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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 1Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall0.000023.00 *
14.50 *
2205 *
7.046e+0046431
-1.060e+005-83.37
-2.338e+0086456 *
Liquid Phase1.000023.0014.502205
7.046e+0046431
-1.060e+005-83.37
-2.338e+0086456
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)
(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)
(psia)
(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)
Overall31.961.50147.976278
-3318-2.60922.55
0.70562.816e+005
8810
2.122e-3140.00000.0000
1.46522.5520.0446.83183.1
1.865e-00311.26
0.00001.0971.235
1.646e+0040.515146.6564561.000
0.6662515.1
0.000044.50
0.16640.395820.56
0.643518.26
0.57153601112.7
6.262e-003
Liquid Phase31.961.50147.976278
-3318-2.60922.55
0.70562.816e+005
88101.0001.000
0.0000
1.46522.5520.0446.83183.1
1.865e-00311.26
1.0971.235
0.515146.6564561.000
0.6662
1.000044.50
0.16640.395820.56
0.643518.26
0.57153601112.7
6.262e-003
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 1 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 1 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(psia)(psia)
(barrel/day)
Overall78.4349.226456
-2.312
Liquid Phase78.4349.226456
-2.312
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
429.9034 *
6.5239 *
874.3342 *
893.8386 *
MOLE FRACTION
0.1950 *
0.0030 *
0.3966 *
0.4054 *
MASS FLOW (lb/hr)
13774.9217 *
300.5544 *
40279.7014 *
16102.5914 *
MASS FRACTION
0.1955 *
0.0043 *
0.5717 *
0.2285 *
LIQUID VOLUMEFLOW (barrel/day)
1185.3515 *
25.8547 *
4114.6604 *
1104.8151 *
LIQUID VOLUMEFRACTION
0.1843 *
0.0040 *
0.6398 *
0.1718 *
Total 2204.6000 1.0000 70457.7689 1.0000 6430.6817 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
429.90346.5239
874.3342893.8386
MOLE FRACTION
0.19500.00300.39660.4054
MASS FLOW (lb/hr)
13774.9217300.5544
40279.701416102.5914
MASS FRACTION
0.19550.00430.57170.2285
LIQUID VOLUMEFLOW (barrel/day)
1185.351525.8547
4114.66041104.8151
LIQUID VOLUMEFRACTION
0.18430.00400.63980.1718
Total 2204.6000 1.0000 70457.7689 1.0000 6430.6817 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED0.00000.00000.00000.0000
LIGHT0.00000.00000.00000.0000
HEAVY
UNIT OPERATIONS
FEED TOPump: P-100
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Active): 14.50 psia *
Flow Specification (Active) Molar: 2205 lbmole/hr * Mass: 7.046e+004 lb/hr Std Ideal Liq Volume:6431 barrel/day
User Variables
NOTES
Description
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 2 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 2Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall0.000023.87152.32205
7.046e+0046431
-1.060e+005-80.54
-2.337e+0086456 *
Liquid Phase1.000023.87152.32205
7.046e+0046431
-1.060e+005-80.54
-2.337e+0086456
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)
(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)
(psia)
(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)
Overall31.961.50247.996275
-3317-2.52022.56
0.70592.816e+005
8810
2.122e-3140.00000.0000
1.46522.5620.0446.83183.0
1.954e-00211.26
0.00001.0971.233
1.426e+0040.511746.6564561.000
0.6659446.3
0.000044.43
0.16640.393420.58
0.643818.30
0.5727384.712.04
5.864e-002
Liquid Phase31.961.50247.996275
-3317-2.52022.56
0.70592.816e+005
88101.0001.000
0.0000
1.46522.5620.0446.83183.0
1.954e-00211.26
1.0971.233
0.511746.6564561.000
0.6659
1.000044.43
0.16640.393420.58
0.643818.30
0.5727384.712.04
5.864e-002
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 3 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 2 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(psia)(psia)
(barrel/day)
Overall78.4349.226456
-2.328
Liquid Phase78.4349.226456
-2.328
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
429.90346.5239
874.3342893.8386
MOLE FRACTION
0.19500.00300.39660.4054
MASS FLOW (lb/hr)
13774.9217300.5544
40279.701416102.5914
MASS FRACTION
0.19550.00430.57170.2285
LIQUID VOLUMEFLOW (barrel/day)
1185.351525.8547
4114.66041104.8151
LIQUID VOLUMEFRACTION
0.18430.00400.63980.1718
Total 2204.6000 1.0000 70457.7689 1.0000 6430.6817 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
429.90346.5239
874.3342893.8386
MOLE FRACTION
0.19500.00300.39660.4054
MASS FLOW (lb/hr)
13774.9217300.5544
40279.701416102.5914
MASS FRACTION
0.19550.00430.57170.2285
LIQUID VOLUMEFLOW (barrel/day)
1185.351525.8547
4114.66041104.8151
LIQUID VOLUMEFRACTION
0.18430.00400.63980.1718
Total 2204.6000 1.0000 70457.7689 1.0000 6430.6817 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED0.00000.00000.00000.0000
LIGHT0.00000.00000.00000.0000
HEAVY
UNIT OPERATIONS
FEED TOMixer: MIX-100
PRODUCT FROMPump: P-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 152.3 psiaFlow Specification (Inactive) Molar: 2205 lbmole/hr Mass: 7.046e+004 lb/hr Std Ideal Liq Volume:6431 barrel/day
User Variables
NOTES
Description
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 4 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 3Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall0.000025.98152.32260
7.228e+0046587
-1.059e+005-78.13
-2.395e+0086612 *
Liquid Phase1.000025.98152.32260
7.228e+0046587
-1.059e+005-78.13
-2.395e+0086612
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)
(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)
(psia)
(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)
Overall31.981.50147.996438
-3313-2.44322.71
0.71012.817e+005
8808
2.122e-3140.00000.0000
1.46722.7120.5546.90187.8
1.947e-00211.25
0.00001.0961.233
1.424e+0040.514246.7366121.000
0.6663445.2
0.000043.98
0.16480.395320.72
0.648018.42
0.5760393.912.32
5.765e-002
Liquid Phase31.981.50147.996438
-3313-2.44322.71
0.71012.817e+005
88081.0001.000
0.0000
1.46722.7120.5546.90187.8
1.947e-00211.25
1.0961.233
0.514246.7366121.000
0.6663
1.000043.98
0.16480.395320.72
0.648018.42
0.5760393.912.32
5.765e-002
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 5 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 3 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(psia)(psia)
(barrel/day)
Overall75.0747.836612
-2.314
Liquid Phase75.0747.836612
-2.314
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
482.97149.0619
874.3540894.0539
MOLE FRACTION
0.21370.00400.38680.3955
MASS FLOW (lb/hr)
15475.3228417.4806
40280.614016106.4702
MASS FRACTION
0.21410.00580.55730.2228
LIQUID VOLUMEFLOW (barrel/day)
1331.673435.9131
4114.75371105.0812
LIQUID VOLUMEFRACTION
0.20220.00550.62460.1678
Total 2260.4412 1.0000 72279.8876 1.0000 6587.4213 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
482.97149.0619
874.3540894.0539
MOLE FRACTION
0.21370.00400.38680.3955
MASS FLOW (lb/hr)
15475.3228417.4806
40280.614016106.4702
MASS FRACTION
0.21410.00580.55730.2228
LIQUID VOLUMEFLOW (barrel/day)
1331.673435.9131
4114.75371105.0812
LIQUID VOLUMEFRACTION
0.20220.00550.62460.1678
Total 2260.4412 1.0000 72279.8876 1.0000 6587.4213 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED0.00000.00000.00000.0000
LIGHT0.00000.00000.00000.0000
HEAVY
UNIT OPERATIONS
FEED TOHeater: E-100
PRODUCT FROMMixer: MIX-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 152.3 psiaFlow Specification (Inactive) Molar: 2260 lbmole/hr Mass: 7.228e+004 lb/hr Std Ideal Liq Volume:6587 barrel/day
User Variables
NOTES
Description
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 6 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 4Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall0.0406192.2 *
152.32260
7.228e+0046587
-1.016e+00526.93
-2.296e+0086612 *
Vapour Phase0.0406192.2152.391.784070411.2
-7.858e+00445.00
-7.212e+006441.1
Liquid Phase0.9594192.2152.32169
6.821e+0046176
-1.025e+00526.17
-2.224e+0086185
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)
(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)
(psia)
(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)
Overall31.98
0.386112.35
2.502e+004-3176
0.842226.74
0.83622.817e+005
88086.243e-0025.631e-002
0.00000.0000
1.46726.7420.5546.90204.3
11.25
0.00001.0801.005
1.424e+004
46.736612
0.95942.590445.2
0.040630.60
24.750.774126.60
0.8320
Vapour Phase44.34
2.177e-0020.9654
1.802e+004-17721.01517.24
0.38895.354e+0051.207e+0046.243e-0025.631e-002
0.000070.26
0.954017.24
0.834342.30
1.00011.37
1.1301.130
0.697939.44441.1
0.000045.94
0.0406
1.297e-0021.079e-002
15.260.344115.26
0.3441
Liquid Phase31.451.32441.637004
-32600.831927.14
0.86292.709e+005
86140.93760.9437
0.0000
1.50127.1419.7147.21204.3
1.645e-00211.24
1.0791.079
0.207647.1561851.000
0.7555
0.959430.60
0.15260.138425.15
0.799725.15
0.7997
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 7 of 76
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 4 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(psia)(psia)
(barrel/day)
Overall75.0747.836626
Vapour Phase113.5110.1441.1
Liquid Phase72.4545.306185
COMPOSITION
Overall Phase Vapour Fraction 0.0406
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
482.97149.0619
874.3540894.0539
MOLE FRACTION
0.21370.00400.38680.3955
MASS FLOW (lb/hr)
15475.3228417.4806
40280.614016106.4702
MASS FRACTION
0.21410.00580.55730.2228
LIQUID VOLUMEFLOW (barrel/day)
1331.673435.9131
4114.75371105.0812
LIQUID VOLUMEFRACTION
0.20220.00550.62460.1678
Total 2260.4412 1.0000 72279.8876 1.0000 6587.4213 1.0000
Vapour Phase Phase Fraction 4.060e-002
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
4.82050.0667
83.65743.2319
MOLE FRACTION
0.05250.00070.91150.0352
MASS FLOW (lb/hr)
154.45953.0743
3854.014558.2234
MASS FRACTION
0.03800.00080.94700.0143
LIQUID VOLUMEFLOW (barrel/day)
13.29150.2645
393.69613.9948
LIQUID VOLUMEFRACTION
0.03230.00060.95730.0097
Total 91.7766 1.0000 4069.7718 1.0000 411.2468 1.0000
Liquid Phase Phase Fraction 0.9594
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
478.15098.9952
790.6965890.8219
MOLE FRACTION
0.22050.00410.36460.4108
MASS FLOW (lb/hr)
15320.8632414.4063
36426.599516048.2468
MASS FRACTION
0.22460.00610.53400.2353
LIQUID VOLUMEFLOW (barrel/day)
1318.382035.6486
3721.05761101.0864
LIQUID VOLUMEFRACTION
0.21350.00580.60250.1783
Total 2168.6645 1.0000 68210.1158 1.0000 6176.1746 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED0.23820.17532.500
8.573e-002
LIGHT0.23820.17532.500
8.573e-002
HEAVY
UNIT OPERATIONS
FEED TOEquilibrium Reactor: ERV-100
PRODUCT FROMHeater: E-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 152.3 psiaFlow Specification (Inactive) Molar: 2260 lbmole/hr Mass: 7.228e+004 lb/hr Std Ideal Liq Volume:6587 barrel/day
User Variables
NOTESHyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 8 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 4 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
NOTES
Description
Material Stream: 5Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall1.0000248.0 *
152.31218
4.963e+0044915
-8.105e+00444.88
-9.870e+0075177 *
Vapour Phase1.0000248.0152.31218
4.963e+0044915
-8.105e+00444.88
-9.870e+0075177
Aqueous Phase0.0000248.0152.3
0.00000.00000.0000
-1.144e+00513.25
0.00000.0000
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal 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)
(psia)
(Btu/lbmole)(cSt)
(lb/ft3)(barrel/day)
(ft3/lbmole)(Btu/lb)
(dyne/cm)(Btu/hr-ft-F)
Overall40.75
2.005e-0020.8173
2.596e+005-19891.10117.07
0.41904.623e+0051.134e+004
4.941e-3240.00000.0000
10121.05917.0711.0743.16
0.0000
11.37
0.00001.1321.132
1.161e+0040.887140.985177
0.000049.87284.9
1.0000
1.477e-002
Vapour Phase40.75
2.005e-0020.8173
2.596e+005-19891.10117.07
0.41904.623e+0051.134e+004
1.0001.000
0.000010121.05917.0711.0743.16
1.00011.37
1.1321.132
0.887140.985177
0.000049.87
1.0000
1.477e-002
Aqueous Phase21.722.33550.73
0.0000-5265
0.610023.711.091
7.476e+0043442
0.0000
0.0000
2.54323.71
0.000055.24
0.00008.588e-003
11.25
1.0911.180
0.196656.82
0.00001.000
0.4282
0.000046.98
0.3081
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 9 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 5 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
ViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(cP)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)
(psia)(psia)
(barrel/day)
Overall1.161e-002
15.090.370215.09
0.3702
113.194.985177
Vapour Phase1.161e-002
15.090.370215.09
0.3702
113.194.985177
Aqueous Phase0.159821.72
0.999920.09
0.9248
77.1422.60
0.0000
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
54.06624.9657
955.0940203.6813
MOLE FRACTION
0.04440.00410.78430.1673
MASS FLOW (lb/hr)
1732.3851228.7692
44000.22353669.3391
MASS FRACTION
0.03490.00460.88660.0739
LIQUID VOLUMEFLOW (barrel/day)
149.074219.6795
4494.7200251.7571
LIQUID VOLUMEFRACTION
0.03030.00400.91440.0512
Total 1217.8072 1.0000 49630.7168 1.0000 4915.2307 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
54.06624.9657
955.0940203.6813
MOLE FRACTION
0.04440.00410.78430.1673
MASS FLOW (lb/hr)
1732.3851228.7692
44000.22353669.3391
MASS FRACTION
0.03490.00460.88660.0739
LIQUID VOLUMEFLOW (barrel/day)
149.074219.6795
4494.7200251.7571
LIQUID VOLUMEFRACTION
0.03030.00400.91440.0512
Total 1217.8072 1.0000 49630.7168 1.0000 4915.2307 1.0000
Aqueous Phase Phase Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
0.00000.00000.00000.0000
MOLE FRACTION
0.05040.00390.10310.8426
MASS FLOW (lb/hr)
0.00000.00000.00000.0000
MASS FRACTION
0.07430.00830.21860.6988
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.08260.00930.28850.6196
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED0.88121.0387.610
0.1985
LIGHT HEAVY0.88121.0387.610
0.1985
UNIT OPERATIONS
FEED TOValve: VLV-100
PRODUCT FROMEquilibrium Reactor: ERV-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 10 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 5 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 152.3 psiaFlow Specification (Inactive) Molar: 1218 lbmole/hr Mass: 4.963e+004 lb/hr Std Ideal Liq Volume:4915 barrel/day
User Variables
NOTES
Description
Material Stream: 6Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall1.0000247.9145.0 *
12184.963e+004
4915-8.105e+004
44.98-9.870e+007
5177 *
Vapour Phase1.0000247.9145.01218
4.963e+0044915
-8.105e+00444.98
-9.870e+0075177
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/Cv
(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)
(psia)
Overall40.75
1.910e-0020.7784
2.725e+005-19891.10417.06
0.41864.623e+0051.134e+004
4.941e-3240.00000.0000
10631.05917.0611.0743.16
1.00011.37
0.00001.1321.132
Vapour Phase40.75
1.910e-0020.7784
2.725e+005-19891.10417.06
0.41864.623e+0051.134e+004
1.0001.000
0.000010631.05917.0611.0743.16
1.00011.37
1.1321.132
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 11 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 6 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Heat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)(psia)
(barrel/day)
Overall1.166e+004
0.929740.985177
0.000052.35286.2
1.0000
1.474e-0021.159e-002
15.070.369815.07
0.3698
113.194.985177
Vapour Phase
0.929740.985177
0.000052.35
1.0000
1.474e-0021.159e-002
15.070.369815.07
0.3698
113.194.985177
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
54.06624.9657
955.0940203.6813
MOLE FRACTION
0.04440.00410.78430.1673
MASS FLOW (lb/hr)
1732.3851228.7692
44000.22353669.3391
MASS FRACTION
0.03490.00460.88660.0739
LIQUID VOLUMEFLOW (barrel/day)
149.074219.6795
4494.7200251.7571
LIQUID VOLUMEFRACTION
0.03030.00400.91440.0512
Total 1217.8072 1.0000 49630.7168 1.0000 4915.2307 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
54.06624.9657
955.0940203.6813
MOLE FRACTION
0.04440.00410.78430.1673
MASS FLOW (lb/hr)
1732.3851228.7692
44000.22353669.3391
MASS FRACTION
0.03490.00460.88660.0739
LIQUID VOLUMEFLOW (barrel/day)
149.074219.6795
4494.7200251.7571
LIQUID VOLUMEFRACTION
0.03030.00400.91440.0512
Total 1217.8072 1.0000 49630.7168 1.0000 4915.2307 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED LIGHT HEAVY
UNIT OPERATIONS
FEED TOCooler: E-101
PRODUCT FROMValve: VLV-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 12 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 6 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROCESS UTILITY
DYNAMICS
Pressure Specification (Active): 145.0 psia *
Flow Specification (Inactive) Molar: 1218 lbmole/hr Mass: 4.963e+004 lb/hr Std Ideal Liq Volume:4915 barrel/day
User Variables
NOTES
Description
Material Stream: 7Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall0.7672192.2 *
145.0 *
12184.963e+004
4915-8.516e+004
39.62-1.037e+008
5177 *
Vapour Phase0.7672192.2145.0934.3
4.146e+0044194
-7.871e+00445.01
-7.354e+0074505
Aqueous Phase0.2328192.2145.0283.58171721.0
-1.064e+00521.87
-3.018e+007713.6
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/Cv
(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)
(psia)
Overall40.75
2.691e-0021.097
1.934e+005-2090
0.972219.13
0.46944.623e+0051.134e+004
0.85330.83540.00000.0000
1.05919.1311.0743.1623.28
11.37
0.00001.1161.087
Vapour Phase44.37
2.073e-0020.9200
1.926e+005-17741.01417.30
0.38985.362e+0051.208e+004
0.85330.8354
0.0000751.1
0.952217.308.49342.25
1.00011.38
1.1301.130
Aqueous Phase28.821.51843.75798.3-3693
0.759025.17
0.87322.185e+005
75790.14670.1646
0.0000
1.68125.172.57748.4423.28
1.366e-00211.30
1.0861.236
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 13 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 7 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Heat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)(psia)
(barrel/day)
Overall1.166e+004
40.985177
0.232837.16286.2
0.767237.52
17.140.420717.60
0.4318
113.194.985218
Vapour Phase
0.737339.344505
0.000048.23
0.7672
1.299e-0021.087e-002
15.310.345115.31
0.3451
116.7111.54505
Aqueous Phase
0.212148.95713.61.000
0.6588
0.232837.52
0.19640.148623.18
0.804320.36
0.7063
88.1343.43713.6
COMPOSITION
Overall Phase Vapour Fraction 0.7672
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
54.06624.9657
955.0940203.6813
MOLE FRACTION
0.04440.00410.78430.1673
MASS FLOW (lb/hr)
1732.3851228.7692
44000.22353669.3391
MASS FRACTION
0.03490.00460.88660.0739
LIQUID VOLUMEFLOW (barrel/day)
149.074219.6795
4494.7200251.7571
LIQUID VOLUMEFRACTION
0.03030.00400.91440.0512
Total 1217.8072 1.0000 49630.7168 1.0000 4915.2307 1.0000
Vapour Phase Phase Fraction 0.7672
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
25.17922.0829
863.214743.8352
MOLE FRACTION
0.02690.00220.92390.0469
MASS FLOW (lb/hr)
806.790895.9600
39767.4388789.6953
MASS FRACTION
0.01950.00230.95920.0190
LIQUID VOLUMEFLOW (barrel/day)
69.42558.2548
4062.331754.1818
LIQUID VOLUMEFRACTION
0.01660.00200.96860.0129
Total 934.3121 1.0000 41459.8850 1.0000 4194.1938 1.0000
Aqueous Phase Phase Fraction 0.2328
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
28.88702.8828
91.8792159.8461
MOLE FRACTION
0.10190.01020.32410.5638
MASS FLOW (lb/hr)
925.5943132.8092
4232.78472879.6437
MASS FRACTION
0.11330.01630.51800.3524
LIQUID VOLUMEFLOW (barrel/day)
79.648711.4247
432.3883197.5753
LIQUID VOLUMEFRACTION
0.11050.01580.59970.2740
Total 283.4951 1.0000 8170.8318 1.0000 721.0369 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
MIXED0.26450.21922.851
LIGHT HEAVY0.26450.21922.851
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 14 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 7 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
K VALUE
COMPONENTSH2O
MIXED8.321e-002
LIGHT HEAVY8.321e-002
UNIT OPERATIONS
FEED TODistillation: T-100
PRODUCT FROMCooler: E-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Active): 145.0 psia *
Flow Specification (Inactive) Molar: 1218 lbmole/hr Mass: 4.963e+004 lb/hr Std Ideal Liq Volume:4915 barrel/day
User Variables
NOTES
Description
Material Stream: 8Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall0.0000110.0139.0956.0
4.403e+0044497
-8.662e+00437.85
-8.281e+0074878 *
Liquid Phase1.0000110.0139.0956.0
4.403e+0044497
-8.662e+00437.85
-8.281e+0074878
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas 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)(ACFM)
Overall46.06
0.779935.925240
-18810.821928.21
0.61265.708e+0051.239e+004
2.122e-3140.00000.0000
Liquid Phase46.06
0.779935.925240
-18810.821928.21
0.61265.708e+0051.239e+004
1.0001.000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 15 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 8 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Avg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(lb/ft3)
(USGPM)
(psia)
(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)
(psia)(psia)
(barrel/day)
Overall0.908728.218.69041.85152.8
2.915e-00211.38
0.00001.0761.0767981
0.131238.5848781.0001.282173.3
0.00009.257
7.011e-0027.548e-002
26.230.569526.23
0.5695
120.4120.74878
Liquid Phase0.908728.218.69041.85152.8
2.915e-00211.38
1.0761.076
0.131238.5848781.0001.282
1.00009.257
7.011e-0027.548e-002
26.230.569526.23
0.5695
120.4120.74878
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
0.93850.0100
955.07410.0075
MOLE FRACTION
0.00100.00000.99900.0000
MASS FLOW (lb/hr)
30.07220.4627
43999.31070.1346
MASS FRACTION
0.00070.00000.99930.0000
LIQUID VOLUMEFLOW (barrel/day)
2.58780.0398
4494.62670.0092
LIQUID VOLUMEFRACTION
0.00060.00000.99940.0000
Total 956.0302 1.0000 44029.9802 1.0000 4497.2635 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
0.93850.0100
955.07410.0075
MOLE FRACTION
0.00100.00000.99900.0000
MASS FLOW (lb/hr)
30.07220.4627
43999.31070.1346
MASS FRACTION
0.00070.00000.99930.0000
LIQUID VOLUMEFLOW (barrel/day)
2.58780.0398
4494.62670.0092
LIQUID VOLUMEFRACTION
0.00060.00000.99940.0000
Total 956.0302 1.0000 44029.9802 1.0000 4497.2635 1.0000
K VALUE
COMPONENTSMethanol
MIXED0.0000
LIGHT0.0000
HEAVY
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 16 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 8 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
K VALUE
COMPONENTSEthanol
diM-EtherH2O
MIXED0.00000.00000.0000
LIGHT0.00000.00000.0000
HEAVY
UNIT OPERATIONS
FEED TOValve: VLV-102
PRODUCT FROMDistillation: T-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 139.0 psiaFlow Specification (Inactive) Molar: 956.0 lbmole/hr Mass: 4.403e+004 lb/hr Std Ideal Liq Volume:4497 barrel/day
User Variables
NOTES
Description
Material Stream: 9Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall0.0000320.5159.0261.85601418.0
-1.133e+00515.54
-2.966e+007410.3 *
Aqueous Phase1.0000320.5159.0261.85601418.0
-1.133e+00515.54
-2.966e+007410.3
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2
(lbmole/ft3)(lb/ft3)
(barrel/day)(Btu/lb)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole)
(Btu/lb)
(psia)
Overall21.402.33249.89479.9-5296
0.726222.691.061
6.577e+0043074
0.00000.0000
Aqueous Phase21.402.33249.89479.9-5296
0.726222.691.061
6.577e+00430741.0001.000
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 17 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 9 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(Cost/s)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(lb/ft3)
(USGPM)
(psia)
(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)
(psia)(psia)
(barrel/day)
Overall0.0000
2.67722.692.38057.2814.00
8.144e-00310.64
0.00001.0961.213
1.539e+0040.168258.35410.31.000
0.4288719.1
0.000038.26
0.28990.134420.70
0.967718.70
0.8741
4.4812.329410.3
Aqueous Phase0.0000
2.67722.692.38057.2814.00
8.144e-00310.64
1.0961.213
0.168258.35410.31.000
0.4288
1.000038.26
0.28990.134420.70
0.967718.70
0.8741
4.4812.329410.3
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
53.12774.95570.0198
203.6738
MOLE FRACTION
0.20300.01890.00010.7780
MASS FLOW (lb/hr)
1702.3129228.3065
0.91283669.2044
MASS FRACTION
0.30390.04080.00020.6551
LIQUID VOLUMEFLOW (barrel/day)
146.486419.63970.0932
251.7478
LIQUID VOLUMEFRACTION
0.35050.04700.00020.6023
Total 261.7770 1.0000 5600.7367 1.0000 417.9672 1.0000
Aqueous Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
53.12774.95570.0198
203.6738
MOLE FRACTION
0.20300.01890.00010.7780
MASS FLOW (lb/hr)
1702.3129228.3065
0.91283669.2044
MASS FRACTION
0.30390.04080.00020.6551
LIQUID VOLUMEFLOW (barrel/day)
146.486419.63970.0932
251.7478
LIQUID VOLUMEFRACTION
0.35050.04700.00020.6023
Total 261.7770 1.0000 5600.7367 1.0000 417.9672 1.0000
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 18 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 9 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED0.00000.00000.00000.0000
LIGHT HEAVY0.00000.00000.00000.0000
UNIT OPERATIONS
FEED TOValve: VLV-101
PRODUCT FROMDistillation: T-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 159.0 psiaFlow Specification (Inactive) Molar: 261.8 lbmole/hr Mass: 5601 lb/hr Std Ideal Liq Volume:418.0 barrel/day
User Variables
NOTES
Description
Material Stream: 10Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall0.275593.091.450 *
261.85601418.0
-1.133e+00514.39
-2.966e+007410.3 *
Vapour Phase0.275593.091.45072.111872150.3
-9.519e+00443.17
-6.864e+006148.3
Aqueous Phase0.724593.091.450189.73729267.7
-1.202e+0053.443
-2.280e+007262.7
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase 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)
Overall21.40
8.875e-0041.899e-0021.261e+006
-52960.672416.65
0.77806.577e+004
30740.35950.3343
Vapour Phase25.96
2.445e-0046.348e-0031.261e+006
-36661.6639.641
0.37131.547e+005
59570.35950.3343
Aqueous Phase19.663.03859.73266.9-6115
0.175219.31
0.98223.198e+004
16270.64050.6657
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 19 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 10 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(psia)(Cost/s)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(lb/ft3)
(USGPM)
(psia)
(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)
(psia)(psia)
(barrel/day)
Overall0.00000.0000
2.67716.652.38057.287.783
10.64
0.00001.1351.034
1.854e+004
58.35410.3
0.72451127866.8
0.275565.90
14.660.685216.10
0.7524
4.4812.329411.0
Vapour Phase
0.000049152.0519.641
0.655553.26
1.00010.64
1.2591.259
65.6053.97148.3
0.00004090
0.2755
9.102e-0036.670e-003
7.6550.29487.655
0.2948
4.4883.249148.3
Aqueous Phase
0.0000
3.02919.311.72459.547.783
8.048e-00510.64
1.1151.164
0.766960.66262.71.000
0.3291
0.724565.90
0.32130.733717.32
0.881216.59
0.8438
4.4701.775262.7
-0.8995
COMPOSITION
Overall Phase Vapour Fraction 0.2755
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
53.12774.95570.0198
203.6738
MOLE FRACTION
0.20300.01890.00010.7780
MASS FLOW (lb/hr)
1702.3129228.3065
0.91283669.2044
MASS FRACTION
0.30390.04080.00020.6551
LIQUID VOLUMEFLOW (barrel/day)
146.486419.63970.0932
251.7478
LIQUID VOLUMEFRACTION
0.35050.04700.00020.6023
Total 261.7770 1.0000 5600.7367 1.0000 417.9672 1.0000
Vapour Phase Phase Fraction 0.2755
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
34.24103.29110.0195
34.5561
MOLE FRACTION
0.47490.04560.00030.4792
MASS FLOW (lb/hr)
1097.1474151.6208
0.8995622.5315
MASS FRACTION
0.58600.08100.00050.3325
LIQUID VOLUMEFLOW (barrel/day)
94.411113.04290.0919
42.7125
LIQUID VOLUMEFRACTION
0.62830.08680.00060.2843
Total 72.1077 1.0000 1872.1992 1.0000 150.2584 1.0000
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 10 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
COMPOSITION
Aqueous Phase Phase Fraction 0.7245
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
18.88671.66460.0003
169.1177
MOLE FRACTION
0.09960.00880.00000.8916
MASS FLOW (lb/hr)
605.165676.68570.0133
3046.6729
MASS FRACTION
0.16230.02060.00000.8171
LIQUID VOLUMEFLOW (barrel/day)
52.07546.59680.0014
209.0353
LIQUID VOLUMEFRACTION
0.19450.02460.00000.7808
Total 189.6693 1.0000 3728.5375 1.0000 267.7088 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED4.7695.201177.7
0.5375
LIGHT HEAVY4.7695.201177.7
0.5375
UNIT OPERATIONS
FEED TODistillation: T-101
PRODUCT FROMValve: VLV-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Active): 1.450 psia *
Flow Specification (Inactive) Molar: 261.8 lbmole/hr Mass: 5601 lb/hr Std Ideal Liq Volume:418.0 barrel/day
User Variables
NOTES
Description
Material Stream: 11Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall0.000092.713.75555.801820156.6
-1.033e+00510.15
-5.765e+006156.2 *
Liquid Phase1.000092.713.75555.801820156.6
-1.033e+00510.15
-5.765e+006156.2
PROPERTIES
Molecular WeightOverall
32.62Liquid Phase
32.62
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 11 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Molar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)
(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)
(psia)(psia)
(barrel/day)
Overall1.49048.61160.1-3167
0.311228.15
0.86302.849e+005
8734
2.122e-3140.00000.0000
1.52328.15
0.507249.694.669
4.251e-00410.63
0.00001.0761.339
1.624e+0040.641149.83156.21.000
0.6711497.9
0.000028.05
0.10170.499226.17
0.802121.02
0.6444
4.570156.2
-1.755
Liquid Phase1.49048.61160.1-3167
0.311228.15
0.86302.849e+005
87341.0001.000
0.0000
1.52328.15
0.507249.694.669
4.251e-00410.63
1.0761.339
0.641149.83156.21.000
0.6711
1.000028.05
0.10170.499226.17
0.802121.02
0.6444
4.570156.2
-1.755
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
53.06622.50360.01980.2086
MOLE FRACTION
0.95100.04490.00040.0037
MASS FLOW (lb/hr)
1700.3431115.3383
0.91283.7578
MASS FRACTION
0.93410.06340.00050.0021
LIQUID VOLUMEFLOW (barrel/day)
146.31699.92180.09320.2578
LIQUID VOLUMEFRACTION
0.93440.06340.00060.0016
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 11 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.0000
Total 55.7982 1.0000 1820.3521 1.0000 156.5898 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
53.06622.50360.01980.2086
MOLE FRACTION
0.95100.04490.00040.0037
MASS FLOW (lb/hr)
1700.3431115.3383
0.91283.7578
MASS FRACTION
0.93410.06340.00050.0021
LIQUID VOLUMEFLOW (barrel/day)
146.31699.92180.09320.2578
LIQUID VOLUMEFRACTION
0.93440.06340.00060.0016
Total 55.7982 1.0000 1820.3521 1.0000 156.5898 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED0.00000.00000.00000.0000
LIGHT0.00000.00000.00000.0000
HEAVY
UNIT OPERATIONS
FEED TOPump: P-101
PRODUCT FROMDistillation: T-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 3.755 psiaFlow Specification (Inactive) Molar: 55.80 lbmole/hr Mass: 1820 lb/hr Std Ideal Liq Volume:156.6 barrel/day
User Variables
NOTES
Description
Material Stream: 12Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall0.000093.58152.3 *
55.801820156.6
-1.033e+00517.57
-5.763e+006156.2 *
Liquid Phase1.000093.58152.355.801820156.6
-1.033e+00517.57
-5.763e+006156.2
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 12 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)
(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)
(psia)(psia)
(barrel/day)
Overall32.621.49048.62160.0-3166
0.538528.17
0.86332.849e+005
8734
2.122e-3140.00000.0000
1.52328.17
0.507249.694.668
1.721e-00210.63
0.00001.0761.337
1.275e+0040.637149.83156.21.000
0.6710390.9
0.000027.97
0.10160.496226.18
0.802521.07
0.6457
4.570156.2
-1.766
Liquid Phase32.621.49048.62160.0-3166
0.538528.17
0.86332.849e+005
87341.0001.000
0.0000
1.52328.17
0.507249.694.668
1.721e-00210.63
1.0761.337
0.637149.83156.21.000
0.6710
1.000027.97
0.10160.496226.18
0.802521.07
0.6457
4.570156.2
-1.766
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-Ether
MOLAR FLOW (lbmole/hr)
53.06622.50360.0198
MOLE FRACTION
0.95100.04490.0004
MASS FLOW (lb/hr)
1700.3431115.3383
0.9128
MASS FRACTION
0.93410.06340.0005
LIQUID VOLUMEFLOW (barrel/day)
146.31699.92180.0932
LIQUID VOLUMEFRACTION
0.93440.06340.0006
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 12 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.0000
COMPONENTS
H2O
MOLAR FLOW (lbmole/hr)
0.2086
MOLE FRACTION
0.0037
MASS FLOW (lb/hr)
3.7578
MASS FRACTION
0.0021
LIQUID VOLUMEFLOW (barrel/day)
0.2578
LIQUID VOLUMEFRACTION
0.0016Total 55.7982 1.0000 1820.3521 1.0000 156.5898 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
53.06622.50360.01980.2086
MOLE FRACTION
0.95100.04490.00040.0037
MASS FLOW (lb/hr)
1700.3431115.3383
0.91283.7578
MASS FRACTION
0.93410.06340.00050.0021
LIQUID VOLUMEFLOW (barrel/day)
146.31699.92180.09320.2578
LIQUID VOLUMEFRACTION
0.93440.06340.00060.0016
Total 55.7982 1.0000 1820.3521 1.0000 156.5898 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED0.00000.00000.00000.0000
LIGHT0.00000.00000.00000.0000
HEAVY
UNIT OPERATIONS
FEED TORecycle: RCY-1
PRODUCT FROMPump: P-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Active): 152.3 psia *
Flow Specification (Inactive) Molar: 55.80 lbmole/hr Mass: 1820 lb/hr Std Ideal Liq Volume:156.6 barrel/day
User Variables
NOTES
Description
Material Stream: 13Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)
Overall0.000093.60 *
152.3 *
55.84 *
1822156.7
-1.033e+00517.57
Liquid Phase1.000093.60152.355.841822156.7
-1.033e+00517.57
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 13 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Heat Flow (Btu/hr)Liq Vol Flow @Std Cond (barrel/day)
Overall-5.768e+006
156.3 *
Liquid Phase-5.768e+006
156.3
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)
(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)
(psia)(psia)
(barrel/day)
Overall32.631.49048.62160.2-3166
0.538428.17
0.86332.851e+005
8736
2.122e-3140.00000.0000
1.52328.17
0.507649.694.672
1.721e-00210.63
0.00001.0761.337
1.276e+0040.637349.83156.31.000
0.6711390.9
0.000027.97
0.10160.496326.18
0.802421.08
0.6459
4.562156.3
-1.766
Liquid Phase32.631.49048.62160.2-3166
0.538428.17
0.86332.851e+005
87361.0001.000
0.0000
1.52328.17
0.507649.694.672
1.721e-00210.63
1.0761.337
0.637349.83156.31.000
0.6711
1.000027.97
0.10160.496326.18
0.802421.08
0.6459
4.562156.3
-1.766
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: 13 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
53.0680 *
2.5380 *
0.0198 *
0.2153 *
MOLE FRACTION
0.9503 *
0.0455 *
0.0004 *
0.0039 *
MASS FLOW (lb/hr)
1700.4011 *
116.9262 *
0.9126 *
3.8788 *
MASS FRACTION
0.9332 *
0.0642 *
0.0005 *
0.0021 *
LIQUID VOLUMEFLOW (barrel/day)
146.3219 *
10.0584 *
0.0932 *
0.2661 *
LIQUID VOLUMEFRACTION
0.9335 *
0.0642 *
0.0006 *
0.0017 *
Total 55.8412 1.0000 1822.1187 1.0000 156.7396 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
53.06802.53800.01980.2153
MOLE FRACTION
0.95030.04550.00040.0039
MASS FLOW (lb/hr)
1700.4011116.9262
0.91263.8788
MASS FRACTION
0.93320.06420.00050.0021
LIQUID VOLUMEFLOW (barrel/day)
146.321910.05840.09320.2661
LIQUID VOLUMEFRACTION
0.93350.06420.00060.0017
Total 55.8412 1.0000 1822.1187 1.0000 156.7396 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED0.00000.00000.00000.0000
LIGHT0.00000.00000.00000.0000
HEAVY
UNIT OPERATIONS
FEED TOMixer: MIX-100
PRODUCT FROMRecycle: RCY-1
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 152.3 psia *
Flow Specification (Inactive) Molar: 55.84 lbmole/hr * Mass: 1822 lb/hr Std Ideal Liq Volume:156.7 barrel/day
User Variables
NOTES
Description
Material Stream: AGUAFluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)
Overall0.0000203.013.76206.03780
Aqueous Phase1.0000203.013.76206.03780
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: AGUA (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
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)
Overall261.4
-1.201e+0055.664
-2.475e+007256.0 *
Aqueous Phase261.4
-1.201e+0055.664
-2.475e+007256.0
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)
(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)
(psia)(psia)
(barrel/day)
Overall18.353.22459.17273.1-6546
0.308618.31
0.99796405349.0
0.00000.00000.0000
3.36918.311.87261.837.965
6.000e-00410.76
0.00001.1221.182
1.759e+0040.316063.12256.01.000
0.3102958.6
0.000059.02
0.38700.299616.33
0.889715.49
0.8442
1.102256.0
-2.518
Aqueous Phase18.353.22459.17273.1-6546
0.308618.31
0.99796405349.01.0001.000
0.0000
3.36918.311.87261.837.965
6.000e-00410.76
1.1221.182
0.316063.12256.01.000
0.3102
1.000059.02
0.38700.299616.33
0.889715.49
0.8442
1.102256.0
-2.518
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: AGUA (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
0.06152.45210.0000
203.4652
MOLE FRACTION
0.00030.01190.00000.9878
MASS FLOW (lb/hr)
1.9696112.9681
0.00003665.4467
MASS FRACTION
0.00050.02990.00000.9696
LIQUID VOLUMEFLOW (barrel/day)
0.16959.71790.0000
251.4900
LIQUID VOLUMEFRACTION
0.00060.03720.00000.9622
Total 205.9788 1.0000 3780.3844 1.0000 261.3774 1.0000
Aqueous Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
0.06152.45210.0000
203.4652
MOLE FRACTION
0.00030.01190.00000.9878
MASS FLOW (lb/hr)
1.9696112.9681
0.00003665.4467
MASS FRACTION
0.00050.02990.00000.9696
LIQUID VOLUMEFLOW (barrel/day)
0.16959.71790.0000
251.4900
LIQUID VOLUMEFRACTION
0.00060.03720.00000.9622
Total 205.9788 1.0000 3780.3844 1.0000 261.3774 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED0.00000.0000
0.0000
LIGHT HEAVY0.00000.0000
0.0000
UNIT OPERATIONS
FEED TO PRODUCT FROMDistillation: T-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 13.76 psiaFlow Specification (Inactive) Molar: 206.0 lbmole/hr Mass: 3780 lb/hr Std Ideal Liq Volume:261.4 barrel/day
User Variables
NOTES
Description
Material Stream: DMEFluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)
Overall0.0133106.2131.7956.0
4.403e+004
Vapour Phase0.0133106.2131.712.75587.2
Liquid Phase0.9867106.2131.7943.3
4.344e+004
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: DME (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
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)
Overall4497
-8.662e+00437.54
-8.281e+0074878 *
Vapour Phase59.98
-7.872e+00442.87
-1.003e+00665.07
Liquid Phase4437
-8.672e+00437.47
-8.181e+0074813
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)
(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)
(psia)(psia)
(barrel/day)
Overall46.06
0.534124.607651
-18810.815127.86
0.60505.708e+0051.239e+0041.334e-0021.334e-002
0.00000.0000
0.908727.868.69041.85149.9
11.38
0.00001.0771.0078026
38.584878
0.98671.872174.3
0.01339.542
25.880.561927.66
0.6006
120.4120.74878
Vapour Phase46.07
2.169e-0020.9995
2511-1709
0.930716.27
0.35335.711e+0051.240e+0041.334e-0021.334e-002
0.00009.792
0.908316.27
0.115941.85
1.00011.38
1.1391.139
0.594438.5765.07
0.000046.09
0.0133
1.046e-0029.516e-003
14.290.310214.29
0.3102
120.665.07
Liquid Phase46.05
0.784536.135140
-18830.813528.02
0.60845.708e+0051.239e+004
0.98670.9867
0.0000
0.908728.028.57441.85149.9
2.765e-00211.38
1.0761.076
0.133038.5848131.0001.275
0.98679.542
7.093e-0027.696e-002
26.030.565326.03
0.5653
120.4120.74813
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: DME (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
COMPOSITION
Overall Phase Vapour Fraction 0.0133
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
0.93850.0100
955.07410.0075
MOLE FRACTION
0.00100.00000.99900.0000
MASS FLOW (lb/hr)
30.07220.4627
43999.31070.1346
MASS FRACTION
0.00070.00000.99930.0000
LIQUID VOLUMEFLOW (barrel/day)
2.58780.0398
4494.62670.0092
LIQUID VOLUMEFRACTION
0.00060.00000.99940.0000
Total 956.0302 1.0000 44029.9802 1.0000 4497.2635 1.0000
Vapour Phase Phase Fraction 1.333e-002
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
0.00040.0000
12.74520.0000
MOLE FRACTION
0.00000.00001.00000.0000
MASS FLOW (lb/hr)
0.01390.0001
587.15650.0000
MASS FRACTION
0.00000.00001.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00120.0000
59.97930.0000
LIQUID VOLUMEFRACTION
0.00000.00001.00000.0000
Total 12.7456 1.0000 587.1706 1.0000 59.9805 1.0000
Liquid Phase Phase Fraction 0.9867
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
0.93820.0100
942.32890.0075
MOLE FRACTION
0.00100.00000.99900.0000
MASS FLOW (lb/hr)
30.06160.4626
43412.14930.1346
MASS FRACTION
0.00070.00000.99930.0000
LIQUID VOLUMEFLOW (barrel/day)
2.58680.0398
4434.64690.0092
LIQUID VOLUMEFRACTION
0.00060.00000.99940.0000
Total 943.2846 1.0000 43442.8081 1.0000 4437.2828 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED3.431e-0021.988e-002
1.0011.237e-002
LIGHT3.431e-0021.988e-002
1.0011.237e-002
HEAVY
UNIT OPERATIONS
FEED TO PRODUCT FROMValve: VLV-102
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 131.7 psiaFlow Specification (Inactive) Molar: 956.0 lbmole/hr Mass: 4.403e+004 lb/hr Std Ideal Liq Volume:4497 barrel/day
User Variables
NOTES
Description
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 31 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: P-RFluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (lbmole/hr)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)
Overall0.0000248.0152.31043
2.265e+0041753
-1.144e+00513.25
-1.193e+0081704 *
Vapour Phase0.0000248.0152.3
0.00000.00000.0000
-8.105e+00444.88
0.00000.0000
Aqueous Phase1.0000248.0152.31043
2.265e+0041753
-1.144e+00513.25
-1.193e+0081704
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)
(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)
(psia)
(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)
Overall21.722.33550.731909
-52650.610023.711.091
7.476e+0043442
4.941e-3240.00000.0000
2.54323.719.47855.2455.67
11.25
0.00001.0911.180
1.637e+0040.196656.8217041.000
0.4282753.4
0.000046.98
0.30810.159821.72
0.999920.09
0.9248
Vapour Phase40.75
2.005e-0020.81730.0000-19891.10117.07
0.41904.623e+0051.134e+004
0.0000
0.0000
1.05917.07
0.000043.16
1.00011.37
1.1321.132
0.887140.98
0.00000.000049.87
0.0000
1.477e-0021.161e-002
15.090.370215.09
0.3702
Aqueous Phase21.722.33550.731909
-52650.610023.711.091
7.476e+00434421.0001.000
0.0000
2.54323.719.47855.2455.67
8.588e-00311.25
1.0911.180
0.196656.8217041.000
0.4282
1.000046.98
0.30810.159821.72
0.999920.09
0.9248
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: P-R (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROPERTIES
Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(psia)(psia)
(barrel/day)
Overall77.1422.601704
Vapour Phase113.194.98
0.0000
Aqueous Phase77.1422.601704
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
52.52874.0962
107.4486878.5611
MOLE FRACTION
0.05040.00390.10310.8426
MASS FLOW (lb/hr)
1683.1186188.7114
4950.049115827.3669
MASS FRACTION
0.07430.00830.21860.6988
LIQUID VOLUMEFLOW (barrel/day)
144.834716.2336
505.65841085.9316
LIQUID VOLUMEFRACTION
0.08260.00930.28850.6196
Total 1042.6346 1.0000 22649.2460 1.0000 1752.6584 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
0.00000.00000.00000.0000
MOLE FRACTION
0.04440.00410.78430.1673
MASS FLOW (lb/hr)
0.00000.00000.00000.0000
MASS FRACTION
0.03490.00460.88660.0739
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.03030.00400.91440.0512
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Aqueous Phase Phase Fraction 1.000
COMPONENTS
MethanolEthanoldiM-EtherH2O
MOLAR FLOW (lbmole/hr)
52.52874.0962
107.4486878.5611
MOLE FRACTION
0.05040.00390.10310.8426
MASS FLOW (lb/hr)
1683.1186188.7114
4950.049115827.3669
MASS FRACTION
0.07430.00830.21860.6988
LIQUID VOLUMEFLOW (barrel/day)
144.834716.2336
505.65841085.9316
LIQUID VOLUMEFRACTION
0.08260.00930.28850.6196
Total 1042.6346 1.0000 22649.2460 1.0000 1752.6584 1.0000
K VALUE
COMPONENTSMethanol
EthanoldiM-Ether
H2O
MIXED0.88121.0387.610
0.1985
LIGHT HEAVY0.88121.0387.610
0.1985
UNIT OPERATIONS
FEED TO PRODUCT FROMEquilibrium Reactor: ERV-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive) 152.3 psiaFlow Specification (Inactive) Molar: 1043 lbmole/hr Mass: 2.265e+004 lb/hr Std Ideal Liq Volume:1753 barrel/day
User Variables
NOTESHyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 33 of 76
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Material Stream: P-R (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
NOTES
Description
Energy Stream: Q1Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: E-100Duty SP: 9.883e+006 Btu/hr Minimum Available Duty: Maximum Available Duty:
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TOHeater: E-100
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive)Flow Specification (Inactive) Molar: Mass: Std Ideal Liq Volume:
User Variables
NOTES
Description
Energy Stream: Q2Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: ERV-100Duty SP: 1.163e+007 Btu/hr Minimum Available Duty: Maximum Available Duty:
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TOEquilibrium Reactor: ERV-100
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive)
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Energy Stream: Q2 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
DYNAMICS
Flow Specification (Inactive) Molar: Mass: Std Ideal Liq Volume:
User Variables
NOTES
Description
Energy Stream: Q3Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: E-101Duty SP: 5.013e+006 Btu/hr Minimum Available Duty: Maximum Available Duty:
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO PRODUCT FROMCooler: E-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive)Flow Specification (Inactive) Molar: Mass: Std Ideal Liq Volume:
User Variables
NOTES
Description
Energy Stream: Q4Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Condenser @COL1Duty SP: 6.041e+007 Btu/hr Minimum Available Duty: Maximum Available Duty:
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO PRODUCT FROMDistillation: T-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Energy Stream: Q4 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive)Flow Specification (Inactive) Molar: Mass: Std Ideal Liq Volume:
User Variables
NOTES
Description
Energy Stream: Q5Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Reboiler @COL1Duty SP: 5.166e+007 Btu/hr Minimum Available Duty: Maximum Available Duty:
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TODistillation: T-100
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive)Flow Specification (Inactive) Molar: Mass: Std Ideal Liq Volume:
User Variables
NOTES
Description
Energy Stream: Q6Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Condenser @COL2Duty SP: 3.402e+013 Btu/hr Minimum Available Duty: Maximum Available Duty:
COMPOSITION
( Not a material stream - No compositions exist )
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 36 of 76
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Energy Stream: Q6 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
UNIT OPERATIONS
FEED TO PRODUCT FROMDistillation: T-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive)Flow Specification (Inactive) Molar: Mass: Std Ideal Liq Volume:
User Variables
NOTES
Description
Energy Stream: Q7Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Reboiler @COL2Duty SP: 3.402e+013 Btu/hr Minimum Available Duty: Maximum Available Duty:
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TODistillation: T-101
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive)Flow Specification (Inactive) Molar: Mass: Std Ideal Liq Volume:
User Variables
NOTES
Description
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Energy Stream: Q-100Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: P-101Duty SP: 1372 Btu/hr Minimum Available Duty: Maximum Available Duty:
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TOPump: P-101
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive)Flow Specification (Inactive) Molar: Mass: Std Ideal Liq Volume:
User Variables
NOTES
Description
Energy Stream: W1Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: P-100Duty SP: 4.993e+004 Btu/hr Minimum Available Duty: Maximum Available Duty:
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TOPump: P-100
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
DYNAMICS
Pressure Specification (Inactive)Flow Specification (Inactive) Molar: Mass: Std Ideal Liq Volume:
User Variables
NOTES
Description
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Energy Stream: W1 (continued)Fluid Package: Basis-1
Property Package: UNIQUAC - Ideal
Recycle: RCY-1
CONNECTIONS
Inlet Stream
Stream Name From Unit Operation
12 P-101Pump
Outlet Stream
Stream Name To Unit Operation
13 MIX-100Mixer
TOLERANCE
Vapour Fraction: 10.00 * Temperature: 10.00 * Pressure: 10.00 *
Flow: 10.00 * Enthalpy: 10.00 * Composition: 10.00 *
NUMERICAL
Acceleration Type: Wegstein Iteration Type: NestedMaximum Iterations: 10 * Iteration Count: 0 *
Wegstein Count: 3 * Q Minimum: -20.00 * Q Maximum: 0.0000 *
Iteration History
Iteration0 *
VariableConverged
Outlet Value Inlet Value
User Variables
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
120.0000
93.5826152.2896 *
55.79821820.3521156.5898
-1.033e+00517.57
-5.7633e+06
130.0000
93.5961 *
152.2896 *
55.8412 *
1822.1187156.7396
-1.033e+00517.57
-5.7684e+06
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. 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)
1232.621.49048.62160.0-3166
0.538528.17
0.86332.849e+005
8734
2.122e-3140.00000.0000
1.523
1332.631.49048.62160.2-3166
0.538428.17
0.86332.851e+005
8736
2.122e-3140.00000.0000
1.523
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Recycle: RCY-1 (continued)
PROPERTIES
NameSpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(Btu/lbmole-F)(MMSCFD)
(lb/ft3)(USGPM)
(psia)
(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)
(psia)(psia)
(barrel/day)
1228.17
0.507249.694.668
1.721e-00210.63
0.00001.0761.337
1.275e+0040.637149.83156.21.000
0.6710390.9
0.000027.97
0.10160.496226.18
0.802521.07
0.6457
4.570156.2
-1.766
1328.17
0.507649.694.672
1.721e-00210.63
0.00001.0761.337
1.276e+0040.637349.83156.31.000
0.6711390.9
0.000027.97
0.10160.496326.18
0.802421.08
0.6459
4.562156.3
-1.766
Heater: E-100
CONNECTIONS
Inlet Stream
STREAM NAME FROM UNIT OPERATION
3 MIX-100Mixer
Outlet Stream
STREAM NAME TO UNIT OPERATION
4 ERV-100Equilibrium Reactor
Energy Stream
STREAM NAME FROM UNIT OPERATION
Q1
PARAMETERS
Pressure Drop: 0.0000 psi * Duty: 9.883e+006 Btu/hr Volume: 3.531 ft3Function: Not Selected Zones: 1
User Variables
RATING
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Heater: E-100 (continued)
NOZZLE PARAMETERS
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)
30.16400.00000.0000
40.16400.00000.0000
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
30.0000
25.9755152.2896
2260.441272279.88766587.4213
-1.059e+005-78.13
-2.3947e+08
40.0406
192.2000 *
152.28962260.4412
72279.88766587.4213
-1.016e+00526.93
-2.2959e+08
Q1
9.8829e+06
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (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)
(psia)
(Btu/lbmole)(cSt)
(lb/ft3)(barrel/day)
(ft3/lbmole)(Btu/lb)
(dyne/cm)(Btu/hr-ft-F)
(cP)(Btu/lbmole-F)
331.981.50147.996438
-3313-2.44322.71
0.71012.817e+005
8808
2.122e-3140.00000.0000
1.46722.7120.5546.90187.8
1.947e-00211.25
0.00001.0961.233
1.424e+0040.514246.7366121.000
0.6663445.2
0.000043.98
0.16480.395320.72
431.98
0.386112.35
2.502e+004-3176
0.842226.74
0.83622.817e+005
88086.243e-0025.631e-002
0.00000.0000
1.46726.7420.5546.90204.3
11.25
0.00001.0801.005
1.424e+004
46.736612
0.95942.590445.2
0.040630.60
24.75
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
20.00 40.00 60.00 80.00 100.0 120.0 140.0 160.0 180.0 200.0
Temperature (F)
147.0
148.0
149.0
150.0
151.0
152.0
153.0
154.0
155.0
156.0
157.0
Pre
ssur
e (p
sia)
Heater: E-100 (continued)
PROPERTIES
NameMass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)
(psia)(psia)
(barrel/day)
30.648018.42
0.5760393.912.32
5.765e-00275.0747.836612
-2.314
40.774126.60
0.8320
75.0747.836626
PERFORMANCE PROFILES
Zone
Inlet0
Pressure (psia)
152.29152.29
Temperature (F)
25.98192.20
Vapour Fraction
0.00000.0406
Enthalpy (Btu/lbmole)
-105940.60-101568.53
PERFORMANCE PLOT
PERFORMANCE TABLE
Overall Phase
Temperature (F)
25.98192.20
Pressure (psia)
152.29152.29
Heat Flow (Btu/hr)
0.009882901.31
Enthalpy (Btu/lbmole)
-105940.60-101568.53
Vapour Fraction
0.00000.0406
Vapour Phase
Mass Flow (lb/hr)
4069.77
Molecular Weight
44.34
Density (lb/ft3)
0.97
Mass Specific Heat (Btu/lb-F)
0.39
Viscosity (cP)
0.01
Thermal Conductivity (Btu/hr-ft-F)
0.01
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Heater: E-100 (continued)
PERFORMANCE TABLE
Light Liquid Phase
Mass Flow (lb/hr)
72279.8968210.12
Density (lb/ft3)
47.9941.63
Mass Specific Heat (Btu/lb-F)
0.710.86
Viscosity (cP)
0.14
Thermal Conductivity (Btu/hr-ft-F)
0.15
Surface Tension (dyne/cm)
43.9830.60
Heavy Liquid Phase
Mass Flow (lb/hr)
Density (lb/ft3)
Mass Specific Heat (Btu/lb-F)
Viscosity (cP)
Thermal Conductivity (Btu/hr-ft-F)
Surface Tension (dyne/cm)
DYNAMICS
Model Details: Supplied Duty
ZoneVolume (ft3)Duty (Btu/hr)
1 *
3.531 *
9.883e+006
Delta P (psi)Overall K (lb/hr/sqrt(psia-lb/ft3))
0.0000 *
8.341e-002 *
Holdup Details
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)
0.00000.00000.0000
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
Individual Zone Holdups: Zone 0
Delta P Specs and Duties
Zone
0 *
dP Value (psi)
0.0000 *
dP Option
not specified
Duty (Btu/hr)
3.658e+006 *
Zone Conductance Specifications
Zone
0 *
k (lb/hr/sqrt(psia-lb/ft3))
8.341e-002
Specification
Disabled
NOTES
Cooler: E-101
CONNECTIONS
Inlet Stream
STREAM NAME FROM UNIT OPERATION
6 VLV-100Valve
Outlet Stream
STREAM NAME TO UNIT OPERATION
7 T-100Distillation
Energy Stream
STREAM NAME TO UNIT OPERATION
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Cooler: E-101 (continued)
CONNECTIONS
Q3
PARAMETERS
Pressure Drop: 0.0000 psi Duty: 5.013e+006 Btu/hr Volume: 3.531 ft3Function: Not Selected Zones: 1
User Variables
NOZZLE PARAMETERS
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)
60.16400.00000.0000
70.16400.00000.0000
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
61.0000
247.9137145.0377 *
1217.807249630.71684915.2307
-8.105e+00444.98
-9.8701e+07
70.7672
192.2000 *
145.0377 *
1217.807249630.71684915.2307
-8.516e+00439.62
-1.0371e+08
Q3
5.0133e+06
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (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)
(psia)
(Btu/lbmole)(cSt)
(lb/ft3)
640.75
1.910e-0020.7784
2.725e+005-19891.10417.06
0.41864.623e+0051.134e+004
4.941e-3240.00000.0000
10631.05917.0611.0743.16
1.00011.37
0.00001.1321.132
1.166e+0040.929740.98
740.75
2.691e-0021.097
1.934e+005-2090
0.972219.13
0.46944.623e+0051.134e+004
0.85330.83540.00000.0000
1.05919.1311.0743.1623.28
11.37
0.00001.1161.087
1.166e+004
40.98
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
190.0 200.0 210.0 220.0 230.0 240.0 250.0
Temperature (F)
140.0
141.0
142.0
143.0
144.0
145.0
146.0
147.0
148.0
149.0
150.0
Pre
ssur
e (p
sia)
Cooler: E-101 (continued)
PROPERTIES
NameLiq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)(psia)
(barrel/day)
65177
0.000052.35286.2
1.0000
1.474e-0021.159e-002
15.070.369815.07
0.3698
113.194.985177
75177
0.232837.16286.2
0.767237.52
17.140.420717.60
0.4318
113.194.985218
PERFORMANCE PROFILES
Zone
Inlet0
Pressure (psia)
145.04145.04
Temperature (F)
247.91192.20
Vapour Fraction
1.00000.7672
Enthalpy (Btu/lbmole)
-81047.22-85163.82
PERFORMANCE PLOT
PERFORMANCE TABLE
Overall Phase
Temperature (F)
247.91
Pressure (psia)
145.04
Heat Flow (Btu/hr)
0.00
Enthalpy (Btu/lbmole)
-81047.22
Vapour Fraction
1.0000
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Cooler: E-101 (continued)
PERFORMANCE TABLE
Overall Phase
Temperature (F)
192.20
Pressure (psia)
145.04
Heat Flow (Btu/hr)
-5013275.30
Enthalpy (Btu/lbmole)
-85163.82
Vapour Fraction
0.7672
Vapour Phase
Mass Flow (lb/hr)
49630.7241459.89
Molecular Weight
40.7544.37
Density (lb/ft3)
0.780.92
Mass Specific Heat (Btu/lb-F)
0.420.39
Viscosity (cP)
0.01
Thermal Conductivity (Btu/hr-ft-F)
0.01
Light Liquid Phase
Mass Flow (lb/hr)
Density (lb/ft3)
Mass Specific Heat (Btu/lb-F)
Viscosity (cP)
Thermal Conductivity (Btu/hr-ft-F)
Surface Tension (dyne/cm)
Heavy Liquid Phase
Mass Flow (lb/hr)
8170.83
Density (lb/ft3)
43.75
Mass Specific Heat (Btu/lb-F)
0.87
Viscosity (cP)
0.15
Thermal Conductivity (Btu/hr-ft-F)
0.20
Surface Tension (dyne/cm)
37.52
DYNAMICS
Model Details: Supplied Duty
ZoneVolume (ft3)Duty (Btu/hr)
1 *
3.531 *
5.013e+006
Delta P (psi)Overall K (lb/hr/sqrt(psia-lb/ft3))
0.00008.341e-002 *
Holdup Details
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)
0.00000.00000.0000
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
Individual Zone Holdups: Zone 0
Delta P Specs and Duties
Zone
0 *
dP Value (psi)
0.0000 *
dP Option
not specified
Duty (Btu/hr)
-6.196e+006 *
Zone Conductance Specifications
Zone
0 *
k (lb/hr/sqrt(psia-lb/ft3))
8.341e-002
Specification
Disabled
NOTES
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Equilibrium Reactor: ERV-100
CONNECTIONS
Inlet Stream Connections
Stream Name From Unit Operation4 E-100Heater
Outlet Stream Connections
Stream Name To Unit Operation5 Valve: VLV-100
P-R
Energy Stream Connections
Stream Name From Unit OperationQ2
PARAMETERS
Physical Parameters Optional Heat Transfer: Heating
Delta P Vessel Volume Duty Energy Stream0.0000 psi 1.163e+007 Btu/hr Q2
User Variables
REACTION DETAILS
ComponentMethanoldiM-Ether
H2O
Molecular Weight32.0446.0718.02
Stoichiometric Coefficient-2 *
1 *
1 *
REACTION RESULTS FOR : Set-1
Extents
Rxn-2
Act. % Conv.77.93
Base Comp.Methanol
Eqm Constant66.55
Rxn Extent (lbmole/hr)188.2
Balance
MethanolEthanol
diM-EtherH2O
Total Inflow (lbmole/hr)
483.09.062874.4894.1
Total Rxn (lbmole/hr)
-376.4-1.721e-015
188.2188.2
Total Outflow (lbmole/hr)
106.69.06210631082
RATING
Sizing
Cylinder Vertical Reactor has a Boot: NoVolume Diameter Height
Nozzles
Base Elevation Relative to Ground Level 0.0000 ft * Diameter Height
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)Elevation (% of Height) (%)
40.16400.00000.0000
50.16400.00000.0000
P-R0.16400.00000.0000
PROPERTIES
NameMolecular Weight
431.98
P-R21.72
540.75
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Equilibrium Reactor: ERV-100 (continued)
PROPERTIES
NameMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)
(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)
(psia)(psia)
(barrel/day)
40.386112.35
2.502e+004-3176
0.842226.74
0.83622.817e+005
88086.243e-0025.631e-002
0.00000.0000
1.46726.7420.5546.90204.3
11.25
0.00001.0801.005
1.424e+004
46.736612
0.95942.590445.2
0.040630.60
24.750.774126.60
0.8320
75.0747.836626
P-R2.33550.731909
-52650.610023.711.091
7.476e+0043442
4.941e-3240.00000.0000
2.54323.719.47855.2455.67
11.25
0.00001.0911.180
1.637e+0040.196656.8217041.000
0.4282753.4
0.000046.98
0.30810.159821.72
0.999920.09
0.9248
77.1422.601704
52.005e-002
0.81732.596e+005
-19891.10117.07
0.41904.623e+0051.134e+004
4.941e-3240.00000.0000
10121.05917.0711.0743.16
0.0000
11.37
0.00001.1321.132
1.161e+0040.887140.985177
0.000049.87284.9
1.0000
1.477e-0021.161e-002
15.090.370215.09
0.3702
113.194.985177
DYNAMICS
Vessel Parameters: Initialize from Product
Vessel Volume (ft3)Vessel Diameter (ft)Vessel Height (ft)Liquid Level Percent (%) 50.00
Level CalculatorFraction CalculatorFeed Delta P (psi)Vessel Pressure (psia)
Vertical cylinderUse levels and nozzles
0.0000152.3
Holdup: Vessel Levels
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Equilibrium Reactor: ERV-100 (continued)Phase
VapourLiquid
Aqueous
Level (ft)
Percent (%)
Volume (ft3)
0.00000.00000.0000
Holdup: Details
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)
0.0000 *
0.0000 *
0.0000 *
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
Duty Valve Source : Direct_Q
SP (Btu/hr)
Min. Available (Btu/hr)
Max. Available (Btu/hr)
1.163e+007
Liquid Heater Height as % of Vessel Volume
Top of Heater : 5.00 % Bottom of Heater : 0.00 %
Heat Flow into the PFR: Heating
NOTES
Mixer: MIX-100
CONNECTIONS
Inlet Stream
STREAM NAME FROM UNIT OPERATION
132
RCY-1
P-100
Recycle
Pump
Outlet Stream
STREAM NAME TO UNIT OPERATION
3 E-100Heater
PARAMETERS
User Variables
NOZZLE PARAMETERS
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)
130.16400.00000.0000
20.16400.00000.0000
30.16400.00000.0000
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)
130.0000
93.5961 *
152.2896 *
55.8412 *
1822.1187156.7396
20.0000
23.8698152.2896
2204.600070457.76896430.6817
30.0000
25.9755152.2896
2260.441272279.88766587.4213
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Mixer: MIX-100 (continued)
CONDITIONS
Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
-1.033e+00517.57
-5.7684e+06
-1.060e+005-80.54
-2.3371e+08
-1.059e+005-78.13
-2.3947e+08
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)
(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)
(psia)(psia)
(barrel/day)
1332.631.49048.62160.2-3166
0.538428.17
0.86332.851e+005
8736
2.122e-3140.00000.0000
1.52328.17
0.507649.694.672
1.721e-00210.63
0.00001.0761.337
1.276e+0040.637349.83156.31.000
0.6711390.9
0.000027.97
0.10160.496326.18
0.802421.08
0.6459
4.562156.3
-1.766
231.961.50247.996275
-3317-2.52022.56
0.70592.816e+005
8810
2.122e-3140.00000.0000
1.46522.5620.0446.83183.0
1.954e-00211.26
0.00001.0971.233
1.426e+0040.511746.6564561.000
0.6659446.3
0.000044.43
0.16640.393420.58
0.643818.30
0.5727384.712.04
5.864e-00278.4349.226456
-2.328
331.981.50147.996438
-3313-2.44322.71
0.71012.817e+005
8808
2.122e-3140.00000.0000
1.46722.7120.5546.90187.8
1.947e-00211.25
0.00001.0961.233
1.424e+0040.514246.7366121.000
0.6663445.2
0.000043.98
0.16480.395320.72
0.648018.42
0.5760393.912.32
5.765e-00275.0747.836612
-2.314
DYNAMICS
Pressure Specification: Set Outlet to Lowest Inlet
Holdup DetailsHyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 50 of 76
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Mixer: MIX-100 (continued)Holdup Details
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)
0.0000 *
0.0000 *
0.0000 *
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
NOTES
Pump: P-100
CONNECTIONS
Inlet Stream
Stream Name From Unit Operation
1
Outlet Stream
Stream Name To Unit Operation
2 MIX-100Mixer
Energy Stream
Stream Name From Unit Operation
W1
PARAMETERS
Adiabatic Efficiency (%): 75.00 Delta P: 137.8 psi * Duty: 19.62 hp
CURVES
Delta P: 137.8 psi * Duty: 19.62 hpCoefficient A: 0.0000 * Coefficient B: 0.0000 * Coefficient C: 0.0000 *
Parameter Preferences Units for Delta P: m Flow Basis ActVolFlow Units for Flow: m3/h
User Variables
RATING
Characteristic Curves
Speed: Flow Head Efficiency (%)
NPSH
NPSH Required NPSH Available Enable NPSH Curves: NoNPSH Curves
Nozzle Paramaters
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)
10.16400.00000.0000
20.16400.00000.0000
Inertia
Rotational inertia (lb-ft2) 11.87 Radius of gyration (ft) 0.3281 Mass (lb) 110.2 Friction loss factor (lb-ft2/s) 1.187
Start Up
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 51 of 76
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Pump: P-100 (continued)Design Flow Typical Operating Capacity 1510 barrel/day
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
10.0000
23.0000 *
14.5038 *
2204.6000 *
70457.76896430.6817
-1.060e+005-83.37
-2.3376e+08
20.0000
23.8698152.2896
2204.600070457.76896430.6817
-1.060e+005-80.54
-2.3371e+08
W1
4.9931e+04
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)
(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)
(psia)
(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)
131.961.50147.976278
-3318-2.60922.55
0.70562.816e+005
8810
2.122e-3140.00000.0000
1.46522.5520.0446.83183.1
1.865e-00311.26
0.00001.0971.235
1.646e+0040.515146.6564561.000
0.6662515.1
0.000044.50
0.16640.395820.56
0.643518.26
0.57153601112.7
6.262e-003
231.961.50247.996275
-3317-2.52022.56
0.70592.816e+005
8810
2.122e-3140.00000.0000
1.46522.5620.0446.83183.0
1.954e-00211.26
0.00001.0971.233
1.426e+0040.511746.6564561.000
0.6659446.3
0.000044.43
0.16640.393420.58
0.643818.30
0.5727384.712.04
5.864e-002
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Pump: P-100 (continued)
PROPERTIES
NameReid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(psia)(psia)
(barrel/day)
178.4349.226456
-2.312
278.4349.226456
-2.328
PERFORMANCE
Results
Total HeadTotal Fluid HeadPressure Head 413.6 ft *
Velocity Head -4.865e-003 ft *
Delta P excluding Static Head Results
DYNAMICS
Dynamic Specifications
Head (ft)Fluid Head (lbf-ft/lbm)Adiabatic Efficiency (rpm)Polytropic Efficiency (%)Pressure Increase (psi)
75.00137.8 *
Not ActiveNot ActiveNot Active
ActiveActive
Power (Btu/hr)
Capacity (barrel/day)
Use Characteristic Curves
Pump is Acting as a Turbine
4.993e+004
6431
Not Active
Not Active
Not Active
Holdup Details
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)
0.0000 *
0.0000 *
0.0000 *
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
NOTES
Pump: P-101
CONNECTIONS
Inlet Stream
Stream Name From Unit Operation
11 T-101Distillation
Outlet Stream
Stream Name To Unit Operation
12 RCY-1Recycle
Energy Stream
Stream Name From Unit Operation
Q-100
PARAMETERS
Adiabatic Efficiency (%): 75.00 Delta P: 148.5 psi Duty: 0.5393 hp
CURVES
Delta P: 148.5 psi Duty: 0.5393 hpCoefficient A: 0.0000 * Coefficient B: 0.0000 * Coefficient C: 0.0000 *
Parameter Preferences Units for Delta P: m Flow Basis ActVolFlow Units for Flow: m3/h
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 53 of 76
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Pump: P-101 (continued)
User Variables
RATING
Characteristic Curves
Speed: Flow Head Efficiency (%)
NPSH
NPSH Required NPSH Available Enable NPSH Curves: NoNPSH Curves
Nozzle Paramaters
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)
110.16400.00000.0000
120.16400.00000.0000
Inertia
Rotational inertia (lb-ft2) 11.87 Radius of gyration (ft) 0.3281 Mass (lb) 110.2 Friction loss factor (lb-ft2/s) 1.187
Start Up
Design Flow Typical Operating Capacity 1510 barrel/day
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
110.0000
92.71013.7550
55.79821820.3521156.5898
-1.033e+00510.15
-5.7647e+06
120.0000
93.5826152.2896 *
55.79821820.3521156.5898
-1.033e+00517.57
-5.7633e+06
Q-100
1.3723e+03
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. 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)
1132.621.49048.61160.1-3167
0.311228.15
0.86302.849e+005
8734
2.122e-3140.00000.0000
1.52328.15
0.507249.69
1232.621.49048.62160.0-3166
0.538528.17
0.86332.849e+005
8734
2.122e-3140.00000.0000
1.52328.17
0.507249.69
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Pump: P-101 (continued)
PROPERTIES
NameAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(USGPM)
(psia)
(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)
(psia)(psia)
(barrel/day)
114.669
4.251e-00410.63
0.00001.0761.339
1.624e+0040.641149.83156.21.000
0.6711497.9
0.000028.05
0.10170.499226.17
0.802121.02
0.6444
4.570156.2
-1.755
124.668
1.721e-00210.63
0.00001.0761.337
1.275e+0040.637149.83156.21.000
0.6710390.9
0.000027.97
0.10160.496226.18
0.802521.07
0.6457
4.570156.2
-1.766
PERFORMANCE
Results
Total HeadTotal Fluid HeadPressure Head 440.0 ft *
Velocity Head -1.155e-006 ft *
Delta P excluding Static Head Results
DYNAMICS
Dynamic Specifications
Head (ft)Fluid Head (lbf-ft/lbm)Adiabatic Efficiency (rpm)Polytropic Efficiency (%)Pressure Increase (psi)
75.00148.5
Not ActiveNot ActiveNot Active
ActiveActive
Power (Btu/hr)
Capacity (barrel/day)
Use Characteristic Curves
Pump is Acting as a Turbine
1372
156.6
Not Active
Not Active
Not Active
Holdup Details
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)
0.0000 *
0.0000 *
0.0000 *
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
NOTES
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-100
CONNECTIONS
Inlet Stream
STREAM NAME Stage FROM UNIT OPERATION
7Q5
4__Main TSReboiler
E-101Cooler
Outlet Stream
STREAM NAME Stage TO UNIT OPERATION
Q489
CondenserCondenserReboiler
VLV-102VLV-101
ValveValve
MONITOR
Specifications SummarySpecified Value Current Value Wt. Error Wt. Tol. Abs. Tol. Active Estimate Used
Distillate Rate 956.0 lbmole/hr 1.000e-002 2.205 lbmole/hr Off On OffReflux Rate 6614 lbmole/hr 1.000e-002 2.205 lbmole/hr Off On OffBtms Prod Rate 261.8 lbmole/hr 1.000e-002 2.205 lbmole/hr Off On OffComp Fraction 1.000e-003 * 1.000e-003 3.893e-006 1.000e-002 1.000e-003 On On OnComp Fraction - 2 1.000e-003 * 1.000e-003 2.353e-005 1.000e-002 1.000e-003 On On On
SPECS
Column Specification Parameters
Distillate Rate
Fixed / Ranged: Fixed Primary / Alternate: Primary Lower Bound: Upper Bound:Stream: 8 @COL1 Flow Basis: Molar
Reflux Rate
Fixed / Ranged: Fixed Primary / Alternate: Primary Lower Bound: Upper Bound:Stage: Condenser Flow Basis: Molar Liquid Specification: ---
Btms Prod Rate
Fixed / Ranged: Fixed Primary / Alternate: Primary Lower Bound: Upper Bound:Stream: 9 @COL1 Flow Basis: Molar
Comp Fraction
Fixed / Ranged: Fixed Primary / Alternate: Primary Lower Bound: Upper Bound:Stage: Condenser Flow Basis: Mole Fraction Phase: LiquidComponents: Methanol Ethanol H2O
Comp Fraction - 2
Fixed / Ranged: Fixed Primary / Alternate: Primary Lower Bound: Upper Bound:Stage: Reboiler Flow Basis: Mole Fraction Phase: VapourComponents: diM-Ether
SUBCOOLING
Degrees of SubcoolingSubcool to
Condenser
User Variables
PROFILES
General ParametersSub-Flow Sheet: T-100 (COL1) Number of Stages: 7 *
Profile Estimates
Condenser
Temperature (F)
110.0
Net Liquid (lbmole/hr)
6614
Net Vapour (lbmole/hr)
1.279e-018
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-100 (continued)Profile Estimates
1__Main TS2__Main TS3__Main TS4__Main TS5__Main TS6__Main TS7__Main TS
Reboiler
Temperature (F)
111.8139.9216.6258.8282.3291.8302.0320.5
Net Liquid (lbmole/hr)
6086451138924206411240143833261.8
Net Vapour (lbmole/hr)
75707042546748483944385037523571
EFFICIENCIES
Stage EfficienciesStages
Condenser1__Main TS2__Main TS3__Main TS4__Main TS5__Main TS6__Main TS7__Main TSReboiler
Overall Efficiency1.0001.0001.0001.0001.0001.0001.0001.0001.000
Methanol1.0001.0001.0001.0001.0001.0001.0001.0001.000
Ethanol1.0001.0001.0001.0001.0001.0001.0001.0001.000
diM-Ether1.0001.0001.0001.0001.0001.0001.0001.0001.000
H2O1.0001.0001.0001.0001.0001.0001.0001.0001.000
SOLVER
Column Solving Algorithm: HYSIM Inside-OutSolving Options
Maximum Iterations: 10000Equilibrium Error Tolerance: 1.000e-05Heat/Spec Error Tolerance: 5.000e-004Save Solutions as Initial Estimate: OnSuper Critical Handling Model: Simple KTrace Level: LowInit from Ideal K's: Off
Initial Estimate Generator ParametersIterative IEG (Good for Chemicals): Off
Acceleration ParametersAccelerate K Value & H Model Parameters: Off
Damping ParametersAzeotrope Check: OffFixed Damping Factor: 1
SIDE STRIPPERS
SIDE RECTIFIERS
PUMP AROUNDS
VAP BYPASSES
RATING
Tray Sections
Tray SectionTray Diameter (ft)Weir Height (ft)Weir Length (ft)Tray Space (ft)Tray Volume (ft3)Disable Heat Loss CalculationsHeat ModelRating Calculations
Main TS @COL14.9210.1640 *
3.937 *
1.804 *
34.32No
NoneNo
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-100 (continued)Tray Hold Up (ft3) 3.120
Vessels
VesselDiameter (ft)Length (ft)Volume (ft3)OrientationVessel has a BootBoot Diameter (ft)Boot Length (ft)Hold Up (ft3)
Reboiler @COL13.9145.87170.63 *
HorizontalNo
35.31
Condenser @COL13.9145.87170.63 *
HorizontalNo
35.31
Other Equipment In Column Flowsheet
Pressure Profile
Pressure (psia) Pressure Drop (psi)Condenser1__Main TS2__Main TS3__Main TS4__Main TS5__Main TS6__Main TS7__Main TS
Reboiler
139.0 psia *
139.0 psia142.3 psia145.7 psia149.0 psia152.3 psia155.7 psia159.0 psia159.0 psia *
0.0000 psi3.333 psi3.333 psi3.333 psi3.333 psi3.333 psi3.333 psi
0.0000 psi
Pressure Solving Options
Pressure Tolerance 1.000e-004 Pressure Drop Tolerance 1.000e-004 Damping Factor 1.000 Max Press Iterations 100
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
70.7672
192.2000 *
145.0377 *
1217.807249630.71684915.2307
-8.516e+00439.62
-1.0371e+08
80.0000
110.0070139.0000956.0302
44029.98024497.2635
-8.662e+00437.85
-8.2809e+07
90.0000
320.5048159.0000261.7770
5600.7367417.9672
-1.133e+00515.54
-2.9664e+07
Q5
5.1655e+07
Q4
6.0414e+07
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas 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)(ACFM)
740.75
2.691e-0021.097
1.934e+005-2090
0.972219.13
0.46944.623e+0051.134e+004
0.85330.83540.00000.0000
846.06
0.779935.925240
-18810.821928.21
0.61265.708e+0051.239e+004
2.122e-3140.00000.0000
921.402.33249.89479.9-5296
0.726222.691.061
6.577e+0043074
0.00000.00000.0000
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-100 (continued)
PROPERTIES
NameAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(lb/ft3)
(USGPM)
(psia)
(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)
(psia)(psia)
(barrel/day)
71.05919.1311.0743.1623.28
11.37
0.00001.1161.087
1.166e+004
40.985177
0.232837.16286.2
0.767237.52
17.140.420717.60
0.4318
113.194.985218
80.908728.218.69041.85152.8
2.915e-00211.38
0.00001.0761.0767981
0.131238.5848781.0001.282173.3
0.00009.257
7.011e-0027.548e-002
26.230.569526.23
0.5695
120.4120.74878
92.67722.692.38057.2814.00
8.144e-00310.64
0.00001.0961.213
1.539e+0040.168258.35410.31.000
0.4288719.1
0.000038.26
0.28990.134420.70
0.967718.70
0.8741
4.4812.329410.3
SUMMARY
Flow Basis: Molar The composition option is selectedFeed Composition
Flow Rate (kgmole/h)
MethanolEthanol
diM-EtherH2O
71.217807e+03
0.04440.00410.78430.1673
Flow Basis: Molar The composition option is selectedFeed Flows
Flow Rate (kgmole/h)
Methanol (kgmole/h)Ethanol (kgmole/h)
diM-Ether (kgmole/h)H2O (kgmole/h)
71.217807e+03
54.06624.9657
955.0940203.6813
ProductsFlow Basis: Molar The composition option is selected
Product Compositions
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-100 (continued)
SUMMARY
Flow Rate (kgmole/h)
MethanolEthanol
diM-EtherH2O
8956.0302
0.00100.00000.99900.0000
9261.7770
0.20300.01890.00010.7780
Flow Basis: Molar The composition option is selectedProduct Flows
Flow Rate (kgmole/h)
Methanol (kgmole/h)Ethanol (kgmole/h)
diM-Ether (kgmole/h)H2O (kgmole/h)
8956.0302 *
0.9385 *
0.0100 *
955.0741 *
0.0075 *
9261.7770 *
53.1277 *
4.9557 *
0.0198 *
203.6738 *
Flow Basis: Molar The composition option is selectedProduct Recoveries
Flow Rate (kgmole/h)
Methanol (%)Ethanol (%)
diM-Ether (%)H2O (%)
8956.0302
1.73590.202399.99790.0037
9261.7770
98.264199.79770.002199.9963
COLUMN PROFILES
Reflux Ratio: 6.918 Reboil Ratio: 13.64 The Flows Option is Selected Flow Basis: MolarColumn Profiles Flows
Condenser1__Main TS2__Main TS3__Main TS4__Main TS5__Main TS6__Main TS7__Main TS
Reboiler
Temperature (F)110.0111.8139.9216.6258.8282.3291.8302.0320.5
Pressure (psia)139.0139.0142.3145.7149.0152.3155.7159.0159.0
Net Liq (lbmole/hr)66146086451138924206411240143833
Net Vap (lbmole/hr)
75707042546748483944385037523571
Net Feed (lbmole/hr)
1218
Net Draws (lbmole/hr)956.0
261.8Column Profiles Energy
Condenser1__Main TS2__Main TS3__Main TS4__Main TS5__Main TS6__Main TS7__Main TS
Reboiler
Temperature (F)110.0111.8139.9216.6258.8282.3291.8302.0320.5
Liquid Enthalpy (Btu/lbmole)-8.662e+004-8.699e+004-9.113e+004-9.695e+004-9.976e+004-1.017e+005-1.039e+005-1.077e+005-1.133e+005
Vapour Enthalpy (Btu/lbmole)-7.866e+004-7.864e+004-7.836e+004-7.929e+004-8.245e+004-8.576e+004-8.753e+004-8.945e+004-9.279e+004
Heat Loss (Btu/hr)
FEEDS / PRODUCTS
Flow Basis: Molar Stream Type Duty (kJ/h) State Flows (kgmole/h) Enthalpy (kJ/kgmole Temp (C)
CondenserQ48
EnergyDraw
6.041e+007 *
Liquid 956.0 * -8.662e+004 * 110.0 *
1__Main TS2__Main TS
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-100 (continued)
FEEDS / PRODUCTS
3__Main TS4__Main TS 7 Feed Mixed 1218 * -8.516e+004 * 192.2 *
5__Main TS6__Main TS7__Main TS
ReboilerQ59
EnergyDraw
5.166e+007 *
Liquid 261.8 * -1.133e+005 * 320.5 *
SETUP
Sub-FlowsheetFeed Streams
Internal Stream7
Q5
External Stream7
Q5
Transfer BasisP-H Flash
None Req'd
Product StreamsInternal Stream
Q489
External StreamQ489
Transfer BasisNone Req'dP-H FlashP-H Flash
VARIABLES
Column Flowsheet Vars Available as ParametersData Source Variable Component Description
COMPONENT MAPS
Feed StreamsFeed Name
7Q5
In to SubFlowSheet Out of SubFlowSheet
Product StreamProduct Name
Q489
In to SubFlowSheet Out of SubFlowSheet
DYNAMICS
Vessel Dynamic Specifications
VesselDiameter (ft)Height.0 (ft)Volume.0 (ft3)Liquid Volume Percent (%)Level CalculatorFraction CalculatorVessel Delta P (psi)Fixed Vessel P Spec (psia)Fixed P Spec Active
Reboiler @COL13.9145.87170.63 *
50.00Horizontal cylinder
Use levels and nozzles0.0000159.0
Not Active
Condenser @COL13.9145.87170.63 *
50.00Horizontal cylinder
Use levels and nozzles0.0000139.0
Not Active
Other Equipment in Column Flowsheet
Holdup Details
Condenser1__Main TS2__Main TS3__Main TS4__Main TS
Pressure (psia)
0.00000.00000.00000.00000.0000
Volume (ft3)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Bulk Liquid Volume (ft3)
0.00000.00000.00000.00000.0000
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-100 (continued)
5__Main TS6__Main TS7__Main TSReboiler
Pressure (psia)
0.00000.00000.00000.0000
Volume (ft3)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Bulk Liquid Volume (ft3)
0.00000.00000.00000.0000
NOTES
Distillation: T-101
CONNECTIONS
Inlet Stream
STREAM NAME Stage FROM UNIT OPERATION
Q710
Reboiler10__Main TS VLV-101Valve
Outlet Stream
STREAM NAME Stage TO UNIT OPERATION
Q6AGUA11
CondenserReboilerCondenser P-101Pump
MONITOR
Specifications SummarySpecified Value Current Value Wt. Error Wt. Tol. Abs. Tol. Active Estimate Used
Reflux Ratio 3.753e+007 1.000e-002 1.000e-002 Off On OffReflux Rate 2.094e+009 lbmole/hr 1.000e-002 2.205 lbmole/hr Off On OffComp Fraction 1.000e-003 * 3.738e-003 0.4221 1.000e-002 1.000e-003 Off On OffComp Fraction - 2 1.000e-003 * 1.220e-002 0.8845 1.000e-002 1.000e-003 Off On OffComp Recovery - 2 0.0010 * 0.0010 -1.613e-003 1.000e-002 1.000e-003 On On On
SPECS
Column Specification Parameters
Reflux Ratio
Fixed / Ranged: Fixed Primary / Alternate: Primary Lower Bound: Upper Bound:Stage: Condenser Flow Basis: Molar Liquid Specification: ---
Reflux Rate
Fixed / Ranged: Fixed Primary / Alternate: Primary Lower Bound: Upper Bound:Stage: Condenser Flow Basis: Molar Liquid Specification: ---
Comp Fraction
Fixed / Ranged: Fixed Primary / Alternate: Primary Lower Bound: Upper Bound:Stage: Condenser Flow Basis: Mole Fraction Phase: LiquidComponents: H2O
Comp Fraction - 2
Fixed / Ranged: Fixed Primary / Alternate: Primary Lower Bound: Upper Bound:Stage: Reboiler Flow Basis: Mole Fraction Phase: LiquidComponents: Methanol Ethanol diM-Ether
Comp Recovery - 2
Fixed / Ranged: Fixed Primary / Alternate: Primary Lower Bound: Upper Bound:Draw: 11 @COL2 Flow Basis: Molar
Components: H2O
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-101 (continued)Column Specification Parameters
Fixed / Ranged: Primary / Alternate: Lower Bound: Upper Bound:Draw: Flow Basis:
Components:
SUBCOOLING
Degrees of SubcoolingSubcool to
Condenser
User Variables
PROFILES
General ParametersSub-Flow Sheet: T-101 (COL2) Number of Stages: 15 *
Profile Estimates
Condenser1__Main TS2__Main TS3__Main TS4__Main TS5__Main TS6__Main TS7__Main TS8__Main TS9__Main TS
10__Main TS11__Main TS12__Main TS13__Main TS14__Main TS15__Main TS
Reboiler
Temperature (F)
92.7193.96102.6111.9121.1129.5136.6142.5147.5151.7155.5158.9162.2165.7170.4182.8203.0
Net Liquid (lbmole/hr)
2.094e+0092.071e+0092.063e+0092.045e+0092.025e+0092.009e+0091.998e+0091.992e+0091.989e+0091.989e+0091.989e+0091.989e+0091.987e+0091.979e+0091.950e+0091.912e+009
206.0
Net Vapour (lbmole/hr)
6.835e-0062.094e+0092.071e+0092.063e+0092.045e+0092.025e+0092.009e+0091.998e+0091.992e+0091.989e+0091.989e+0091.989e+0091.989e+0091.987e+0091.979e+0091.950e+0091.912e+009
EFFICIENCIES
Stage EfficienciesStages
Condenser1__Main TS2__Main TS3__Main TS4__Main TS5__Main TS6__Main TS7__Main TS8__Main TS9__Main TS10__Main TS11__Main TS12__Main TS13__Main TS14__Main TS15__Main TSReboiler
Overall Efficiency1.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.000
Methanol1.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.000
Ethanol1.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.000
diM-Ether1.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.000
H2O1.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.0001.000
SOLVER
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-101 (continued)Column Solving Algorithm: HYSIM Inside-Out
Solving OptionsMaximum Iterations: 10000Equilibrium Error Tolerance: 1.000e-05Heat/Spec Error Tolerance: 5.000e-004Save Solutions as Initial Estimate: OnSuper Critical Handling Model: Simple KTrace Level: LowInit from Ideal K's: Off
Initial Estimate Generator ParametersIterative IEG (Good for Chemicals): Off
Acceleration ParametersAccelerate K Value & H Model Parameters: Off
Damping ParametersAzeotrope Check: OffFixed Damping Factor: 1
SIDE STRIPPERS
SIDE RECTIFIERS
PUMP AROUNDS
VAP BYPASSES
RATING
Tray Sections
Tray SectionTray Diameter (ft)Weir Height (ft)Weir Length (ft)Tray Space (ft)Tray Volume (ft3)Disable Heat Loss CalculationsHeat ModelRating CalculationsTray Hold Up (ft3)
Main TS @COL24.9210.1640 *
3.937 *
1.804 *
34.32No
NoneNo
3.120
Vessels
VesselDiameter (ft)Length (ft)Volume (ft3)OrientationVessel has a BootBoot Diameter (ft)Boot Length (ft)Hold Up (ft3)
Reboiler @COL23.9145.87170.63 *
HorizontalNo
35.31
Condenser @COL23.9145.87170.63 *
HorizontalNo
35.31
Other Equipment In Column Flowsheet
Pressure Profile
Pressure (psia) Pressure Drop (psi)Condenser1__Main TS2__Main TS3__Main TS4__Main TS5__Main TS6__Main TS7__Main TS
3.755 psia *
3.755 psia4.469 psia5.184 psia5.898 psia6.612 psia7.327 psia8.041 psia
0.0000 psi0.7143 psi0.7143 psi0.7143 psi0.7143 psi0.7143 psi0.7143 psi0.7143 psi
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-101 (continued)8__Main TS9__Main TS10__Main TS11__Main TS12__Main TS13__Main TS14__Main TS15__Main TS
Reboiler
8.755 psia9.470 psia10.18 psia10.90 psia11.61 psia12.33 psia13.04 psia13.76 psia13.76 psia *
0.7143 psi0.7143 psi0.7143 psi0.7143 psi0.7143 psi0.7143 psi0.7143 psi
0.0000 psi
Pressure Solving Options
Pressure Tolerance 1.000e-004 Pressure Drop Tolerance 1.000e-004 Damping Factor 1.000 Max Press Iterations 100
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
100.2755
93.08521.4504 *
261.77705600.7367417.9672
-1.133e+00514.39
-2.9664e+07
110.0000
92.71013.7550
55.79821820.3521156.5898
-1.033e+00510.15
-5.7647e+06
AGUA0.0000
202.963613.7554
205.97883780.3844261.3774
-1.201e+0055.664
-2.4745e+07
Q7
3.4021e+13
Q6
3.4017e+13
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass 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)
(psia)
(Btu/lbmole)(cSt)
(lb/ft3)(barrel/day)
(ft3/lbmole)(Btu/lb)
1021.40
8.875e-0041.899e-0021.261e+006
-52960.672416.65
0.77806.577e+004
30740.35950.33430.00000.0000
2.67716.652.38057.287.783
10.64
0.00001.1351.034
1.854e+004
58.35410.3
0.72451127866.8
1132.621.49048.61160.1-3167
0.311228.15
0.86302.849e+005
8734
2.122e-3140.00000.0000
1.52328.15
0.507249.694.669
4.251e-00410.63
0.00001.0761.339
1.624e+0040.641149.83156.21.000
0.6711497.9
AGUA18.353.22459.17273.1-6546
0.308618.31
0.99796405349.0
0.00000.00000.0000
3.36918.311.87261.837.965
6.000e-00410.76
0.00001.1221.182
1.759e+0040.316063.12256.01.000
0.3102958.6
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-101 (continued)
PROPERTIES
NamePhase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)(psia)
(barrel/day)
100.275565.90
14.660.685216.10
0.7524
4.4812.329411.0
110.000028.05
0.10170.499226.17
0.802121.02
0.6444
4.570156.2
-1.755
AGUA0.000059.02
0.38700.299616.33
0.889715.49
0.8442
1.102256.0
-2.518
SUMMARY
Flow Basis: Molar The composition option is selectedFeed Composition
Flow Rate (kgmole/h)
MethanolEthanol
diM-EtherH2O
10261.7770
0.20300.01890.00010.7780
Flow Basis: Molar The composition option is selectedFeed Flows
Flow Rate (kgmole/h)
Methanol (kgmole/h)Ethanol (kgmole/h)
diM-Ether (kgmole/h)H2O (kgmole/h)
10261.7770
53.12774.95570.0198
203.6738Products
Flow Basis: Molar The composition option is selectedProduct Compositions
Flow Rate (kgmole/h)
MethanolEthanol
diM-EtherH2O
1155.7982
0.95100.04490.00040.0037
AGUA205.9788
0.00030.01190.00000.9878
Flow Basis: Molar The composition option is selectedProduct Flows
Flow Rate (kgmole/h)
Methanol (kgmole/h)Ethanol (kgmole/h)
diM-Ether (kgmole/h)H2O (kgmole/h)
1155.7982 *
53.0662 *
2.5036 *
0.0198 *
0.2086 *
AGUA205.9788 *
0.0615 *
2.4521 *
0.0000 *
203.4652 *
Flow Basis: Molar The composition option is selectedProduct Recoveries
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-101 (continued)
SUMMARY
Flow Rate (kgmole/h)
Methanol (%)Ethanol (%)
diM-Ether (%)H2O (%)
1155.7982
99.884350.519199.99980.1024
AGUA205.9788
0.115749.48090.000099.8976
COLUMN PROFILES
Reflux Ratio: 3.753e+007 Reboil Ratio: 9.283e+006 The Flows Option is Selected Flow Basis: MolarColumn Profiles Flows
Condenser1__Main TS2__Main TS3__Main TS4__Main TS5__Main TS6__Main TS7__Main TS8__Main TS9__Main TS10__Main TS11__Main TS12__Main TS13__Main TS14__Main TS15__Main TS
Reboiler
Temperature (F)92.7193.96102.6111.9121.1129.5136.6142.5147.5151.7155.5158.9162.2165.7170.4182.8203.0
Pressure (psia)3.7553.7554.4695.1845.8986.6127.3278.0418.7559.47010.1810.9011.6112.3313.0413.7613.76
Net Liq (lbmole/hr)2.094e+0092.071e+0092.063e+0092.045e+0092.025e+0092.009e+0091.998e+0091.992e+0091.989e+0091.989e+0091.989e+0091.989e+0091.987e+0091.979e+0091.950e+0091.912e+009
Net Vap (lbmole/hr)
2.094e+0092.071e+0092.063e+0092.045e+0092.025e+0092.009e+0091.998e+0091.992e+0091.989e+0091.989e+0091.989e+0091.989e+0091.987e+0091.979e+0091.950e+0091.912e+009
Net Feed (lbmole/hr)
261.8
Net Draws (lbmole/hr)55.80
206.0Column Profiles Energy
Condenser1__Main TS2__Main TS3__Main TS4__Main TS5__Main TS6__Main TS7__Main TS8__Main TS9__Main TS10__Main TS11__Main TS12__Main TS13__Main TS14__Main TS15__Main TS
Reboiler
Temperature (F)92.7193.96102.6111.9121.1129.5136.6142.5147.5151.7155.5158.9162.2165.7170.4182.8203.0
Liquid Enthalpy (Btu/lbmole)-1.033e+005-1.042e+005-1.056e+005-1.077e+005-1.101e+005-1.122e+005-1.139e+005-1.151e+005-1.159e+005-1.164e+005-1.168e+005-1.171e+005-1.173e+005-1.177e+005-1.185e+005-1.199e+005-1.201e+005
Vapour Enthalpy (Btu/lbmole)-8.667e+004-8.707e+004-8.776e+004-8.911e+004-9.109e+004-9.330e+004-9.530e+004-9.687e+004-9.799e+004-9.877e+004-9.930e+004-9.966e+004-9.994e+004-1.002e+005-1.005e+005-1.010e+005-1.021e+005
Heat Loss (Btu/hr)
FEEDS / PRODUCTS
Flow Basis: Molar Stream Type Duty (kJ/h) State Flows (kgmole/h) Enthalpy (kJ/kgmole Temp (C)
CondenserQ611
EnergyDraw
3.402e+013 *
Liquid 55.80 * -1.033e+005 * 92.71 *
1__Main TS2__Main TS3__Main TS4__Main TS
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-101 (continued)
FEEDS / PRODUCTS
5__Main TS6__Main TS7__Main TS8__Main TS9__Main TS10__Main TS 10 Feed Mixed 261.8 * -1.133e+005 * 93.09 *
11__Main TS12__Main TS13__Main TS14__Main TS15__Main TS
ReboilerQ7AGUA
EnergyDraw
3.402e+013 *
Liquid 206.0 * -1.201e+005 * 203.0 *
SETUP
Sub-FlowsheetFeed Streams
Internal StreamQ710
External StreamQ710
Transfer BasisNone Req'dP-H Flash
Product StreamsInternal Stream
Q6AGUA
11
External StreamQ6
AGUA11
Transfer BasisNone Req'dP-H FlashP-H Flash
VARIABLES
Column Flowsheet Vars Available as ParametersData Source Variable Component Description
COMPONENT MAPS
Feed StreamsFeed Name
Q710
In to SubFlowSheet Out of SubFlowSheet
Product StreamProduct Name
Q6AGUA11
In to SubFlowSheet Out of SubFlowSheet
DYNAMICS
Vessel Dynamic Specifications
VesselDiameter (ft)Height.0 (ft)Volume.0 (ft3)Liquid Volume Percent (%)Level CalculatorFraction CalculatorVessel Delta P (psi)Fixed Vessel P Spec (psia)Fixed P Spec Active
Reboiler @COL23.9145.87170.63 *
50.00Horizontal cylinder
Use levels and nozzles0.000013.76
Not Active
Condenser @COL23.9145.87170.63 *
50.00Horizontal cylinder
Use levels and nozzles0.00003.755
Not Active
Other Equipment in Column Flowsheet
Holdup Details
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Distillation: T-101 (continued)
Condenser1__Main TS2__Main TS3__Main TS4__Main TS5__Main TS6__Main TS7__Main TS8__Main TS9__Main TS10__Main TS11__Main TS12__Main TS13__Main TS14__Main TS15__Main TSReboiler
Pressure (psia)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Volume (ft3)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Bulk Liquid Volume (ft3)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
NOTES
Valve: VLV-100
CONNECTIONS
Inlet Stream
STREAM NAME FROM UNIT OPERATION
5 ERV-100Equilibrium Reactor
Outlet Stream
STREAM NAME TO UNIT OPERATION
6 E-101Cooler
PARAMETERS
Physical Properties
Pressure Drop: 7.252 psi
User Variables
RATING
Sizing
Sizing ConditionsInlet Pressure 152.3 psia Molecular Weight 40.75 CurrentValve Opening 50.00 % * Delta P 7.252 psi Flow Rate 4.963e+004 lb/hr
Valve Manufacturer and Valve TypeManufacturer: Universal Gas Sizing Type: ---
Valve Operating Characteristic and Sizing MethodLinear Sizing Method: Cg
C1 25.00 Km 0.9000 Cv 903e+004 USGPM Cg 1.476e+006
Nozzle Parameters
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)
50.16400.0000
60.16400.0000
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Valve: VLV-100 (continued)Elevation (Ground) (ft)Elevation (% of Height) (%)
0.0000 0.0000
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
51.0000
248.0000 *
152.28961217.8072
49630.71684915.2307
-8.105e+00444.88
-9.8701e+07
61.0000
247.9137145.0377 *
1217.807249630.71684915.2307
-8.105e+00444.98
-9.8701e+07
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)
(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)
(psia)
(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)
540.75
2.005e-0020.8173
2.596e+005-19891.10117.07
0.41904.623e+0051.134e+004
4.941e-3240.00000.0000
10121.05917.0711.0743.16
0.0000
11.37
0.00001.1321.132
1.161e+0040.887140.985177
0.000049.87284.9
1.0000
1.477e-0021.161e-002
15.090.370215.09
0.3702
640.75
1.910e-0020.7784
2.725e+005-19891.10417.06
0.41864.623e+0051.134e+004
4.941e-3240.00000.0000
10631.05917.0611.0743.16
1.00011.37
0.00001.1321.132
1.166e+0040.929740.985177
0.000052.35286.2
1.0000
1.474e-0021.159e-002
15.070.369815.07
0.3698
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Valve: VLV-100 (continued)
PROPERTIES
NameCp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(psia)(psia)
(barrel/day)
5
113.194.985177
6
113.194.985177
DYNAMICS
Dynamic Specifications
Total Delta P (psi)Pressure Flow Relation
7.252 Not ActiveActive
Dynamic Parameters
Valve Opening (%)Conductance (USGPM)
50.00 *
5.903e+004Mass Flow (lb/hr)Friction Delta P (psi)
4.963e+0047.252
Pipe Model Parameters
MaterialRoughness (ft)Pipe Length (ft)Feed Diameter (ft)
Cast Iron8.497e-004
0.0000 *
0.1640
Darcy Friction FactorPipe k (lb/hr/sqrt(psia-lb/ft3))Velocity (ft/s)Reynolds Number
0.0000 *
798.2 *
1.371e+007 *
Hold-Up Volume: 0.0000 ft3 *
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)
0.0000 *
0.0000 *
0.0000 *
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
Actuator Parameters
Parameters Mode: Instantaneous
Actuator Time Constant (seconds)Valve Stickiness Time Constant (seconds)
1.000 * Actuator Linear Rate 1.000e-002 *
Activator Position
Fail Position: None
Min (%)
Max (%)
Current (%)
Desired (%)
Offset (%)
ValveActuator
0.00 *
0.00 *
100.00 *
100.00 *
50.00 *
50.00 * 50.00 *
0.00 *
Valve: VLV-101
CONNECTIONS
Inlet Stream
STREAM NAME FROM UNIT OPERATION
9 T-100Distillation
Outlet Stream
STREAM NAME TO UNIT OPERATION
10 T-101Distillation
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Valve: VLV-101 (continued)
PARAMETERS
Physical Properties
Pressure Drop: 157.5 psi
User Variables
RATING
Sizing
Sizing ConditionsInlet Pressure 159.0 psia Molecular Weight 21.40 CurrentValve Opening 50.00 % * Delta P 157.5 psi Flow Rate 5601 lb/hr
Valve Manufacturer and Valve TypeManufacturer: Universal Gas Sizing Type: ---
Valve Operating Characteristic and Sizing MethodLinear Sizing Method: Cv (standard) cal/min.sqrt(psi)
C1 25.00 Km 0.9000 Cv Cg
Nozzle Parameters
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)Elevation (% of Height) (%)
90.16400.00000.0000
100.16400.00000.0000
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
90.0000
320.5048159.0000261.7770
5600.7367417.9672
-1.133e+00515.54
-2.9664e+07
100.2755
93.08521.4504 *
261.77705600.7367417.9672
-1.133e+00514.39
-2.9664e+07
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas 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)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)
921.402.33249.89479.9-5296
0.726222.691.061
6.577e+0043074
0.00000.00000.0000
2.67722.692.380
1021.40
8.875e-0041.899e-0021.261e+006
-52960.672416.65
0.77806.577e+004
30740.35950.33430.00000.0000
2.67716.652.380
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Valve: VLV-101 (continued)
PROPERTIES
NameStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(lb/ft3)(USGPM)
(psia)
(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)
(psia)(psia)
(barrel/day)
957.2814.00
8.144e-00310.64
0.00001.0961.213
1.539e+0040.168258.35410.31.000
0.4288719.1
0.000038.26
0.28990.134420.70
0.967718.70
0.8741
4.4812.329410.3
1057.287.783
10.64
0.00001.1351.034
1.854e+004
58.35410.3
0.72451127866.8
0.275565.90
14.660.685216.10
0.7524
4.4812.329411.0
DYNAMICS
Dynamic Specifications
Total Delta P (psi)Pressure Flow Relation
157.5 Not ActiveActive
Dynamic Parameters
Valve Opening (%)Conductance (USGPM)
50.00 * Mass Flow (lb/hr)Friction Delta P (psi)
5601157.5
Pipe Model Parameters
MaterialRoughness (ft)Pipe Length (ft)Feed Diameter (ft)
Cast Iron8.497e-004
0.0000 *
0.1640
Darcy Friction FactorPipe k (lb/hr/sqrt(psia-lb/ft3))Velocity (ft/s)Reynolds Number
0.0000 *
1.475 *
1.337e+005 *
Hold-Up Volume: 0.0000 ft3 *
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)
0.0000 *
0.0000 *
0.0000 *
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
Actuator Parameters
Parameters Mode: InstantaneousHyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 73 of 76
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Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Valve: VLV-101 (continued)Parameters Mode: Instantaneous
Actuator Time Constant (seconds)Valve Stickiness Time Constant (seconds)
1.000 * Actuator Linear Rate 1.000e-002 *
Activator Position
Fail Position: None
Min (%)
Max (%)
Current (%)
Desired (%)
Offset (%)
ValveActuator
0.00 *
0.00 *
100.00 *
100.00 *
50.00 *
50.00 * 50.00 *
0.00 *
Valve: VLV-102
CONNECTIONS
Inlet Stream
STREAM NAME FROM UNIT OPERATION
8 T-100Distillation
Outlet Stream
STREAM NAME TO UNIT OPERATION
DME
PARAMETERS
Physical Properties
Pressure Drop: 7.252 psi *
User Variables
RATING
Sizing
Sizing ConditionsInlet Pressure 139.0 psia Molecular Weight 46.06 CurrentValve Opening 50.00 % * Delta P 7.252 psi * Flow Rate 4.403e+004 lb/hr
Valve Manufacturer and Valve TypeManufacturer: Universal Gas Sizing Type: ---
Valve Operating Characteristic and Sizing MethodLinear Sizing Method: Cv (standard) cal/min.sqrt(psi)
C1 25.00 Km 0.9000 Cv 84.16 USGPM Cg 2104
Nozzle Parameters
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)Elevation (% of Height) (%)
80.16400.00000.0000
DME0.16400.00000.0000
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)
80.0000
110.0070139.0000956.0302
44029.9802
DME0.0133
106.2195131.7481956.0302
44029.9802
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Valve: VLV-102 (continued)
CONDITIONS
Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
4497.2635-8.662e+004
37.85-8.2809e+07
4497.2635-8.662e+004
37.54-8.2809e+07
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(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)
(psia)
(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)
(psia)(psia)
(barrel/day)
846.06
0.779935.925240
-18810.821928.21
0.61265.708e+0051.239e+004
2.122e-3140.00000.0000
0.908728.218.69041.85152.8
2.915e-00211.38
0.00001.0761.0767981
0.131238.5848781.0001.282173.3
0.00009.257
7.011e-0027.548e-002
26.230.569526.23
0.5695
120.4120.74878
DME46.06
0.534124.607651
-18810.815127.86
0.60505.708e+0051.239e+0041.334e-0021.334e-002
0.00000.0000
0.908727.868.69041.85149.9
11.38
0.00001.0771.0078026
38.584878
0.98671.872174.3
0.01339.542
25.880.561927.66
0.6006
120.4120.74878
DYNAMICS
Dynamic SpecificationsHyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 75 of 76
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LEGENDSBurlington, MAUSA
Case Name: DFP FINAL.HSC
Unit Set: Field
Date/Time: Wed Mar 21 00:56:33 2012
Valve: VLV-102 (continued)Dynamic Specifications
Total Delta P (psi)Pressure Flow Relation
7.252 * Not ActiveActive
Dynamic Parameters
Valve Opening (%)Conductance (USGPM)
50.00 *
84.16Mass Flow (lb/hr)Friction Delta P (psi)
4.403e+0047.252
Pipe Model Parameters
MaterialRoughness (ft)Pipe Length (ft)Feed Diameter (ft)
Cast Iron8.497e-004
0.0000 *
0.1640
Darcy Friction FactorPipe k (lb/hr/sqrt(psia-lb/ft3))Velocity (ft/s)Reynolds Number
0.0000 *
16.11 *
1.872e+006 *
Hold-Up Volume: 0.0000 ft3 *
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)
0.0000 *
0.0000 *
0.0000 *
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
Actuator Parameters
Parameters Mode: Instantaneous
Actuator Time Constant (seconds)Valve Stickiness Time Constant (seconds)
1.000 * Actuator Linear Rate 1.000e-002 *
Activator Position
Fail Position: None
Min (%)
Max (%)
Current (%)
Desired (%)
Offset (%)
ValveActuator
0.00 *
0.00 *
100.00 *
100.00 *
50.00 *
50.00 * 50.00 *
0.00 *
Equilibrium: Rxn-2
STOICHIOMETRY
ComponentMethanoldiM-Ether
H2O
Molecular Weight32.0446.0718.02
Stoichiometric Coefficient-2 *
1 *
1 *
Balance Error : 0.0000 Reaction Heat (25 C) : -5035 Btu/lbmole
BASIS
Basis PhaseApproach
(F)Min. Temp
(F)Max. Temp
(F)
Activity VapourPhase -459.7 5432
PARAMETERS
Source : Gibbs Free Energy
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 76 of 76
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