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LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 Fluid Package: Basis-1Property Package: Peng-RobinsonCONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psig)Molar Flow (MMSCFD)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)Liq Vol Flow @Std Cond (barrel/day)
Overall1.0000
106.168.004.923
1.248e+0042263
-4.144e+00442.37
-2.240e+0078.711e+005 *
Vapour Phase1.0000
106.168.004.923
1.248e+0042263
-4.144e+00442.37
-2.240e+0078.711e+005
Liquid Phase0.0000
106.168.00
0.00000.00000.0000
-1.943e+00579.31
0.00000.0000
Aqueous Phase0.0000
106.168.00
0.00000.00000.0000
-1.225e+00513.81
0.00000.0000
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLHV Molar Basis (Std)HHV Molar Basis (Std)HHV Mass Basis (Std)CO2 LoadingCO2 App ML ConCO2 App WT ConLHV Mass Basis (Std)Phase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Phase Fraction [Act. Vol. 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)Cv
(lbmole/ft3)(lb/ft3)
(barrel/day)(Btu/lb)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole)(Btu/lbmole)
(Btu/lb)
(lbmole/ft3)(lbmol/lb)
(Btu/lb)
(psig)(Cost/s)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(API_60)
(barrel/day)
(psig)
(Btu/lbmole)(cSt)
(API_60)(barrel/day)
(ft3/lbmole)(Btu/lb)
(dyne/cm)(Btu/hr-ft-F)
(cP)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
Overall23.09
1.390e-0020.3211
1.662e+005-17941.83410.97
0.4751---------------------
1.0001.0001.000
-11.130.0000
648.11.02110.974.923242.4
0.0000---
16.91---
-14.701.2211.2467805
2.2781.438e+0058.711e+005
0.000071.93338.0
1.0000---
1.789e-0021.172e-002
8.9870.3892
8.809
Vapour Phase23.09
1.390e-0020.3211
1.662e+005-17941.83410.97
0.4751---------------------
1.0001.0001.000
---0.0000
648.11.02110.974.923242.4
---0.9797
16.91------
1.2211.246
---2.278
1.438e+0058.711e+005
0.000071.93
---1.0000
---1.789e-0021.172e-002
8.9870.3892
8.809
Liquid Phase211.5
0.244851.79
0.0000-918.30.3749
98.250.4644
------------------------
0.00000.0000
---0.0000
---0.2491
98.250.0000
35.82---
5.563e-00211.74
------
1.0211.159
---6.02534.79
0.00001.0004.084
---0.0000
23.076.685e-002
4.99996.26
0.455184.78
Aqueous Phase18.023.44862.13
0.0000-6800
0.766418.571.031
2.078e-0021.763e+004
978.5---------
1.153e-003---
0.00000.0000
---0.0000
---3.45818.57
0.000010.01
0.00003.950e-003
8.523------
1.1201.156
---0.6402
7.6500.0000
1.0000.2900
---0.0000
69.280.36570.6371
16.580.9204
16.06Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 1 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonPROPERTIES
Mass 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 IndexMass Exergy
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)
(psig)(psig)
(barrel/day)
(Btu/lb)
Overall0.3814
------------
27108.711e+005
-15.1479.18
Vapour Phase0.3814
------------
27108.711e+005
------
Liquid Phase0.4008
91.980.4348
1.0680.6418
65.570.0000
------
Aqueous Phase0.8915
16.160.8970
1.149---
-10.060.0000
------
COMPOSITIONOverall Phase Vapour Fraction 1.0000
COMPONENTS
NitrogenMethaneCO2EthanePropanei-Butanen-Butanei-Pentanen-Pentanen-Hexanen-Heptanen-Octanen-Nonanen-Decanen-C11H2SH2OSEF-10*NBP[0]80*NBP[0]110*NBP[0]135*NBP[0]159*NBP[0]186*NBP[0]215*NBP[0]233*NBP[0]263*NBP[0]286*NBP[0]310*NBP[0]336*NBP[0]360*NBP[0]386*NBP[0]411*NBP[0]437*NBP[0]461*NBP[0]487*NBP[0]511*NBP[0]536*NBP[0]562*NBP[0]587*NBP[0]612*NBP[0]637*NBP[0]662*NBP[0]687*NBP[0]713*
MOLAR FLOW (MMSCFD)
0.01663.55970.21230.51120.29880.07270.09200.02850.01990.01320.00700.00250.00050.00010.00000.00000.06870.00000.00460.00190.00200.00160.00140.00190.00230.00120.00120.00070.00040.00020.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00340.72300.04310.10380.06070.01480.01870.00580.00400.00270.00140.00050.00010.00000.00000.00000.01390.00000.00090.00040.00040.00030.00030.00040.00050.00020.00020.00010.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
50.98566270.67281025.83851687.99001446.8370
463.8848587.3719225.6301157.4906125.2290
76.743831.7293
6.77461.18380.00110.0182
135.85310.0000
33.084914.445316.419513.963113.443020.406526.423314.979015.4663
9.19066.40173.01721.47910.85320.52610.25270.11800.06500.02630.01150.00550.00220.00080.00030.00010.0000
MASS FRACTION
0.00410.50230.08220.13520.11590.03720.04700.01810.01260.01000.00610.00250.00050.00010.00000.00000.01090.00000.00270.00120.00130.00110.00110.00160.00210.00120.00120.00070.00050.00020.00010.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
4.32941434.1326
85.1073324.9563195.5266
56.522168.959924.781017.124512.9399
7.65113.08000.64410.11060.00010.00169.32100.00003.32061.43221.60241.34431.27671.90222.43561.36351.39420.82050.56480.26370.12800.07310.04460.02120.00980.00540.00220.00090.00040.00020.00010.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00190.63370.03760.14360.08640.02500.03050.01090.00760.00570.00340.00140.00030.00000.00000.00000.00410.00000.00150.00060.00070.00060.00060.00080.00110.00060.00060.00040.00020.00010.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 2 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000COMPONENTS
NBP[0]738*NBP[0]763*NBP[0]788*NBP[0]825*NBP[0]874*NBP[0]924*NBP[0]975*NBP[0]1025*NBP[0]1076*NBP[0]1125*NBP[0]1173*NBP[0]1250*NBP[0]1363*NBP[0]1466*NBP[0]1587*NBP[0]1697*NBP[1]107*NBP[1]133*NBP[1]158*NBP[1]184*NBP[1]210*NBP[1]236*NBP[1]260*NBP[1]285*NBP[1]310*NBP[1]335*NBP[1]360*NBP[1]385*NBP[1]411*NBP[1]436*NBP[1]461*NBP[1]487*NBP[1]511*NBP[1]536*NBP[1]562*NBP[1]587*NBP[1]612*NBP[1]637*NBP[1]662*NBP[1]687*NBP[1]712*NBP[1]738*NBP[1]763*NBP[1]788*NBP[1]825*NBP[1]874*NBP[1]925*NBP[1]975*NBP[1]1025*NBP[1]1075*NBP[1]1125*NBP[1]1174*NBP[1]1252*NBP[2]93*NBP[2]125*NBP[2]151*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 3 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000COMPONENTS
NBP[2]173*NBP[2]206*NBP[2]228*NBP[2]250*NBP[2]280*NBP[2]304*NBP[2]328*NBP[2]352*NBP[2]380*NBP[2]405*NBP[2]430*NBP[2]454*NBP[2]480*NBP[2]506*NBP[2]532*NBP[2]558*NBP[2]583*NBP[2]609*NBP[2]634*NBP[2]660*NBP[2]686*NBP[2]711*NBP[2]736*NBP[2]762*NBP[2]788*NBP[2]821*NBP[2]869*NBP[2]926*NBP[2]985*NBP[2]1035*NBP[2]1079*NBP[2]1131*NBP[2]1187*NBP[2]1264*NBP[2]1361*NBP[2]1456*NBP[2]1559*NBP[3]98*NBP[3]129*NBP[3]153*NBP[3]179*NBP[3]212*NBP[3]228*NBP[3]255*NBP[3]281*NBP[3]306*NBP[3]331*NBP[3]356*NBP[3]382*NBP[3]407*NBP[3]433*NBP[3]459*NBP[3]483*NBP[3]509*NBP[3]533*NBP[3]561*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 4 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000COMPONENTS
NBP[3]585*NBP[3]610*NBP[3]636*NBP[3]661*NBP[3]687*NBP[3]712*NBP[3]737*NBP[3]763*NBP[3]789*NBP[3]824*NBP[3]872*NBP[3]922*NBP[3]973*NBP[3]1023*NBP[3]1073*NBP[3]1123*NBP[8]110*NBP[8]136*NBP[8]162*NBP[8]189*NBP[8]217*NBP[8]239*NBP[8]267*NBP[8]292*NBP[8]318*NBP[8]344*NBP[8]370*NBP[8]397*NBP[8]423*NBP[8]449*NBP[8]475*NBP[8]501*NBP[8]527*NBP[8]554*NBP[8]579*NBP[8]605*NBP[8]631*NBP[8]657*NBP[8]683*NBP[8]709*NBP[8]735*NBP[8]762*NBP[8]788*NBP[8]825*NBP[8]874*NBP[8]925*NBP[8]975*NBP[8]1025*NBP[8]1075*NBP[8]1125*NBP[8]1174*NBP[8]1240*NBP[8]1332*NBP[8]1433*NBP[8]1531*NBP[9]96*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 5 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000COMPONENTS
NBP[9]125*NBP[9]149*NBP[9]176*NBP[9]205*NBP[9]226*NBP[9]253*NBP[9]278*NBP[9]304*NBP[9]329*NBP[9]354*NBP[9]380*NBP[9]406*NBP[9]431*NBP[9]457*NBP[9]482*NBP[9]507*NBP[9]533*NBP[9]559*NBP[9]584*NBP[9]609*NBP[9]635*NBP[9]661*NBP[9]686*NBP[9]711*NBP[9]737*NBP[9]763*NBP[9]788*NBP[9]825*NBP[9]875*NBP[9]927*NBP[9]978*NBP[9]1029*NBP[9]1079*NBP[9]1132*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Total 4.9232 1.0000 12484.8155 1.0000 2263.1948 1.0000Vapour Phase Phase Fraction 1.000
COMPONENTS
NitrogenMethaneCO2EthanePropanei-Butanen-Butanei-Pentanen-Pentanen-Hexanen-Heptanen-Octanen-Nonanen-Decanen-C11H2SH2O
MOLAR FLOW (MMSCFD)
0.01663.55970.21230.51120.29880.07270.09200.02850.01990.01320.00700.00250.00050.00010.00000.00000.0687
MOLE FRACTION
0.00340.72300.04310.10380.06070.01480.01870.00580.00400.00270.00140.00050.00010.00000.00000.00000.0139
MASS FLOW (lb/hr)
50.98566270.67281025.83851687.99001446.8370
463.8848587.3719225.6301157.4906125.2290
76.743831.7293
6.77461.18380.00110.0182
135.8531
MASS FRACTION
0.00410.50230.08220.13520.11590.03720.04700.01810.01260.01000.00610.00250.00050.00010.00000.00000.0109
LIQUID VOLUMEFLOW (barrel/day)
4.32941434.1326
85.1073324.9563195.5266
56.522168.959924.781017.124512.9399
7.65113.08000.64410.11060.00010.00169.3210
LIQUID VOLUMEFRACTION
0.00190.63370.03760.14360.08640.02500.03050.01090.00760.00570.00340.00140.00030.00000.00000.00000.0041
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 6 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Vapour Phase (continued) Phase Fraction 1.000COMPONENTS
SEF-10*NBP[0]80*NBP[0]110*NBP[0]135*NBP[0]159*NBP[0]186*NBP[0]215*NBP[0]233*NBP[0]263*NBP[0]286*NBP[0]310*NBP[0]336*NBP[0]360*NBP[0]386*NBP[0]411*NBP[0]437*NBP[0]461*NBP[0]487*NBP[0]511*NBP[0]536*NBP[0]562*NBP[0]587*NBP[0]612*NBP[0]637*NBP[0]662*NBP[0]687*NBP[0]713*NBP[0]738*NBP[0]763*NBP[0]788*NBP[0]825*NBP[0]874*NBP[0]924*NBP[0]975*NBP[0]1025*NBP[0]1076*NBP[0]1125*NBP[0]1173*NBP[0]1250*NBP[0]1363*NBP[0]1466*NBP[0]1587*NBP[0]1697*NBP[1]107*NBP[1]133*NBP[1]158*NBP[1]184*NBP[1]210*NBP[1]236*NBP[1]260*NBP[1]285*NBP[1]310*NBP[1]335*NBP[1]360*NBP[1]385*NBP[1]411*
MOLAR FLOW (MMSCFD)
0.00000.00460.00190.00200.00160.00140.00190.00230.00120.00120.00070.00040.00020.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00090.00040.00040.00030.00030.00040.00050.00020.00020.00010.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.000033.084914.445316.419513.963113.443020.406526.423314.979015.4663
9.19066.40173.01721.47910.85320.52610.25270.11800.06500.02630.01150.00550.00220.00080.00030.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00270.00120.00130.00110.00110.00160.00210.00120.00120.00070.00050.00020.00010.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00003.32061.43221.60241.34431.27671.90222.43561.36351.39420.82050.56480.26370.12800.07310.04460.02120.00980.00540.00220.00090.00040.00020.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00150.00060.00070.00060.00060.00080.00110.00060.00060.00040.00020.00010.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 7 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Vapour Phase (continued) Phase Fraction 1.000COMPONENTS
NBP[1]436*NBP[1]461*NBP[1]487*NBP[1]511*NBP[1]536*NBP[1]562*NBP[1]587*NBP[1]612*NBP[1]637*NBP[1]662*NBP[1]687*NBP[1]712*NBP[1]738*NBP[1]763*NBP[1]788*NBP[1]825*NBP[1]874*NBP[1]925*NBP[1]975*NBP[1]1025*NBP[1]1075*NBP[1]1125*NBP[1]1174*NBP[1]1252*NBP[2]93*NBP[2]125*NBP[2]151*NBP[2]173*NBP[2]206*NBP[2]228*NBP[2]250*NBP[2]280*NBP[2]304*NBP[2]328*NBP[2]352*NBP[2]380*NBP[2]405*NBP[2]430*NBP[2]454*NBP[2]480*NBP[2]506*NBP[2]532*NBP[2]558*NBP[2]583*NBP[2]609*NBP[2]634*NBP[2]660*NBP[2]686*NBP[2]711*NBP[2]736*NBP[2]762*NBP[2]788*NBP[2]821*NBP[2]869*NBP[2]926*NBP[2]985*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 8 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Vapour Phase (continued) Phase Fraction 1.000COMPONENTS
NBP[2]1035*NBP[2]1079*NBP[2]1131*NBP[2]1187*NBP[2]1264*NBP[2]1361*NBP[2]1456*NBP[2]1559*NBP[3]98*NBP[3]129*NBP[3]153*NBP[3]179*NBP[3]212*NBP[3]228*NBP[3]255*NBP[3]281*NBP[3]306*NBP[3]331*NBP[3]356*NBP[3]382*NBP[3]407*NBP[3]433*NBP[3]459*NBP[3]483*NBP[3]509*NBP[3]533*NBP[3]561*NBP[3]585*NBP[3]610*NBP[3]636*NBP[3]661*NBP[3]687*NBP[3]712*NBP[3]737*NBP[3]763*NBP[3]789*NBP[3]824*NBP[3]872*NBP[3]922*NBP[3]973*NBP[3]1023*NBP[3]1073*NBP[3]1123*NBP[8]110*NBP[8]136*NBP[8]162*NBP[8]189*NBP[8]217*NBP[8]239*NBP[8]267*NBP[8]292*NBP[8]318*NBP[8]344*NBP[8]370*NBP[8]397*NBP[8]423*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 9 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Vapour Phase (continued) Phase Fraction 1.000COMPONENTS
NBP[8]449*NBP[8]475*NBP[8]501*NBP[8]527*NBP[8]554*NBP[8]579*NBP[8]605*NBP[8]631*NBP[8]657*NBP[8]683*NBP[8]709*NBP[8]735*NBP[8]762*NBP[8]788*NBP[8]825*NBP[8]874*NBP[8]925*NBP[8]975*NBP[8]1025*NBP[8]1075*NBP[8]1125*NBP[8]1174*NBP[8]1240*NBP[8]1332*NBP[8]1433*NBP[8]1531*NBP[9]96*NBP[9]125*NBP[9]149*NBP[9]176*NBP[9]205*NBP[9]226*NBP[9]253*NBP[9]278*NBP[9]304*NBP[9]329*NBP[9]354*NBP[9]380*NBP[9]406*NBP[9]431*NBP[9]457*NBP[9]482*NBP[9]507*NBP[9]533*NBP[9]559*NBP[9]584*NBP[9]609*NBP[9]635*NBP[9]661*NBP[9]686*NBP[9]711*NBP[9]737*NBP[9]763*NBP[9]788*NBP[9]825*NBP[9]875*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 10 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Vapour Phase (continued) Phase Fraction 1.000COMPONENTS
NBP[9]927*NBP[9]978*NBP[9]1029*NBP[9]1079*NBP[9]1132*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.0000
Total 4.9232 1.0000 12484.8155 1.0000 2263.1948 1.0000Liquid Phase Phase Fraction 0.0000
COMPONENTS
NitrogenMethaneCO2EthanePropanei-Butanen-Butanei-Pentanen-Pentanen-Hexanen-Heptanen-Octanen-Nonanen-Decanen-C11H2SH2OSEF-10*NBP[0]80*NBP[0]110*NBP[0]135*NBP[0]159*NBP[0]186*NBP[0]215*NBP[0]233*NBP[0]263*NBP[0]286*NBP[0]310*NBP[0]336*NBP[0]360*NBP[0]386*NBP[0]411*NBP[0]437*NBP[0]461*NBP[0]487*NBP[0]511*NBP[0]536*NBP[0]562*NBP[0]587*NBP[0]612*NBP[0]637*NBP[0]662*NBP[0]687*NBP[0]713*NBP[0]738*NBP[0]763*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.01670.00290.01120.02100.01220.02100.01560.01410.02830.04360.04620.02470.01070.00000.00000.00100.00000.00250.00170.00280.00340.00510.01240.02190.02160.03530.03450.04060.03280.02870.02990.03440.03080.02850.03040.02520.02400.02430.02120.01890.01740.01630.01520.01410.0136
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00130.00060.00160.00440.00340.00580.00530.00480.01150.02070.02500.01500.00720.00000.00000.00010.00000.00080.00060.00100.00130.00210.00570.01080.01150.01990.02060.02600.02230.02070.02300.02840.02690.02650.03020.02640.02680.02860.02640.02480.02410.02380.02320.02240.0227
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00360.00060.00380.00730.00510.00840.00720.00640.01470.02540.02990.01760.00830.00000.00000.00010.00000.00090.00070.00120.00160.00250.00660.01230.01290.02210.02270.02830.02400.02210.02430.02960.02790.02720.03070.02670.02680.02840.02600.02420.02330.02290.02210.02120.0214
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 11 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Liquid Phase (continued) Phase Fraction 0.0000COMPONENTS
NBP[0]788*NBP[0]825*NBP[0]874*NBP[0]924*NBP[0]975*NBP[0]1025*NBP[0]1076*NBP[0]1125*NBP[0]1173*NBP[0]1250*NBP[0]1363*NBP[0]1466*NBP[0]1587*NBP[0]1697*NBP[1]107*NBP[1]133*NBP[1]158*NBP[1]184*NBP[1]210*NBP[1]236*NBP[1]260*NBP[1]285*NBP[1]310*NBP[1]335*NBP[1]360*NBP[1]385*NBP[1]411*NBP[1]436*NBP[1]461*NBP[1]487*NBP[1]511*NBP[1]536*NBP[1]562*NBP[1]587*NBP[1]612*NBP[1]637*NBP[1]662*NBP[1]687*NBP[1]712*NBP[1]738*NBP[1]763*NBP[1]788*NBP[1]825*NBP[1]874*NBP[1]925*NBP[1]975*NBP[1]1025*NBP[1]1075*NBP[1]1125*NBP[1]1174*NBP[1]1252*NBP[2]93*NBP[2]125*NBP[2]151*NBP[2]173*NBP[2]206*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.01350.02420.01920.01420.01150.01000.00980.00870.00670.01160.00640.00360.00200.00190.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.02360.04570.03940.03140.02730.02550.02660.02590.02130.04020.02510.01550.00920.00930.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.02210.04230.03610.02840.02440.02260.02330.02240.01820.03380.02070.01260.00740.00740.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 12 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Liquid Phase (continued) Phase Fraction 0.0000COMPONENTS
NBP[2]228*NBP[2]250*NBP[2]280*NBP[2]304*NBP[2]328*NBP[2]352*NBP[2]380*NBP[2]405*NBP[2]430*NBP[2]454*NBP[2]480*NBP[2]506*NBP[2]532*NBP[2]558*NBP[2]583*NBP[2]609*NBP[2]634*NBP[2]660*NBP[2]686*NBP[2]711*NBP[2]736*NBP[2]762*NBP[2]788*NBP[2]821*NBP[2]869*NBP[2]926*NBP[2]985*NBP[2]1035*NBP[2]1079*NBP[2]1131*NBP[2]1187*NBP[2]1264*NBP[2]1361*NBP[2]1456*NBP[2]1559*NBP[3]98*NBP[3]129*NBP[3]153*NBP[3]179*NBP[3]212*NBP[3]228*NBP[3]255*NBP[3]281*NBP[3]306*NBP[3]331*NBP[3]356*NBP[3]382*NBP[3]407*NBP[3]433*NBP[3]459*NBP[3]483*NBP[3]509*NBP[3]533*NBP[3]561*NBP[3]585*NBP[3]610*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 13 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Liquid Phase (continued) Phase Fraction 0.0000COMPONENTS
NBP[3]636*NBP[3]661*NBP[3]687*NBP[3]712*NBP[3]737*NBP[3]763*NBP[3]789*NBP[3]824*NBP[3]872*NBP[3]922*NBP[3]973*NBP[3]1023*NBP[3]1073*NBP[3]1123*NBP[8]110*NBP[8]136*NBP[8]162*NBP[8]189*NBP[8]217*NBP[8]239*NBP[8]267*NBP[8]292*NBP[8]318*NBP[8]344*NBP[8]370*NBP[8]397*NBP[8]423*NBP[8]449*NBP[8]475*NBP[8]501*NBP[8]527*NBP[8]554*NBP[8]579*NBP[8]605*NBP[8]631*NBP[8]657*NBP[8]683*NBP[8]709*NBP[8]735*NBP[8]762*NBP[8]788*NBP[8]825*NBP[8]874*NBP[8]925*NBP[8]975*NBP[8]1025*NBP[8]1075*NBP[8]1125*NBP[8]1174*NBP[8]1240*NBP[8]1332*NBP[8]1433*NBP[8]1531*NBP[9]96*NBP[9]125*NBP[9]149*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 14 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Liquid Phase (continued) Phase Fraction 0.0000COMPONENTS
NBP[9]176*NBP[9]205*NBP[9]226*NBP[9]253*NBP[9]278*NBP[9]304*NBP[9]329*NBP[9]354*NBP[9]380*NBP[9]406*NBP[9]431*NBP[9]457*NBP[9]482*NBP[9]507*NBP[9]533*NBP[9]559*NBP[9]584*NBP[9]609*NBP[9]635*NBP[9]661*NBP[9]686*NBP[9]711*NBP[9]737*NBP[9]763*NBP[9]788*NBP[9]825*NBP[9]875*NBP[9]927*NBP[9]978*NBP[9]1029*NBP[9]1079*NBP[9]1132*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000Aqueous Phase Phase Fraction 0.0000
COMPONENTS
NitrogenMethaneCO2EthanePropanei-Butanen-Butanei-Pentanen-Pentanen-Hexanen-Heptanen-Octanen-Nonanen-Decanen-C11H2SH2OSEF-10*NBP[0]80*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.99990.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00020.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.99980.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00020.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.99980.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 15 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Aqueous Phase (continued) Phase Fraction 0.0000COMPONENTS
NBP[0]110*NBP[0]135*NBP[0]159*NBP[0]186*NBP[0]215*NBP[0]233*NBP[0]263*NBP[0]286*NBP[0]310*NBP[0]336*NBP[0]360*NBP[0]386*NBP[0]411*NBP[0]437*NBP[0]461*NBP[0]487*NBP[0]511*NBP[0]536*NBP[0]562*NBP[0]587*NBP[0]612*NBP[0]637*NBP[0]662*NBP[0]687*NBP[0]713*NBP[0]738*NBP[0]763*NBP[0]788*NBP[0]825*NBP[0]874*NBP[0]924*NBP[0]975*NBP[0]1025*NBP[0]1076*NBP[0]1125*NBP[0]1173*NBP[0]1250*NBP[0]1363*NBP[0]1466*NBP[0]1587*NBP[0]1697*NBP[1]107*NBP[1]133*NBP[1]158*NBP[1]184*NBP[1]210*NBP[1]236*NBP[1]260*NBP[1]285*NBP[1]310*NBP[1]335*NBP[1]360*NBP[1]385*NBP[1]411*NBP[1]436*NBP[1]461*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 16 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Aqueous Phase (continued) Phase Fraction 0.0000COMPONENTS
NBP[1]487*NBP[1]511*NBP[1]536*NBP[1]562*NBP[1]587*NBP[1]612*NBP[1]637*NBP[1]662*NBP[1]687*NBP[1]712*NBP[1]738*NBP[1]763*NBP[1]788*NBP[1]825*NBP[1]874*NBP[1]925*NBP[1]975*NBP[1]1025*NBP[1]1075*NBP[1]1125*NBP[1]1174*NBP[1]1252*NBP[2]93*NBP[2]125*NBP[2]151*NBP[2]173*NBP[2]206*NBP[2]228*NBP[2]250*NBP[2]280*NBP[2]304*NBP[2]328*NBP[2]352*NBP[2]380*NBP[2]405*NBP[2]430*NBP[2]454*NBP[2]480*NBP[2]506*NBP[2]532*NBP[2]558*NBP[2]583*NBP[2]609*NBP[2]634*NBP[2]660*NBP[2]686*NBP[2]711*NBP[2]736*NBP[2]762*NBP[2]788*NBP[2]821*NBP[2]869*NBP[2]926*NBP[2]985*NBP[2]1035*NBP[2]1079*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 17 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Aqueous Phase (continued) Phase Fraction 0.0000COMPONENTS
NBP[2]1131*NBP[2]1187*NBP[2]1264*NBP[2]1361*NBP[2]1456*NBP[2]1559*NBP[3]98*NBP[3]129*NBP[3]153*NBP[3]179*NBP[3]212*NBP[3]228*NBP[3]255*NBP[3]281*NBP[3]306*NBP[3]331*NBP[3]356*NBP[3]382*NBP[3]407*NBP[3]433*NBP[3]459*NBP[3]483*NBP[3]509*NBP[3]533*NBP[3]561*NBP[3]585*NBP[3]610*NBP[3]636*NBP[3]661*NBP[3]687*NBP[3]712*NBP[3]737*NBP[3]763*NBP[3]789*NBP[3]824*NBP[3]872*NBP[3]922*NBP[3]973*NBP[3]1023*NBP[3]1073*NBP[3]1123*NBP[8]110*NBP[8]136*NBP[8]162*NBP[8]189*NBP[8]217*NBP[8]239*NBP[8]267*NBP[8]292*NBP[8]318*NBP[8]344*NBP[8]370*NBP[8]397*NBP[8]423*NBP[8]449*NBP[8]475*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Aqueous Phase (continued) Phase Fraction 0.0000COMPONENTS
NBP[8]501*NBP[8]527*NBP[8]554*NBP[8]579*NBP[8]605*NBP[8]631*NBP[8]657*NBP[8]683*NBP[8]709*NBP[8]735*NBP[8]762*NBP[8]788*NBP[8]825*NBP[8]874*NBP[8]925*NBP[8]975*NBP[8]1025*NBP[8]1075*NBP[8]1125*NBP[8]1174*NBP[8]1240*NBP[8]1332*NBP[8]1433*NBP[8]1531*NBP[9]96*NBP[9]125*NBP[9]149*NBP[9]176*NBP[9]205*NBP[9]226*NBP[9]253*NBP[9]278*NBP[9]304*NBP[9]329*NBP[9]354*NBP[9]380*NBP[9]406*NBP[9]431*NBP[9]457*NBP[9]482*NBP[9]507*NBP[9]533*NBP[9]559*NBP[9]584*NBP[9]609*NBP[9]635*NBP[9]661*NBP[9]686*NBP[9]711*NBP[9]737*NBP[9]763*NBP[9]788*NBP[9]825*NBP[9]875*NBP[9]927*NBP[9]978*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Aqueous Phase (continued) Phase Fraction 0.0000COMPONENTS
NBP[9]1029*NBP[9]1079*NBP[9]1132*
MOLAR FLOW (MMSCFD)
0.00000.00000.0000
MOLE FRACTION
0.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.0000
MASS FRACTION
0.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.0000
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000K VALUE
COMPONENTSNitrogenMethane
CO2Ethane
Propanei-Butane
n-Butanei-Pentane
n-Pentanen-Hexane
n-Heptanen-Octane
n-Nonanen-Decane
n-C11H2SH2O
SEF-10*NBP[0]80*
NBP[0]110*NBP[0]135*NBP[0]159*NBP[0]186*NBP[0]215*NBP[0]233*NBP[0]263*NBP[0]286*NBP[0]310*NBP[0]336*NBP[0]360*NBP[0]386*NBP[0]411*NBP[0]437*NBP[0]461*NBP[0]487*NBP[0]511*NBP[0]536*NBP[0]562*NBP[0]587*NBP[0]612*NBP[0]637*NBP[0]662*NBP[0]687*NBP[0]713*NBP[0]738*NBP[0]763*NBP[0]788*NBP[0]825*NBP[0]874*
MIXED111.343.3615.069.3112.8921.206
0.88980.37150.2867
9.501e-0023.249e-0021.111e-0023.952e-0031.435e-0035.039e-004
5.69014.32
---0.37850.22810.1443
9.336e-0025.536e-0023.130e-0022.141e-0021.140e-0026.809e-0033.903e-0032.152e-0031.185e-0036.256e-0043.242e-0041.622e-0048.204e-0053.888e-0051.886e-0058.710e-0063.767e-0061.672e-0067.122e-0072.885e-0071.138e-0074.348e-0081.608e-0085.722e-0091.942e-0096.418e-0101.174e-0101.086e-011
LIGHT111.343.3615.069.3112.8921.206
0.88980.37150.2867
9.501e-0023.249e-0021.111e-0023.952e-0031.435e-0035.039e-004
5.69014.32
---0.37850.22810.1443
9.336e-0025.536e-0023.130e-0022.141e-0021.140e-0026.809e-0033.903e-0032.152e-0031.185e-0036.256e-0043.242e-0041.622e-0048.204e-0053.888e-0051.886e-0058.710e-0063.767e-0061.672e-0067.122e-0072.885e-0071.138e-0074.348e-0081.608e-0085.722e-0091.942e-0096.418e-0101.174e-0101.086e-011
HEAVY1.731e+0041.294e+007
525.94.569e+0084.373e+010
------------------------------
162.31.395e-002
------------------------------------------------------------------------------------------------
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonK VALUE
COMPONENTSNBP[0]924*NBP[0]975*
NBP[0]1025*NBP[0]1076*NBP[0]1125*NBP[0]1173*NBP[0]1250*NBP[0]1363*NBP[0]1466*NBP[0]1587*NBP[0]1697*
NBP[1]107*NBP[1]133*NBP[1]158*NBP[1]184*NBP[1]210*NBP[1]236*NBP[1]260*NBP[1]285*NBP[1]310*NBP[1]335*NBP[1]360*NBP[1]385*NBP[1]411*NBP[1]436*NBP[1]461*NBP[1]487*NBP[1]511*NBP[1]536*NBP[1]562*NBP[1]587*NBP[1]612*NBP[1]637*NBP[1]662*NBP[1]687*NBP[1]712*NBP[1]738*NBP[1]763*NBP[1]788*NBP[1]825*NBP[1]874*NBP[1]925*NBP[1]975*
NBP[1]1025*NBP[1]1075*NBP[1]1125*NBP[1]1174*NBP[1]1252*
NBP[2]93*NBP[2]125*NBP[2]151*NBP[2]173*NBP[2]206*NBP[2]228*NBP[2]250*NBP[2]280*NBP[2]304*NBP[2]328*NBP[2]352*
MIXED7.852e-0134.934e-0142.527e-0151.165e-0165.247e-0182.181e-0191.203e-0216.365e-0256.834e-0284.712e-0317.299e-033
------------------------------------------------------------------------------------------------------------------------------------------------
LIGHT7.852e-0134.934e-0142.527e-0151.165e-0165.247e-0182.181e-0191.203e-0216.365e-0256.834e-0284.712e-0317.299e-033
------------------------------------------------------------------------------------------------------------------------------------------------
HEAVY---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonK VALUE
COMPONENTSNBP[2]380*NBP[2]405*NBP[2]430*NBP[2]454*NBP[2]480*NBP[2]506*NBP[2]532*NBP[2]558*NBP[2]583*NBP[2]609*NBP[2]634*NBP[2]660*NBP[2]686*NBP[2]711*NBP[2]736*NBP[2]762*NBP[2]788*NBP[2]821*NBP[2]869*NBP[2]926*NBP[2]985*
NBP[2]1035*NBP[2]1079*NBP[2]1131*NBP[2]1187*NBP[2]1264*NBP[2]1361*NBP[2]1456*NBP[2]1559*
NBP[3]98*NBP[3]129*NBP[3]153*NBP[3]179*NBP[3]212*NBP[3]228*NBP[3]255*NBP[3]281*NBP[3]306*NBP[3]331*NBP[3]356*NBP[3]382*NBP[3]407*NBP[3]433*NBP[3]459*NBP[3]483*NBP[3]509*NBP[3]533*NBP[3]561*NBP[3]585*NBP[3]610*NBP[3]636*NBP[3]661*NBP[3]687*NBP[3]712*NBP[3]737*NBP[3]763*NBP[3]789*NBP[3]824*NBP[3]872*
MIXED---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------
LIGHT---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------
HEAVY---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonK VALUE
COMPONENTSNBP[3]922*NBP[3]973*
NBP[3]1023*NBP[3]1073*NBP[3]1123*
NBP[8]110*NBP[8]136*NBP[8]162*NBP[8]189*NBP[8]217*NBP[8]239*NBP[8]267*NBP[8]292*NBP[8]318*NBP[8]344*NBP[8]370*NBP[8]397*NBP[8]423*NBP[8]449*NBP[8]475*NBP[8]501*NBP[8]527*NBP[8]554*NBP[8]579*NBP[8]605*NBP[8]631*NBP[8]657*NBP[8]683*NBP[8]709*NBP[8]735*NBP[8]762*NBP[8]788*NBP[8]825*NBP[8]874*NBP[8]925*NBP[8]975*
NBP[8]1025*NBP[8]1075*NBP[8]1125*NBP[8]1174*NBP[8]1240*NBP[8]1332*NBP[8]1433*NBP[8]1531*
NBP[9]96*NBP[9]125*NBP[9]149*NBP[9]176*NBP[9]205*NBP[9]226*NBP[9]253*NBP[9]278*NBP[9]304*NBP[9]329*NBP[9]354*NBP[9]380*NBP[9]406*NBP[9]431*NBP[9]457*
MIXED---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------
LIGHT---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------
HEAVY---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 8-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonK VALUE
COMPONENTSNBP[9]482*NBP[9]507*NBP[9]533*NBP[9]559*NBP[9]584*NBP[9]609*NBP[9]635*NBP[9]661*NBP[9]686*NBP[9]711*NBP[9]737*NBP[9]763*NBP[9]788*NBP[9]825*NBP[9]875*NBP[9]927*NBP[9]978*
NBP[9]1029*NBP[9]1079*NBP[9]1132*
MIXED------------------------------------------------------------
LIGHT------------------------------------------------------------
HEAVY------------------------------------------------------------
UNIT OPERATIONSFEED TO
Mixer: MIX-103-3PRODUCT FROM
Separator: V-101-3LOGICAL CONNECTION
UTILITIES( No utilities reference this stream )
PROCESS UTILITY
DYNAMICSPressure Specification (Inactive): 68.00 psigFlow Specification (Inactive) Molar: 4.923 MMSCFD Mass: 1.248e+004 lb/hr Std Ideal Liq Volume:2263 barrel/day
User VariablesNOTES
Description
Material Stream: 17-3 Fluid Package: Basis-1Property Package: Peng-RobinsonCONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psig)Molar Flow (MMSCFD)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)Liq Vol Flow @Std Cond (barrel/day)
Overall1.0000
106.168.009.846
2.497e+0044526
-4.144e+00442.37
-4.480e+0071.742e+006 *
Vapour Phase1.0000
106.168.009.846
2.497e+0044526
-4.144e+00442.37
-4.480e+0071.742e+006
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 17-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonPROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLHV Molar Basis (Std)HHV Molar Basis (Std)HHV Mass Basis (Std)CO2 LoadingCO2 App ML ConCO2 App WT ConLHV Mass Basis (Std)Phase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Phase Fraction [Act. Vol. 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 IndexMass Exergy
(lbmole/ft3)(lb/ft3)
(barrel/day)(Btu/lb)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole)(Btu/lbmole)
(Btu/lb)
(lbmole/ft3)(lbmol/lb)
(Btu/lb)
(psig)(Cost/s)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(API_60)
(barrel/day)
(psig)
(Btu/lbmole)(cSt)
(API_60)(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)
(psig)(psig)
(barrel/day)
(Btu/lb)
Overall23.09
1.390e-0020.3211
3.325e+005-17941.83410.97
0.4751---------------------
1.0001.0001.000
-11.130.0000
12961.02110.979.847242.4
---0.9797
16.91---
-14.701.2211.2467813
2.2781.438e+0051.742e+006
0.000071.93338.3
1.0000---
1.789e-0021.172e-002
8.9870.3892
8.8090.3814
------------
27101.742e+006
-15.1479.18
Vapour Phase23.09
1.390e-0020.3211
3.325e+005-17941.83410.97
0.4751---------------------
1.0001.0001.000
---0.0000
12961.02110.979.847242.4
---0.9797
16.91------
1.2211.246
---2.278
1.438e+0051.742e+006
0.000071.93
---1.0000
---1.789e-0021.172e-002
8.9870.3892
8.8090.3814
------------
27101.742e+006
------
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 17-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Overall Phase Vapour Fraction 1.0000COMPONENTS
NitrogenMethaneCO2EthanePropanei-Butanen-Butanei-Pentanen-Pentanen-Hexanen-Heptanen-Octanen-Nonanen-Decanen-C11H2SH2OSEF-10*NBP[0]80*NBP[0]110*NBP[0]135*NBP[0]159*NBP[0]186*NBP[0]215*NBP[0]233*NBP[0]263*NBP[0]286*NBP[0]310*NBP[0]336*NBP[0]360*NBP[0]386*NBP[0]411*NBP[0]437*NBP[0]461*NBP[0]487*NBP[0]511*NBP[0]536*NBP[0]562*NBP[0]587*NBP[0]612*NBP[0]637*NBP[0]662*NBP[0]687*NBP[0]713*NBP[0]738*NBP[0]763*NBP[0]788*NBP[0]825*NBP[0]874*NBP[0]924*NBP[0]975*NBP[0]1025*NBP[0]1076*NBP[0]1125*NBP[0]1173*NBP[0]1250*
MOLAR FLOW (MMSCFD)
0.03327.11940.42461.02250.59760.14540.18410.05700.03980.02650.01390.00510.00100.00020.00000.00000.13740.00000.00930.00380.00400.00310.00280.00380.00460.00240.00240.00130.00090.00040.00020.00010.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00340.72300.04310.10380.06070.01480.01870.00580.00400.00270.00140.00050.00010.00000.00000.00000.01390.00000.00090.00040.00040.00030.00030.00040.00050.00020.00020.00010.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
101.971212541.3457
2051.67713375.98002893.6739
927.76951174.7438
451.2602314.9811250.4580153.4875
63.458613.5492
2.36760.00220.0364
271.70620.0000
66.169828.890732.838927.926226.886040.813152.846729.958030.932618.381312.8033
6.03432.95811.70641.05220.50540.23600.13010.05270.02310.01100.00430.00160.00060.00020.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00410.50230.08220.13520.11590.03720.04700.01810.01260.01000.00610.00250.00050.00010.00000.00000.01090.00000.00270.00120.00130.00110.00110.00160.00210.00120.00120.00070.00050.00020.00010.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
8.65882868.2652
170.2147649.9127391.0532113.0442137.9199
49.562034.249125.879715.3021
6.16011.28810.22120.00020.0032
18.64200.00006.64122.86433.20492.68862.55343.80444.87122.72702.78831.64101.12960.52740.25600.14620.08920.04250.01960.01070.00430.00190.00090.00030.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00190.63370.03760.14360.08640.02500.03050.01090.00760.00570.00340.00140.00030.00000.00000.00000.00410.00000.00150.00060.00070.00060.00060.00080.00110.00060.00060.00040.00020.00010.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 26 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 17-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000COMPONENTS
NBP[0]1363*NBP[0]1466*NBP[0]1587*NBP[0]1697*NBP[1]107*NBP[1]133*NBP[1]158*NBP[1]184*NBP[1]210*NBP[1]236*NBP[1]260*NBP[1]285*NBP[1]310*NBP[1]335*NBP[1]360*NBP[1]385*NBP[1]411*NBP[1]436*NBP[1]461*NBP[1]487*NBP[1]511*NBP[1]536*NBP[1]562*NBP[1]587*NBP[1]612*NBP[1]637*NBP[1]662*NBP[1]687*NBP[1]712*NBP[1]738*NBP[1]763*NBP[1]788*NBP[1]825*NBP[1]874*NBP[1]925*NBP[1]975*NBP[1]1025*NBP[1]1075*NBP[1]1125*NBP[1]1174*NBP[1]1252*NBP[2]93*NBP[2]125*NBP[2]151*NBP[2]173*NBP[2]206*NBP[2]228*NBP[2]250*NBP[2]280*NBP[2]304*NBP[2]328*NBP[2]352*NBP[2]380*NBP[2]405*NBP[2]430*NBP[2]454*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 27 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 17-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000COMPONENTS
NBP[2]480*NBP[2]506*NBP[2]532*NBP[2]558*NBP[2]583*NBP[2]609*NBP[2]634*NBP[2]660*NBP[2]686*NBP[2]711*NBP[2]736*NBP[2]762*NBP[2]788*NBP[2]821*NBP[2]869*NBP[2]926*NBP[2]985*NBP[2]1035*NBP[2]1079*NBP[2]1131*NBP[2]1187*NBP[2]1264*NBP[2]1361*NBP[2]1456*NBP[2]1559*NBP[3]98*NBP[3]129*NBP[3]153*NBP[3]179*NBP[3]212*NBP[3]228*NBP[3]255*NBP[3]281*NBP[3]306*NBP[3]331*NBP[3]356*NBP[3]382*NBP[3]407*NBP[3]433*NBP[3]459*NBP[3]483*NBP[3]509*NBP[3]533*NBP[3]561*NBP[3]585*NBP[3]610*NBP[3]636*NBP[3]661*NBP[3]687*NBP[3]712*NBP[3]737*NBP[3]763*NBP[3]789*NBP[3]824*NBP[3]872*NBP[3]922*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Aspen Technology Inc. Aspen HYSYS Version 8 (27.0.0.8138) Page 28 of 125
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* Specified by user.Licensed to: LEGENDS
-
LEGENDSBurlington, MAUSA
Case Name: SIMULACION COMPLETA.HSCUnit Set: CHIMIREDate/Time: Thu Jun 05 13:33:05 2014
Material Stream: 17-3 (continued) Fluid Package: Basis-1Property Package: Peng-RobinsonCOMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000COMPONENTS
NBP[3]973*NBP[3]1023*NBP[3]1073*NBP[3]1123*NBP[8]110*NBP[8]136*NBP[8]162*NBP[8]189*NBP[8]217*NBP[8]239*NBP[8]267*NBP[8]292*NBP[8]318*NBP[8]344*NBP[8]370*NBP[8]397*NBP[8]423*NBP[8]449*NBP[8]475*NBP[8]501*NBP[8]527*NBP[8]554*NBP[8]579*NBP[8]605*NBP[8]631*NBP[8]657*NBP[8]683*NBP[8]709*NBP[8]735*NBP[8]762*NBP[8]788*NBP[8]825*NBP[8]874*NBP[8]925*NBP[8]975*NBP[8]1025*NBP[8]1075*NBP[8]1125*NBP[8]1174*NBP[8]1240*NBP[8]1332*NBP[8]1433*NBP[8]1531*NBP[9]96*NBP[9]125*NBP[9]149*NBP[9]176*NBP[9]205*NBP[9]226*NBP[9]253*NBP[9]278*NBP[9]304*NBP[9]329*NBP[9]354*NBP[9]380*NBP[9]406*
MOLAR FLOW (MMSCFD)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FLOW (lb/hr)
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.