4.226e-002
9.244e-002
37.25
0.6964
37.25
0.6964
---
---
---
2275
---
113.0
119.3
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 52 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 72b (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Overall Phase Vapour Fraction 0.5387
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
9.7300
486.4942
79.3866
103.6937
31.8378
20.2037
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0129
0.6456
0.1054
0.1376
0.0423
0.0268
0.0294
MASS FLOW
(lb/hr)
0.0000
0.0009
0.0000
292.5811
21452.9336
4614.2693
6027.0907
2297.1263
1457.7164
1911.6714
MASS FRACTION
0.0000
0.0000
0.0000
0.0077
0.5638
0.1213
0.1584
0.0604
0.0383
0.0502
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0001
0.0000
56.3250
2899.1648
562.2263
707.6057
252.2941
158.5031
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0117
0.5998
0.1163
0.1464
0.0522
0.0328
0.0409
Total 753.5288 1.0000 38053.3897 1.0000 4833.6514 1.0000
Vapour Phase Phase Fraction 0.5387
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
7.6246
300.0592
37.4308
43.5268
9.0857
5.1181
3.1129
MOLE FRACTION
0.0000
0.0000
0.0000
0.0188
0.7391
0.0922
0.1072
0.0224
0.0126
0.0077
MASS FLOW
(lb/hr)
0.0000
0.0008
0.0000
229.2713
13231.7091
2175.6289
2529.9545
655.5455
369.2795
268.2650
MASS FRACTION
0.0000
0.0000
0.0000
0.0118
0.6800
0.1118
0.1300
0.0337
0.0190
0.0138
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0001
0.0000
44.1372
1788.1427
265.0898
297.0273
71.9988
40.1532
27.7197
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0174
0.7056
0.1046
0.1172
0.0284
0.0158
0.0109
Total 405.9583 1.0000 19459.6545 1.0000 2534.2687 1.0000
Liquid Phase Phase Fraction 0.4613
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
2.1054
186.4350
41.9558
60.1668
22.7520
15.0855
19.0699
MOLE FRACTION
0.0000
0.0000
0.0000
0.0061
0.5364
0.1207
0.1731
0.0655
0.0434
0.0549
MASS FLOW
(lb/hr)
0.0000
0.0001
0.0000
63.3098
8221.2245
2438.6404
3497.1362
1641.5809
1088.4369
1643.4064
MASS FRACTION
0.0000
0.0000
0.0000
0.0034
0.4422
0.1312
0.1881
0.0883
0.0585
0.0884
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0000
12.1878
1111.0222
297.1365
410.5785
180.2953
118.3499
169.8126
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0053
0.4832
0.1292
0.1786
0.0784
0.0515
0.0739
Total 347.5706 1.0000 18593.7352 1.0000 2299.3828 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
5.790
9.126
3.101
1.378
0.7638
0.6194
0.3419
0.2905
0.1398
LIGHT
---
5.790
9.126
3.101
1.378
0.7638
0.6194
0.3419
0.2905
0.1398
HEAVY
---
---
---
---
---
---
---
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 53 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 72b (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
UNIT OPERATIONS
FEED TO
Distillation: Debutanizadora
PRODUCT FROM
Heater: E-103
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 240.0 psia
Flow Specification (Inactive) Molar: 6.862 MMSCFD Mass: 3.805e+004 lb/hr Std Ideal Liq Volume: 4834 barrel/day
User Variables
NOTES
Description
Material Stream: 91Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
109.5
905.0
200.0
4.110e+005
8.547e+004
-3.575e+004
36.44
-7.853e+008
---
Vapour Phase
1.0000
109.5
905.0
200.0
4.110e+005
8.547e+004
-3.575e+004
36.44
-7.853e+008
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
Overall
18.71
0.1704
3.189
5.510e+005
-1911
1.947
11.44
0.6111
3.766e+005
2.012e+004
---
4.941e-324
17.10
0.0000
2148
1.099
11.44
200.0
20.56
Vapour Phase
18.71
0.1704
3.189
5.510e+005
-1911
1.947
11.44
0.6111
3.766e+005
2.012e+004
1.000
1.000
---
0.0000
2148
1.099
11.44
200.0
20.56
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 54 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 91 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
---
0.8696
18.36
---
1.210
1.487
2275
0.2636
---
---
0.0000
5.869
121.5
1.0000
---
2.303e-002
1.346e-002
9.450
0.5050
7.692
0.4110
7.692
0.4110
1.487
0.0000
0.0000
---
---
Vapour Phase
---
0.8696
18.36
---
1.210
1.487
---
0.2636
---
---
0.0000
5.869
---
1.0000
---
2.303e-002
1.346e-002
9.450
0.5050
7.692
0.4110
7.692
0.4110
1.487
0.0000
---
---
---
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
107.8380
415.0990
19293.3260
1386.8600
502.9510
79.7250
103.8850
31.8460
20.2060
22.1830
MOLE FRACTION
0.0049
0.0189
0.8784
0.0631
0.0229
0.0036
0.0047
0.0014
0.0009
0.0010
MASS FLOW
(lb/hr)
3020.8659
18268.3828
309520.9013
41702.7422
22178.6303
4633.9359
6038.2118
2297.7208
1457.8831
1911.6844
MASS FRACTION
0.0073
0.0444
0.7530
0.1015
0.0540
0.0113
0.0147
0.0056
0.0035
0.0047
LIQUID VOLUME
FLOW (barrel/day)
256.5153
1515.6122
70788.8970
8028.2292
2997.2360
564.6226
708.9114
252.3594
158.5212
197.5337
LIQUID VOLUME
FRACTION
0.0030
0.0177
0.8282
0.0939
0.0351
0.0066
0.0083
0.0030
0.0019
0.0023
Total 21963.9190 1.0000 411030.9586 1.0000 85468.4379 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
MOLAR FLOW
(lbmole/hr)
107.8380
415.0990
19293.3260
1386.8600
502.9510
79.7250
103.8850
31.8460
MOLE FRACTION
0.0049
0.0189
0.8784
0.0631
0.0229
0.0036
0.0047
0.0014
MASS FLOW
(lb/hr)
3020.8659
18268.3828
309520.9013
41702.7422
22178.6303
4633.9359
6038.2118
2297.7208
MASS FRACTION
0.0073
0.0444
0.7530
0.1015
0.0540
0.0113
0.0147
0.0056
LIQUID VOLUME
FLOW (barrel/day)
256.5153
1515.6122
70788.8970
8028.2292
2997.2360
564.6226
708.9114
252.3594
LIQUID VOLUME
FRACTION
0.0030
0.0177
0.8282
0.0939
0.0351
0.0066
0.0083
0.0030
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 55 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 91 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
20.2060
22.1830
MOLE FRACTION
0.0009
0.0010
MASS FLOW
(lb/hr)
1457.8831
1911.6844
MASS FRACTION
0.0035
0.0047
LIQUID VOLUME
FLOW (barrel/day)
158.5212
197.5337
LIQUID VOLUME
FRACTION
0.0019
0.0023
Total 21963.9190 1.0000 411030.9586 1.0000 85468.4379 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Heat Exchanger: E-100
PRODUCT FROM
Tee: TEE-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 905.0 psia
Flow Specification (Inactive) Molar: 200.0 MMSCFD Mass: 4.110e+005 lb/hr Std Ideal Liq Volume:47e+004 barrel/day
User Variables
NOTES
Description
Material Stream: 92Fluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.9708
-29.00 *
895.0
200.0
4.110e+005
8.547e+004
-3.759e+004
32.71
-8.256e+008
---
Vapour Phase
0.9708
-29.00
895.0
194.2
3.906e+005
8.226e+004
-3.723e+004
32.93
-7.939e+008
---
Liquid Phase
0.0292
-29.00
895.0
5.844
2.045e+004
3209
-4.949e+004
25.37
-3.176e+007
5166
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 56 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 92 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
18.71
0.3068
5.742
3.060e+005
-2009
1.748
16.54
0.8838
3.766e+005
2.012e+004
0.9625
0.9503
16.77
0.0000
---
1.099
16.54
200.0
20.56
88.92
---
18.36
---
1.136
2.264
2319
---
---
---
2.922e-002
3.259
123.9
0.9708
7.167
---
---
14.55
0.7777
7.305
0.3904
---
---
---
5166
0.0000
---
---
Vapour Phase
18.32
0.3009
5.512
3.029e+005
-2033
1.798
16.40
0.8952
3.692e+005
2.015e+004
0.9625
0.9503
---
0.0000
1181
1.108
16.40
194.2
20.30
---
0.6436
18.51
---
1.138
2.361
---
0.1389
---
---
0.0000
3.324
---
0.9708
---
2.004e-002
1.226e-002
14.41
0.7868
6.945
0.3791
6.944
0.3791
2.361
0.0000
---
---
---
Liquid Phase
31.86
0.8998
28.67
3049
-1553
0.7964
21.23
0.6662
6.237e+005
1.957e+004
3.754e-002
4.975e-002
---
0.0000
---
0.8549
21.23
5.845
27.24
88.92
0.2152
15.69
---
1.103
1.103
---
0.2048
16.92
5166
1.000
1.111
---
0.0292
7.167
5.377e-002
9.405e-002
19.24
0.6039
19.24
0.6039
---
---
---
5166
---
---
1591
COMPOSITION
Overall Phase Vapour Fraction 0.9708
COMPONENTS
Nitrogen
CO2
Methane
Ethane
MOLAR FLOW
(lbmole/hr)
107.8380
415.0990
19293.3260
1386.8600
MOLE FRACTION
0.0049
0.0189
0.8784
0.0631
MASS FLOW
(lb/hr)
3020.8659
18268.3828
309520.9013
41702.7422
MASS FRACTION
0.0073
0.0444
0.7530
0.1015
LIQUID VOLUME
FLOW (barrel/day)
256.5153
1515.6122
70788.8970
8028.2292
LIQUID VOLUME
FRACTION
0.0030
0.0177
0.8282
0.0939
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 57 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 92 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.9708
COMPONENTS
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
502.9510
79.7250
103.8850
31.8460
20.2060
22.1830
MOLE FRACTION
0.0229
0.0036
0.0047
0.0014
0.0009
0.0010
MASS FLOW
(lb/hr)
22178.6303
4633.9359
6038.2118
2297.7208
1457.8831
1911.6844
MASS FRACTION
0.0540
0.0113
0.0147
0.0056
0.0035
0.0047
LIQUID VOLUME
FLOW (barrel/day)
2997.2360
564.6226
708.9114
252.3594
158.5212
197.5337
LIQUID VOLUME
FRACTION
0.0351
0.0066
0.0083
0.0030
0.0019
0.0023
Total 21963.9190 1.0000 411030.9586 1.0000 85468.4379 1.0000
Vapour Phase Phase Fraction 0.9708
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
107.1555
399.5579
18971.3068
1289.6265
411.7035
54.3696
63.3751
13.7097
7.3604
4.0030
MOLE FRACTION
0.0050
0.0187
0.8897
0.0605
0.0193
0.0025
0.0030
0.0006
0.0003
0.0002
MASS FLOW
(lb/hr)
3001.7482
17584.4258
304354.7802
38778.9391
18154.8880
3160.1815
3683.6140
989.1677
531.0567
344.9736
MASS FRACTION
0.0077
0.0450
0.7792
0.0993
0.0465
0.0081
0.0094
0.0025
0.0014
0.0009
LIQUID VOLUME
FLOW (barrel/day)
254.8919
1458.8686
69607.3806
7465.3655
2453.4646
385.0528
432.4717
108.6406
57.7438
35.6460
LIQUID VOLUME
FRACTION
0.0031
0.0177
0.8462
0.0908
0.0298
0.0047
0.0053
0.0013
0.0007
0.0004
Total 21322.1681 1.0000 390583.7747 1.0000 82259.5261 1.0000
Liquid Phase Phase Fraction 2.922e-002
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.6825
15.5411
322.0192
97.2335
91.2475
25.3554
40.5099
18.1363
12.8456
18.1800
MOLE FRACTION
0.0011
0.0242
0.5018
0.1515
0.1422
0.0395
0.0631
0.0283
0.0200
0.0283
MASS FLOW
(lb/hr)
19.1178
683.9570
5166.1211
2923.8031
4023.7423
1473.7545
2354.5978
1308.5531
926.8265
1566.7108
MASS FRACTION
0.0009
0.0334
0.2527
0.1430
0.1968
0.0721
0.1152
0.0640
0.0453
0.0766
LIQUID VOLUME
FLOW (barrel/day)
1.6234
56.7436
1181.5164
562.8637
543.7714
179.5698
276.4397
143.7188
100.7774
161.8877
LIQUID VOLUME
FRACTION
0.0005
0.0177
0.3682
0.1754
0.1695
0.0560
0.0861
0.0448
0.0314
0.0504
Total 641.7509 1.0000 20447.1840 1.0000 3208.9118 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
4.726
0.7738
1.773
0.3992
0.1358
6.454e-002
4.709e-002
2.275e-002
1.725e-002
6.627e-003
LIGHT
4.726
0.7738
1.773
0.3992
0.1358
6.454e-002
4.709e-002
2.275e-002
1.725e-002
6.627e-003
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Separator: V-100
PRODUCT FROM
Heat Exchanger: E-100
LOGICAL CONNECTION
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 58 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: 92 (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 895.0 psia
Flow Specification (Inactive) Molar: 200.0 MMSCFD Mass: 4.110e+005 lb/hr Std Ideal Liq Volume:47e+004 barrel/day
User Variables
NOTES
Description
Material Stream: Fuel UsersFluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
151.6
150.0
4.080 *
7878
1703
-3.440e+004
41.14
-1.541e+007
---
Vapour Phase
1.0000
151.6
150.0
4.080
7878
1703
-3.440e+004
41.14
-1.541e+007
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
Overall
17.58
2.325e-002
0.4088
8.237e+004
-1956
2.340
9.520
0.5414
3.545e+005
2.016e+004
---
4.941e-324
2.936
0.0000
321.2
1.124
9.520
4.080
19.77
---
0.9836
18.83
---
Vapour Phase
17.58
2.325e-002
0.4088
8.237e+004
-1956
2.340
9.520
0.5414
3.545e+005
2.016e+004
1.000
1.000
---
0.0000
321.2
1.124
9.520
4.080
19.77
---
0.9836
18.83
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 59 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: Fuel Users (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
(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)
(barrel/day)
(psia)
(psia)
(psia)
Overall
1.264
1.294
3643
1.954
---
---
0.0000
43.01
207.2
1.0000
---
2.253e-002
1.280e-002
7.534
0.4285
7.358
0.4184
7.146
0.4064
1.332
0.0000
0.0000
---
---
Vapour Phase
1.264
1.294
---
1.954
---
---
0.0000
43.01
---
1.0000
---
2.253e-002
1.280e-002
7.534
0.4285
7.358
0.4184
7.146
0.4064
1.332
0.0000
---
---
---
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
2.2777
8.7677
407.5112
29.0876
0.3476
0.0071
0.0040
0.0002
0.0000
0.0000
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
63.8063
385.8624
6537.6609
874.6601
15.3281
0.4154
0.2349
0.0126
0.0035
0.0003
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
5.4181
32.0126
1495.1940
168.3815
2.0714
0.0506
0.0276
0.0014
0.0004
0.0000
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 448.0031 1.0000 7877.9845 1.0000 1703.1577 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
2.2777
8.7677
407.5112
29.0876
0.3476
0.0071
0.0040
0.0002
0.0000
0.0000
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
63.8063
385.8624
6537.6609
874.6601
15.3281
0.4154
0.2349
0.0126
0.0035
0.0003
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
5.4181
32.0126
1495.1940
168.3815
2.0714
0.0506
0.0276
0.0014
0.0004
0.0000
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 448.0031 1.0000 7877.9845 1.0000 1703.1577 1.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 60 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: Fuel Users (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO PRODUCT FROM
Tee: TEE-102
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 150.0 psia
Flow Specification (Active) Molar: 4.080 MMSCFD * Mass: 7878 lb/hr Std Ideal Liq Volume: 1703 barrel/day
User Variables
NOTES
Description
Material Stream: Gas de ventaFluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
120.0 *
915.0 *
189.1
3.651e+005
7.893e+004
-3.510e+004
36.55
-7.288e+008
---
Vapour Phase
1.0000
120.0
915.0
189.1
3.651e+005
7.893e+004
-3.510e+004
36.55
-7.288e+008
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
Overall
17.58
0.1646
2.895
5.392e+005
-1996
2.078
Vapour Phase
17.58
0.1646
2.895
5.392e+005
-1996
2.078
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 61 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: Gas de venta (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
Higher Heating Value[Gas]
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
(psia)
(psia)
(psia)
(MMBtu/gal)
Overall
10.73
0.6103
3.545e+005
2.016e+004
---
4.941e-324
17.91
0.0000
2102
1.124
10.73
189.1
19.77
---
0.8936
18.83
---
1.227
1.468
---
0.2913
---
---
0.0000
6.075
---
1.0000
---
2.382e-002
1.351e-002
8.746
0.4974
7.310
0.4157
7.310
0.4157
1.468
0.0000
0.0000
---
---
1.390e-004
Vapour Phase
10.73
0.6103
3.545e+005
2.016e+004
1.000
1.000
---
0.0000
2102
1.124
10.73
189.1
19.77
---
0.8936
18.83
---
1.227
1.468
---
0.2913
---
---
0.0000
6.075
---
1.0000
---
2.382e-002
1.351e-002
8.746
0.4974
7.310
0.4157
7.310
0.4157
1.468
0.0000
---
---
---
1.390e-004
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
MOLAR FLOW
(lbmole/hr)
105.5603
406.3313
18885.8148
1348.0424
16.1092
0.3312
0.1873
0.0081
0.0023
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
2957.0596
17882.5195
302983.2404
40535.5010
710.3686
19.2512
10.8862
0.5819
0.1632
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
251.0972
1483.5996
69293.7030
7803.5226
95.9997
2.3457
1.2781
0.0639
0.0177
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 62 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: Gas de venta (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000
COMPONENTS
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0001
MOLE FRACTION
0.0000
MASS FLOW
(lb/hr)
0.0127
MASS FRACTION
0.0000
LIQUID VOLUME
FLOW (barrel/day)
0.0013
LIQUID VOLUME
FRACTION
0.0000
Total 20762.3870 1.0000 365099.5844 1.0000 78931.6289 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
105.5603
406.3313
18885.8148
1348.0424
16.1092
0.3312
0.1873
0.0081
0.0023
0.0001
MOLE FRACTION
0.0051
0.0196
0.9096
0.0649
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW
(lb/hr)
2957.0596
17882.5195
302983.2404
40535.5010
710.3686
19.2512
10.8862
0.5819
0.1632
0.0127
MASS FRACTION
0.0081
0.0490
0.8299
0.1110
0.0019
0.0001
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (barrel/day)
251.0972
1483.5996
69293.7030
7803.5226
95.9997
2.3457
1.2781
0.0639
0.0177
0.0013
LIQUID VOLUME
FRACTION
0.0032
0.0188
0.8779
0.0989
0.0012
0.0000
0.0000
0.0000
0.0000
0.0000
Total 20762.3870 1.0000 365099.5844 1.0000 78931.6289 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO PRODUCT FROM
Air cooler: AC-102
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Active): 915.0 psia *
Flow Specification (Inactive) Molar: 189.1 MMSCFD Mass: 3.651e+005 lb/hr Std Ideal Liq Volume:93e+004 barrel/day
User Variables
NOTES
Description
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 63 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: GasolinaFluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.0000
120.0 *
205.0
0.6356
5346
573.2
-7.719e+004
19.48
-5.387e+006
570.8 *
Liquid Phase
1.0000
120.0
205.0
0.6356
5346
573.2
-7.719e+004
19.48
-5.387e+006
570.8
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(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)
(barrel/day)
Overall
76.61
0.4968
38.06
600.5
-1008
0.2542
42.97
0.5609
1.490e+006
1.945e+004
---
2.122e-314
0.0000
0.0000
---
0.5205
42.97
0.6356
39.87
17.51
6.634e-002
12.96
---
1.048
1.331
7929
0.3205
40.04
570.8
1.000
2.013
103.5
0.0000
13.16
5.745e-002
0.1954
40.98
0.5350
32.29
0.4215
---
---
---
570.8
Liquid Phase
76.61
0.4968
38.06
600.5
-1008
0.2542
42.97
0.5609
1.490e+006
1.945e+004
1.000
1.000
---
0.0000
---
0.5205
42.97
0.6356
39.87
17.51
6.634e-002
12.96
---
1.048
1.331
---
0.3205
40.04
570.8
1.000
2.013
---
1.0000
13.16
5.745e-002
0.1954
40.98
0.5350
32.29
0.4215
---
---
---
570.8
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 64 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: Gasolina (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
Higher Heating Value[Gas]
(psia)
(psia)
(psia)
(MMBtu/gal)
Overall
0.0000
13.97
14.03
6.082e-004
Liquid Phase
---
13.97
14.03
6.082e-004
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0041
27.5055
20.0949
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.3941
0.2879
0.3179
MASS FLOW
(lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0118
0.2368
1984.5529
1449.8645
1911.6713
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3712
0.2712
0.3576
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0014
0.0278
217.9641
157.6493
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3803
0.2750
0.3446
Total 69.7875 1.0000 5346.3373 1.0000 573.1749 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0041
27.5055
20.0949
22.1828
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.3941
0.2879
0.3179
MASS FLOW
(lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0118
0.2368
1984.5529
1449.8645
1911.6713
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3712
0.2712
0.3576
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0014
0.0278
217.9641
157.6493
197.5323
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3803
0.2750
0.3446
Total 69.7875 1.0000 5346.3373 1.0000 573.1749 1.0000
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
---
---
---
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO PRODUCT FROM
Air cooler: AC-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 65 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: Gasolina (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 205.0 psia
Flow Specification (Inactive) Molar: 0.6356 MMSCFD Mass: 5346 lb/hr Std Ideal Liq Volume:573.2 barrel/day
User Variables
NOTES
Description
Material Stream: GLPFluid Package: Basis-1
Property Package: Peng Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (F)
Pressure: (psia)
Molar Flow (MMSCFD)
Mass Flow (lb/hr)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
143.1
215.0
6.227
3.271e+004
4260
-4.718e+004
35.26
-3.226e+007
4235 *
Vapour Phase
1.0000
143.1
215.0
6.227
3.271e+004
4260
-4.718e+004
35.26
-3.226e+007
4235
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
(lbmole/ft3)
(lb/ft3)
(barrel/day)
(Btu/lb)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(psia)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(Btu/lbmole)
Overall
47.84
4.376e-002
2.093
6.679e+004
-986.2
0.7371
24.75
0.5174
9.492e+005
1.984e+004
---
4.941e-324
6.407e-006
0.0000
260.4
0.6860
24.75
6.227
32.82
---
0.7595
14.37
---
1.087
1.272
6395
Vapour Phase
47.84
4.376e-002
2.093
6.679e+004
-986.2
0.7371
24.75
0.5174
9.492e+005
1.984e+004
1.000
1.000
---
0.0000
260.4
0.6860
24.75
6.227
32.82
---
0.7595
14.37
---
1.087
1.272
---
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 66 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: GLP (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
PROPERTIES
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Liq. Vol. Flow - Sum(Std. Cond)
Partial Pressure of H2S
Reid VP at 37.8 C
True VP at 37.8 C
Higher Heating Value[Gas]
(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)
(barrel/day)
(psia)
(psia)
(psia)
(MMBtu/gal)
Overall
0.2941
33.01
4235
0.0000
22.85
133.7
1.0000
---
1.315e-002
9.862e-003
22.77
0.4759
19.45
0.4067
---
---
---
4235
0.0000
150.8
156.0
3.716e-004
Vapour Phase
0.2941
33.01
4235
0.0000
22.85
---
1.0000
---
1.315e-002
9.862e-003
22.77
0.4759
19.45
0.4067
17.48
0.3654
1.416
4235
---
150.8
156.0
3.716e-004
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
9.7300
486.4942
79.3864
103.6896
4.3322
0.1088
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0142
0.7115
0.1161
0.1517
0.0063
0.0002
0.0000
MASS FLOW
(lb/hr)
0.0000
0.0009
0.0000
292.5811
21452.9336
4614.2575
6026.8539
312.5734
7.8520
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0089
0.6559
0.1411
0.1843
0.0096
0.0002
0.0000
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0001
0.0000
56.3250
2899.1648
562.2249
707.5779
34.3300
0.8538
0.0000
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0132
0.6805
0.1320
0.1661
0.0081
0.0002
0.0000
Total 683.7413 1.0000 32707.0524 1.0000 4260.4765 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MOLAR FLOW
(lbmole/hr)
0.0000
0.0000
0.0000
9.7300
486.4942
79.3864
103.6896
4.3322
0.1088
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0142
0.7115
0.1161
0.1517
0.0063
0.0002
0.0000
MASS FLOW
(lb/hr)
0.0000
0.0009
0.0000
292.5811
21452.9336
4614.2575
6026.8539
312.5734
7.8520
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0089
0.6559
0.1411
0.1843
0.0096
0.0002
0.0000
LIQUID VOLUME
FLOW (barrel/day)
0.0000
0.0001
0.0000
56.3250
2899.1648
562.2249
707.5779
34.3300
0.8538
0.0000
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0132
0.6805
0.1320
0.1661
0.0081
0.0002
0.0000
Total 683.7413 1.0000 32707.0524 1.0000 4260.4765 1.0000
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 67 of 68* Specified by user.Licensed to: LEGENDS
PROYECTO RIO GRANDE
Santa Cruz Bolivia
Case Name: PROYECTO FINAL.HSC
Unit Set: NewUser
Date/Time: Tue Jul 17 11:57:47 2012
Material Stream: GLP (continued)Fluid Package: Basis-1
Property Package: Peng Robinson
K VALUE
COMPONENTS
Nitrogen
CO2
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
n-Hexane
MIXED
---
---
---
---
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO PRODUCT FROM
Distillation: Debutanizadora
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 215.0 psia
Flow Specification (Inactive) Molar: 6.227 MMSCFD Mass: 3.271e+004 lb/hr Std Ideal Liq Volume: 4260 barrel/day
User Variables
NOTES
Description
Hyprotech Ltd. Aspen HYSYS Version 2006.5 (21.0.0.6924) Page 68 of 68* Specified by user.Licensed to: LEGENDS
