FSD100MbP?h㈵>dk*dgffffr@м@ COCO teamcocosimulator.orgR.H. Cavett (Cavett, R. H., 'Application of Numerical Methods to the Convergence of Simulated Processes Involving Recycle Loops', American Petroleum Institute, 43, 57, 1963) devised a now famous problem to test tearing, sequencing and convergence procedures of flowsheet simulation programs. The flowsheet is equivalent to a four theoretical stage near isothermal distillation (rather than a conventional near isobaric type). Thanks to Dean J MastropietroHKx temperaturepressure compositionflow Rosen Cavettڐ@'t+nj Rosen Cavett:0yE>MbP?MbP?MbP?K%c:\werk\CO\COCO\bin\data\ChemSep1.pcdVCarbon dioxideOCOCO2124-38-9O=C=O \s@)\A@b?@7? 8`k@`k@@A@7F@I??Y=p@<,?@A|th A3aA 8E@ @y2 8 8@3a@`k@ $@? \s@w? 8`k@ \s@iW@̯#( 0>@ k@ \s@ejtA]?@ݿ ?I?`k@ \s@j@3A@VN(7i?`./9@`k@d@5[@@ ?@S>`k@ r@@A@z~`P%@k൓,>I@@@`?KA@}`b^@@o@3c@@h @d Ra?@@`k@`fr@e>?=Jr@`f@ 8@e@@fϿ`Kܵ?`t>`k@r@K7@|~ܿ@ ш@R@A 8f@p@fЇpfܱ?]i`k@ \s@V@)\R@@> 8@o@@ 8 8 8 8 8 8 8C5@@0 8 8 \k@@p@ *È?D 8 8`k@`fr@ ڬ\m1@`"8d@>@?@?@?h?`q@`? 8 8h?}ͺ? 8 8?`f:@I?[_/ @`}g@ 8 W?`?MNitrogenN2N2 7727-37-9N#NJ̌_@IA ?~?`fVS@`O@`O@t@<@`֡??=@-?d6A``A%A 8 \B@ۮ 8 8 8`f4@@3O@@z@@r?G_@`;? 8@3O@࣐_@iBD@|@??@ gN@࣐_@e"zAY5@ 33@+@3O@࣐_@jHnA]@`-'``?@%5@`f @ 8@3O@Ȟ@f˿$@ u7?&eN@_@`?6?@^?@3@@^r@ 8I@@@f@d5X@Ֆ3?`7@3O@̌_@@@`]\AC? 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L`?=n@@j@ (3h?֔>`<@=j@dd AH@Ҟ@~?@F=n@`{@ Aֆ`+@`+@o>i@p@@f?QćR$(As@p@h$W`8@@`e)@ O@=n@@3@e ^_>`;? ]@ 8=n@@@f@P?GjͦgRt`ݶ>=n@GQ}@ [A?(?`T@_gaA 8GQ}@@@f9^#Al[k>=n@@  ]@@:gZ!? 8i@p@ 8 8 8 8 8 8 8G5@`f@AT 8 8x@`d@ @}?@ k ? 8 8=n@@3@ |@ X9@ X9@@?9@^)? 8 8?`?? 8`?@l@ *?Cn @Bs@ &?)?  compressibilityFactorcompressibilityFactordensitydensitydensity/volume (pure)density/volume (pure) enthalpyenthalpyentropyentropyfugacityfugacityfugacityCoefficientfugacityCoefficient heatOfVaporizationheatOfVaporizationOidealGasEnthalpyidealGasEnthalpy logFugacityCoefficientlogFugacityCoefficientsurfaceTensionsurfaceTensionsurfaceTension (pure)surfaceTension (pure)thermalConductivitythermalConductivity04thermalConductivity (pure)thermalConductivity (pure))1 vaporPressure vaporPressureN viscosity viscosity& viscosity (pure)viscosity (pure)" volumevolumeVapor Vapor phaseLiquid Liquid phase   {Gz?Carbon dioxide/carbon dioxideimported from HAYDENO.IPD?Hydrogen sulfide/carbon dioxideimported from HAYDENO.IPD?Hydrogen sulfide/carbon dioxideimported from HAYDENO.IPD$Aǘ,Nitrogen/CarbonDioxide T=223.15-273.15K p306imported from PR.IPD(~k ?-CarbonDioxide/HydrogenSulfide T=225-363K p581imported from PR.IPD:M?+C1/CarbonDioxide T=173-220K P=26-66bar p398imported from PR.IPD~k ?CarbonDioxide/C2 T=250K p525imported from PR.IPDE?&CarbonDioxide/C3 T=277.59-344.26K p589imported from PR.IPDp= ף?*CarbonDioxide/Iso-C4 T=310.93-394.26K p601imported from PR.IPDX5;N?'CarbonDioxide/nC4 T=310.93-410.93K p607imported from PR.IPDa4?CarbonDioxide/Iso-C5 p612imported from PR.IPD{Gz'CarbonDioxide/nC5 P=41.33-82.79bar p616imported from PR.IPD)\(?CarbonDioxide/nC6 p625imported from PR.IPD?CarbonDioxide/nC7 p631imported from PR.IPD=yX5?CarbonDioxide/nC10 p638imported from PR.IPDAǘ,Nitrogen/CarbonDioxide T=223.15-273.15K p306imported from PR.IPD.1?.Nitrogen/HydrogenSulfide T=227.98,200.15K p316imported from PR.IPDj+? Nitrogen/C1 T=88.71-188.71K p285imported from PR.IPD"u?Nitrogen/C2 T=200-290K p300imported from PR.IPDz?!Nitrogen/C3 T=143.15-353.15K p322imported from PR.IPDBiq?Nitrogen/Iso-C4 p330imported from PR.IPD߾3?"Nitrogen/nC4 T=310.93-422.04K p333imported from PR.IPD|Pk?Nitrogen/Iso-C5 p336imported from PR.IPD?Nitrogen/nC5 p338imported from PR.IPD&?Nitrogen/nC6 p341imported from PR.IPDBiq?Nitrogen/nC7 p344imported from PR.IPDٿNitrogen/nC8 p347imported from PR.IPDw#?#Nitrogen/nC10 T=310.93-410.93K p349imported from PR.IPD(~k ?-CarbonDioxide/HydrogenSulfide T=225-363K p581imported from PR.IPD.1?.Nitrogen/HydrogenSulfide T=227.98,200.15K p316imported from PR.IPD/' ?0C2/HydrogenSulfide T=200-283 P=0.65-30.5bar p533imported from PR.IPDQ?(HydrogenSulfide/C3 P=27.58-41.44bar p643imported from PR.IPD0*D?HydrogenSulfide/Iso-C4 p645imported from PR.IPDT㥛 ?HydrogenSulfide/nC5 p647imported from PR.IPD镲 ?HydrogenSulfide/nC10 p652imported from PR.IPD:M?+C1/CarbonDioxide T=173-220K P=26-66bar p398imported from PR.IPDj+? Nitrogen/C1 T=88.71-188.71K p285imported from PR.IPDF%ukC1/C2 T=130.37-199.93K p385imported from PR.IPDtF_?C1/C3 T=130.37-213.71K p413imported from PR.IPD-C6?C1/Iso-C4 p419imported from PR.IPDHP?C1/nC4 T=294-394K p422imported from PR.IPDǺvC1/Iso-C5 p436imported from PR.IPDZd;O?C1/nC5 T=278-461K p438imported from PR.IPD{Gz?C1/nC6 T=183-423K p453imported from PR.IPD#?C1/nC7 T=200-255K p469imported from PR.IPDa+e? C1/nC8 p477imported from PR.IPD0*D? C1/nC9 p481imported from PR.IPD(~k ?C1/nC10 T=244-277K p485imported from PR.IPD~k ?CarbonDioxide/C2 T=250K p525imported from PR.IPD"u?Nitrogen/C2 T=200-290K p300imported from PR.IPD/' ?0C2/HydrogenSulfide T=200-283 P=0.65-30.5bar p533imported from PR.IPDF%ukC1/C2 T=130.37-199.93K p385imported from PR.IPD/nR? C2/C3 p539imported from PR.IPDS!uq{C2/Iso-C4 p542imported from PR.IPDy):?$C2/nC4 T=229-361K P=6.9-57.9bar p544imported from PR.IPDq? C2/nC5 p550imported from PR.IPD{GzC2/nC6 T=338.7-449.8K p557imported from PR.IPD_vO~?C2/nC7 P=6.89-86.186bar p567imported from PR.IPDl? C2/nC8 p570imported from PR.IPDH}? C2/nC10 p572imported from PR.IPDE?&CarbonDioxide/C3 T=277.59-344.26K p589imported from PR.IPDz?!Nitrogen/C3 T=143.15-353.15K p322imported from PR.IPDQ?(HydrogenSulfide/C3 P=27.58-41.44bar p643imported from PR.IPDtF_?C1/C3 T=130.37-213.71K p413imported from PR.IPD/nR? C2/C3 p539imported from PR.IPDqC3/Iso-C4 p663imported from PR.IPDF%uk? C3/nC4 p666imported from PR.IPDAǘ?C3/Iso-C5 p668imported from PR.IPDz6>W? C3/nC5 p671imported from PR.IPDǺF? C3/nC6 p674imported from PR.IPDǺv? C3/nC7 p681imported from PR.IPD C3/nC8 p683imported from PR.IPD C3/nC10 p686imported from PR.IPDp= ף?*CarbonDioxide/Iso-C4 T=310.93-394.26K p601imported from PR.IPDBiq?Nitrogen/Iso-C4 p330imported from PR.IPD0*D?HydrogenSulfide/Iso-C4 p645imported from PR.IPD-C6?C1/Iso-C4 p419imported from PR.IPDS!uq{C2/Iso-C4 p542imported from PR.IPDqC3/Iso-C4 p663imported from PR.IPD-C6:Iso-C4/nC4 p694imported from PR.IPDX5;N?'CarbonDioxide/nC4 T=310.93-410.93K p607imported from PR.IPD߾3?"Nitrogen/nC4 T=310.93-422.04K p333imported from PR.IPDHP?C1/nC4 T=294-394K p422imported from PR.IPDy):?$C2/nC4 T=229-361K P=6.9-57.9bar p544imported from PR.IPDF%uk? C3/nC4 p666imported from PR.IPD-C6:Iso-C4/nC4 p694imported from PR.IPD5;Nё? nC4/nC5 p704imported from PR.IPDǺv nC4/nC6 p706imported from PR.IPDF%uk? nC4/nC7 p707imported from PR.IPD_vO~? nC4/nC8 p708imported from PR.IPDq? nC4/nC10 p710imported from PR.IPDa4?CarbonDioxide/Iso-C5 p612imported from PR.IPD|Pk?Nitrogen/Iso-C5 p336imported from PR.IPDǺvC1/Iso-C5 p436imported from PR.IPDAǘ?C3/Iso-C5 p668imported from PR.IPDQ?Iso-C5/nC5 p715imported from PR.IPD{Gz'CarbonDioxide/nC5 P=41.33-82.79bar p616imported from PR.IPD?Nitrogen/nC5 p338imported from PR.IPDT㥛 ?HydrogenSulfide/nC5 p647imported from PR.IPDZd;O?C1/nC5 T=278-461K p438imported from PR.IPDq? C2/nC5 p550imported from PR.IPDz6>W? C3/nC5 p671imported from PR.IPD5;Nё? nC4/nC5 p704imported from PR.IPDQ?Iso-C5/nC5 p715imported from PR.IPD_vO~? nC5/nC7 p720imported from PR.IPD nC5/nC8 p721imported from PR.IPD)\(?CarbonDioxide/nC6 p625imported from PR.IPD&?Nitrogen/nC6 p341imported from PR.IPD{Gz?C1/nC6 T=183-423K p453imported from PR.IPD{GzC2/nC6 T=338.7-449.8K p557imported from PR.IPDǺF? C3/nC6 p674imported from PR.IPDǺv nC4/nC6 p706imported from PR.IPDq nC6/nC7 p745imported from PR.IPD?CarbonDioxide/nC7 p631imported from PR.IPDBiq?Nitrogen/nC7 p344imported from PR.IPD#?C1/nC7 T=200-255K p469imported from PR.IPD_vO~?C2/nC7 P=6.89-86.186bar p567imported from PR.IPDǺv? C3/nC7 p681imported from PR.IPDF%uk? nC4/nC7 p707imported from PR.IPD_vO~? nC5/nC7 p720imported from PR.IPDq nC6/nC7 p745imported from PR.IPDٿNitrogen/nC8 p347imported from PR.IPDa+e? C1/nC8 p477imported from PR.IPDl? C2/nC8 p570imported from PR.IPD C3/nC8 p683imported from PR.IPD_vO~? nC4/nC8 p708imported from PR.IPD nC5/nC8 p721imported from PR.IPD0*D? C1/nC9 p481imported from PR.IPD=yX5?CarbonDioxide/nC10 p638imported from PR.IPDw#?#Nitrogen/nC10 T=310.93-410.93K p349imported from PR.IPD镲 ?HydrogenSulfide/nC10 p652imported from PR.IPD(~k ?C1/nC10 T=244-277K p485imported from PR.IPDH}? C2/nC10 p572imported from PR.IPD C3/nC10 p686imported from PR.IPDq? nC4/nC10 p710imported from PR.IPD y): C1/C2 p385imported from SRK.IPD;On? C1/nC3 p416imported from SRK.IPDjt? C1/nC4 p422imported from SRK.IPD;On? C1/nC5 p438imported from SRK.IPDݓZ? C1/nC6 p458imported from SRK.IPD?߾? C1/nC7 p471imported from SRK.IPDǺ? C1/nC8 p477imported from SRK.IPDǺ? C1/nC9 p481imported from SRK.IPDy): C1/C2 p385imported from SRK.IPD/nb C2/nC3 p539imported from SRK.IPD_Lu? C2/nC4 p544imported from SRK.IPDǺv? C2/nC5 p550imported from SRK.IPDfj+ C2/nC6 p557imported from SRK.IPD ^)p? C2/nC7 p567imported from SRK.IPD rh? C2/nC8 p570imported from SRK.IPD;On? C1/nC3 p416imported from SRK.IPD/nb C2/nC3 p539imported from SRK.IPD nC3/nC4 p666imported from SRK.IPD$ۗ? nC3/nC5 p671imported from SRK.IPD/nb nC3/nC6 p674imported from SRK.IPD/nr? nC3/nC7 p681imported from SRK.IPD_vO~? nC3/nC8 p683imported from SRK.IPDjt? C1/nC4 p422imported from SRK.IPD_Lu? C2/nC4 p544imported from SRK.IPD nC3/nC4 p666imported from SRK.IPDZӼ? nC4/nC5 p704imported from SRK.IPDAǘ nC4/nC6 p706imported from SRK.IPD-C6: nC4/nC7 p707imported from SRK.IPD/nr? nC4/nC8 p708imported from SRK.IPD;On? C1/nC5 p438imported from SRK.IPDǺv? C2/nC5 p550imported from SRK.IPD$ۗ? nC3/nC5 p671imported from SRK.IPDZӼ? nC4/nC5 p704imported from SRK.IPDŏ1w-!_? nC5/nC7 p720imported from SRK.IPD/nb nC5/nC8 p721imported from SRK.IPDݓZ? C1/nC6 p458imported from SRK.IPDfj+ C2/nC6 p557imported from SRK.IPD/nb nC3/nC6 p674imported from SRK.IPDAǘ nC4/nC6 p706imported from SRK.IPD/nR nC6/nC7 p745imported from SRK.IPD?߾? C1/nC7 p471imported from SRK.IPD ^)p? C2/nC7 p567imported from SRK.IPD/nr? nC3/nC7 p681imported from SRK.IPD-C6: nC4/nC7 p707imported from SRK.IPDŏ1w-!_? nC5/nC7 p720imported from SRK.IPD/nR nC6/nC7 p745imported from SRK.IPDǺ? C1/nC8 p477imported from SRK.IPD rh? C2/nC8 p570imported from SRK.IPD_vO~? nC3/nC8 p683imported from SRK.IPD/nr? nC4/nC8 p708imported from SRK.IPD/nb nC5/nC8 p721imported from SRK.IPDǺ? C1/nC9 p481imported from SRK.IPD y): C1/C2 p385imported from SRK.IPD;On? C1/nC3 p416imported from SRK.IPDjt? C1/nC4 p422imported from SRK.IPD;On? C1/nC5 p438imported from SRK.IPDݓZ? C1/nC6 p458imported from SRK.IPD?߾? C1/nC7 p471imported from SRK.IPDǺ? C1/nC8 p477imported from SRK.IPDǺ? C1/nC9 p481imported from SRK.IPDy): C1/C2 p385imported from SRK.IPD/nb C2/nC3 p539imported from SRK.IPD_Lu? C2/nC4 p544imported from SRK.IPDǺv? C2/nC5 p550imported from SRK.IPDfj+ C2/nC6 p557imported from SRK.IPD ^)p? C2/nC7 p567imported from SRK.IPD rh? C2/nC8 p570imported from SRK.IPD;On? C1/nC3 p416imported from SRK.IPD/nb C2/nC3 p539imported from SRK.IPD nC3/nC4 p666imported from SRK.IPD$ۗ? nC3/nC5 p671imported from SRK.IPD/nb nC3/nC6 p674imported from SRK.IPD/nr? nC3/nC7 p681imported from SRK.IPD_vO~? nC3/nC8 p683imported from SRK.IPDjt? C1/nC4 p422imported from SRK.IPD_Lu? C2/nC4 p544imported from SRK.IPD nC3/nC4 p666imported from SRK.IPDZӼ? nC4/nC5 p704imported from SRK.IPDAǘ nC4/nC6 p706imported from SRK.IPD-C6: nC4/nC7 p707imported from SRK.IPD/nr? nC4/nC8 p708imported from SRK.IPD;On? C1/nC5 p438imported from SRK.IPDǺv? C2/nC5 p550imported from SRK.IPD$ۗ? nC3/nC5 p671imported from SRK.IPDZӼ? nC4/nC5 p704imported from SRK.IPDŏ1w-!_? nC5/nC7 p720imported from SRK.IPD/nb nC5/nC8 p721imported from SRK.IPDݓZ? C1/nC6 p458imported from SRK.IPDfj+ C2/nC6 p557imported from SRK.IPD/nb nC3/nC6 p674imported from SRK.IPDAǘ nC4/nC6 p706imported from SRK.IPD/nR nC6/nC7 p745imported from SRK.IPD?߾? C1/nC7 p471imported from SRK.IPD ^)p? C2/nC7 p567imported from SRK.IPD/nr? nC3/nC7 p681imported from SRK.IPD-C6: nC4/nC7 p707imported from SRK.IPDŏ1w-!_? nC5/nC7 p720imported from SRK.IPD/nR nC6/nC7 p745imported from SRK.IPDǺ? C1/nC8 p477imported from SRK.IPD rh? C2/nC8 p570imported from SRK.IPD_vO~? nC3/nC8 p683imported from SRK.IPD/nr? nC4/nC8 p708imported from SRK.IPD/nb nC5/nC8 p721imported from SRK.IPDǺ? C1/nC9 p481imported from SRK.IPD* QNitrogen/n-Butaneimported from UNIQUACP.IPDQ?Nitrogen/n-Hexaneimported from UNIQUACP.IPDGzMethane/Propaneimported from UNIQUACP.IPDffffffMethane/n-Butaneimported from UNIQUACP.IPDQMethane/n-Pentaneimported from UNIQUACP.IPDQMethane/n-Hexaneimported from UNIQUACP.IPDQοMethane/n-Decaneimported from UNIQUACP.IPD ףp=p@Ethane/n-Heptaneimported from UNIQUACP.IPD@Methane/Propaneimported from UNIQUACP.IPD?i-Butane/n-Butaneimported from UNIQUACP.IPDp@Nitrogen/n-Butaneimported from UNIQUACP.IPD؆@Methane/n-Butaneimported from UNIQUACP.IPD?i-Butane/n-Butaneimported from UNIQUACP.IPD@Methane/n-Pentaneimported from UNIQUACP.IPDu@Nitrogen/n-Hexaneimported from UNIQUACP.IPDW@Methane/n-Hexaneimported from UNIQUACP.IPDףp= '\Ethane/n-Heptaneimported from UNIQUACP.IPDb@Methane/n-Decaneimported from UNIQUACP.IPD* QNitrogen/n-Butaneimported from UNIQUACP.IPDQ?Nitrogen/n-Hexaneimported from UNIQUACP.IPDGzMethane/Propaneimported from UNIQUACP.IPDffffffMethane/n-Butaneimported from UNIQUACP.IPDQMethane/n-Pentaneimported from UNIQUACP.IPDQMethane/n-Hexaneimported from UNIQUACP.IPDQοMethane/n-Decaneimported from UNIQUACP.IPD ףp=p@Ethane/n-Heptaneimported from UNIQUACP.IPD@Methane/Propaneimported from UNIQUACP.IPD?i-Butane/n-Butaneimported from UNIQUACP.IPDp@Nitrogen/n-Butaneimported from UNIQUACP.IPD؆@Methane/n-Butaneimported from UNIQUACP.IPD?i-Butane/n-Butaneimported from UNIQUACP.IPD@Methane/n-Pentaneimported from UNIQUACP.IPDu@Nitrogen/n-Hexaneimported from UNIQUACP.IPDW@Methane/n-Hexaneimported from UNIQUACP.IPDףp= '\Ethane/n-Heptaneimported from UNIQUACP.IPDb@Methane/n-Decaneimported from UNIQUACP.IPDCH2CH3ͪ?A`"? rh.@CH2M O?HzG?Zd;O ,@CH F%u?v/?K7 *@CH2CH3ͪ?A`"? rh.@CH2M O?HzG?Zd;O ,@CH F%u?v/?K7 *@ V瞯< Rosen Cavett 7727-37-9Nitrogen<@`fVS@N2 Rosen CavettNitrogen74-82-8Methane 0@=[@CH4 Rosen CavettMethane74-84-0Ethane>@g@C2H6 Rosen CavettEthane74-98-6Propanej F@l@C3H8 Rosen CavettPropane75-28-5 IsobutaneM@pUp@C4H10 Rosen Cavett Isobutane106-97-8N-butaneM@` q@C4H10 Rosen CavettN-butane78-78-4 Isopentane R@r@C5H12 Rosen Cavett Isopentane109-66-0 N-pentane R@ Ss@C5H12 Rosen Cavett N-pentane110-54-3N-hexaneTU@^u@C6H14 Rosen CavettN-hexane142-82-5 N-heptane` Y@9w@C7H16 Rosen Cavett N-heptane111-65-9N-octaneȎ\@x@C8H18 Rosen CavettN-octane111-84-2N-nonaneA`@ z@C9H20 Rosen CavettN-nonane124-18-5N-decanea@{@C10H22 Rosen CavettN-decane 1120-21-4 N-undecanec@GQ}@C11H24 Rosen Cavett N-undecaneCarbon dioxide@7F@CO2 Rosen CavettCarbon dioxideHydrogen sulfideZ A@j@H2S Rosen CavettHydrogen sulfide ????????????excessEnthalpy.Dpressure??thermalConductivity.Dmoles??gibbsFreeEnergy.Dpressure??viscosity.Dtemperature????thermalConductivity.Dpressure??activityCoefficient thermalConductivity.Dtemperature??heatCapacity.DmolFraction??density.Dpressure?@?@enthalpy.Dmoles??heatOfVaporization??#logFugacityCoefficient.DmolFractionentropy.Dtemperature??viscosity.Dmoles???? volume.Dmoles@@@@enthalpy??vaporPressure.Dtemperature??activity.DmolFractionfugacity.Dtemperature??volume.Dpressure@@@@excessEnthalpy.Dtemperature??surfaceTension.DmolFraction??idealGasEnthalpy.DmolFraction??heatOfVaporization.DmolFraction?? activityCoefficient.DtemperaturefugacityCoefficient.DmolesgibbsFreeEnergy??heatOfVaporization.Dpressure??"compressibilityFactor.DtemperaturecompressibilityFactor.DpressureactivityCoefficient.Dmolesactivity.DmolesgibbsFreeEnergy.DmolFraction??enthalpy.DmolFraction??enthalpy.Dpressure??logFugacityCoefficientactivityfugacity.Dpressure fugacityCoefficient.DmolFractionvolume.DmolFraction@@@@density?@?@activity.DtemperaturethermalConductivity??surfaceTension.Dtemperature??surfaceTension??density.DmolFraction?@?@heatCapacity.Dtemperature??#logFugacityCoefficient.DtemperatureexcessEnthalpy??viscosity.DmolFraction????fugacityCoefficient.DpressuresurfaceTension.Dmoles??enthalpy.Dtemperature??entropy.Dpressure??gibbsFreeEnergy.Dmoles??density.Dmoles?@?@ thermalConductivity.DmolFraction??logFugacityCoefficient.DmolesidealGasEnthalpy.Dtemperature??heatOfVaporization.Dtemperature??surfaceTension.Dpressure??entropy.DmolFraction??volume@@@@entropy??heatCapacity.Dpressure??gibbsFreeEnergy.Dtemperature??compressibilityFactorfugacityCoefficient logFugacityCoefficient.Dpressureviscosity.Dpressure??idealGasEnthalpy??entropy.Dmoles?? heatCapacity?? fugacityCoefficient.DtemperatureactivityCoefficient.Dpressure activityCoefficient.DmolFraction"compressibilityFactor.DmolFraction viscosity????heatOfVaporization.Dmoles??excessEnthalpy.Dmoles??volume.Dtemperature@@@@fugacity.Dmoles?? / moldensity.Dtemperature?@?@heatCapacity.Dmoles??activity.DpressurecompressibilityFactor.DmolesexcessEnthalpy.DmolFraction??@&{779B2C7A-F54B-4A1D-B345-7FA14B889642}Outlet temperature?? Heat duty?? Pressure drop??TotalMassBalancePropertiesFraction?? TotalFlowMass??&{5E216BDD-C82F-45FE-830C-61FDDD2D9BC7} Pressure drop??&{BD25A684-3814-4212-84CD-76D752E106EE} Pressure drop??Pressure?? Heat duty?? Temperature??&{429DC999-9073-4549-8647-BA72D6BE7931}Pressure increase??Pressure?? Energy demand??&{74475174-0CAC-48E0-93D5-90276104D854}Pressure difference??Pressure??DbubblePointPressurebubblePointTemperaturecompressibilityFactor"compressibilityFactor.Dtemperature"compressibilityFactor.DmolFractioncompressibilityFactor.Dpressuredensitydensity.Dtemperaturedensity.DmolFractiondensity.DpressuredewPointPressuredewPointTemperatureenthalpyenthalpy.Dtemperatureenthalpy.DmolFractionenthalpy.Dpressureentropyentropy.Dtemperatureentropy.DmolFractionentropy.Dpressurefugacityfugacity.Dtemperaturefugacity.DmolFractionfugacity.DpressurefugacityCoefficient fugacityCoefficient.Dtemperature fugacityCoefficient.DmolFractionfugacityCoefficient.DpressureheatOfVaporizationheatOfVaporization.DtemperatureheatOfVaporization.DmolFractionheatOfVaporization.DpressureidealGasEnthalpyidealGasEnthalpy.DtemperaturelogFugacityCoefficient#logFugacityCoefficient.Dtemperature#logFugacityCoefficient.DmolFraction logFugacityCoefficient.DpressuresurfaceTensionsurfaceTension.DtemperaturesurfaceTension.DmolFractionsurfaceTension.DpressurethermalConductivity thermalConductivity.Dtemperature thermalConductivity.DmolFractionthermalConductivity.Dpressure vaporPressurevaporPressure.Dtemperature viscosityviscosity.Dtemperatureviscosity.DmolFractionviscosity.Dpressurevolumevolume.Dtemperaturevolume.DmolFractionvolume.DpressurecompressibilityFactor.Dmolesdensity.Dmolesenthalpy.Dmolesentropy.Dmolesfugacity.DmolesfugacityCoefficient.DmolesheatOfVaporization.DmoleslogFugacityCoefficient.DmolessurfaceTension.DmolesthermalConductivity.Dmolesviscosity.Dmoles volume.DmolesVapor Rosen CavettVaporLiquid Rosen CavettLiquid VaporLiquiddefaultdefault material template Rosen Cavett S1----- default,=AI t@%5@X?'ؚ?o?)?`'?8p?}ۢKɃ?kic?V{?BF?IcUb?0?3r?a*V?EL`?b??'ؚ?o?*?aSeq?~5|5P? i ?oE?i#$z?'2?]Ӱ\~?6D]>'?9p?ۢKɃ?lic?V{?BF?IcUb?0?3r?a*V?EL`?b?f`&^R?|A9?n!_? n$q?S?\b ?=S?tC?F8Ҡ?mq?S?G&`{?FO?mP?&>?8[?S3w?[kO?F^ފ?-Q?M<4?o?G\ ?U?$gS?ò*?LT %?3x?_)Y?/ Dΰ? {?'*w?2P1>%>> default@4>mUA-ns@~E @Fh?(Cx?3qC?T@4b?AAIaջ?ƪ2?y4%? ?c?)3ml?UYo?l?+d?Ε!p?ݐu?hzq?- z?XdaZ?Kq:p?hjD?#r;^??'6^|5?ˤ/>ղse?؞F>>m<>5J'>ߖ?P:}-?Lκ?c0??(Cx?3qC?T@4b?CAIaջ?Ǫ2?y4%? ?c?*3ml?UYo?l?+d?ϕ!p?ݐu?hzq?. z?XdaZ?Kq:p?ijD?#r;^??)6^|5?ˤ/>ֲse?ڞF>>m<>6J'>ߖ?Q:}-?Lκ?d0?pKv?mUA3C-ns@7}?C`)?rKv?k2N]l?zb k?wk̟?r?XC&?-[?bPɷ^?x 3Or!?t ݩ?[XU?am'=?#~D?d Њ?f ?gQ?@8? v^P?Q=b?ҿUGɥ?aky?@?5񌛂6d?D(0|?`- A?v2\?69m5?e#R?\xI?N1?]dV,%?`JҔ ?RQc?T Qml?&Yo?a> ?b?5R!p?tp[u?Dzq?YWz?aZ?)[n:p?iL}D?1;^?b_?nx5?ΠƤ/>e?F>$x>!<>"d?~-?_ͺ?0??rKv?o2N]l?{b k?wk̟?r?\C&?/[?bPɷ^?y 3Or!?t ݩ?[XU?em'=?#~D?h Њ?f ?kQ?@8? v^P?R=b?ԿUGɥ?cky?@?6񌛂6d?D(0|?a- A?v2\?69m5?e#R?\xI?N1?]dV'? p?hIɃ?5ic?N{?xYBF?,x`Ub? 0??Rm?O*V?EU_?Nb??'^R? zF9?U!_?% n$q?MǸS?cWc ?S?+!tC?Z 8Ҡ?אq??v`{?KFO?㦐mP??a&[?VYw?\kO?sފ?^Q?7<4??oG\ ?xU?g~e?D_Q?^| "?zrYܡ?i}?31qSG?ف״?%%X>5]?h4?i0튛?,S?zOY&r?}ve?Ή7?ruI?f}t?icF?~g?[ F?\R?Z؁?]Vc?=3Q?o ZL89?5=?#_Cq?!*I ?rx?ޣ ?:=?ڿס?'sZȫ?ϸ?INB? f?8TS?pS'?ey?I&57v?yֈ?J?I ?{?tw?RZ?mھ?0螢?Ky ?*a-?9Q?ʇ>x?#92?TfU?c "{?@1?;n?&d?ӡ`k?)Ž?EH$??WSL??W㔷6?eԚ Y?pbk?w?>z?1s`9? @?ie?`Ǚ?U[?_ ?Rr?)Ȅ?KNQ?Wh?&6?{:Q?JZ'#?vm]+?-8pl?^?MsN?$4?V8?gA6,?_3?f?]x#>OaX? b.%I1?{l??x@G?jӓ1?噩?ۣhe?)GUJ?-+ ;?D|]?񎋯?qHR]?\#?˫?7m? ?\ &k?2N??[c/Pݼ?eF?~0?tC2?&?8*?}o?n!?nKSj?ET3? 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_BPressurePressure?IpA _B Heat spec.Operation type Temperature Heat duty Heat duty TemperatureEnergy inlet streamVapor fraction Heat duty Heat duty@?@Gئԙ@ _ _B Temperature Temperature?IIKs@ _B TPOutletFlashTP Flash at outletThermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Vapor fractionFlash vapor fraction̜H|?? 3-phase flash?3-phase flash: additional outlet port for lightest liquid phaseLast run+++ specifications +++ Pressure: 439196.211998392 Pa Temperature: 308.705555555556 K +++ optional parameters +++ Pressure drop: 0 Pa Heat duty: 1653.16293442005 W Vapor fraction: 0.288835705828377 '1 $not all material ports are connectedInletVaporLiquid   ?@$@@@@@@@@@@@@ @@ @ @ @@ @ @@ @ @@ @ @@ @@@?@333333?@@FL4=Flash - seperate input stream into vapor and remaining phases%8BvRCOUSCOUS0002 Pressure spec.Operation typePressure Pressure drop Pressure dropPressure Pressure drop Pressure drop? _BPressurePressure?mFPA _B Heat spec.Operation type Temperature Heat duty Heat duty TemperatureEnergy inlet streamVapor fraction Heat duty Heat duty@?@rܓ@ _ _B Temperature Temperature?ق-؂r@ _B TPOutletFlashTP Flash at outletThermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Vapor fractionFlash vapor fractionEJ?? 3-phase flash?3-phase flash: additional outlet port for lightest liquid phaseLast run+++ specifications +++ Pressure: 190984.851999301 Pa Temperature: 302.594444444444 K +++ optional parameters +++ Pressure drop: 0 Pa Heat duty: 1271.20012835428 W Vapor fraction: 9.48886438042674E-02 )40> $not all material ports are connected Inlet Vapor Liquid   ?@$@@@@@@@@@@@@ @@ @ @ @@ @ @@ @ @@ @ @@ @@@?@333333?@ @@CP1@Compressor - unit increasing the pressure due to the work input.ɝBsIEGr־y1COUSCOUS0002Pressure spec.Operation typePressurePressure increasePressure increasePressure Energy spec.Operation type Efficiency Efficiency Energy demand EfficiencyEnergy specification streamPressure increasePressure increase?2ef'KA _BPressurePressure?@4>mUAj@ _B Energy demand Energy demand@?@4\@@xDIsentropic efficiencyIsentropic efficiency???Thermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Last run+++ specifications +++ Pressure: 5617160.97197944 Pa Isentropic efficiency: 0.75 +++ optional parameters +++ Pressure increase: 3654222.79998662 Pa Energy demand: 18800.8276260151 W Isentropic efficiency: 0.75  $not all material ports are connectedInletOutlet@@@K(^&?033333??033333?@@:t= @@?:t= @@?:t= @@@M26Mixer - mix 2 or more inlet streams to a single outletk!^/E a-COUSCOUS0002Number of inletsNumber of inlet ports Pressure drop Pressure drop? 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֧8@+,?q1v*/5@ٟ?@?@?@CP2@Compressor - unit increasing the pressure due to the work input.ɝBsIEGr־y1COUSCOUS0002Pressure spec.Operation typePressurePressure increasePressure increasePressure Energy spec.Operation type Efficiency Efficiency Energy demand EfficiencyEnergy specification streamPressure increasePressure increase?1@7A _BPressurePressure?,=Aj@ _B Energy demand Energy demand@?@[Sy@@xDIsentropic efficiencyIsentropic efficiency???Thermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Last run+++ specifications +++ Pressure: 1962938.17199281 Pa Isentropic efficiency: 0.75 +++ optional parameters +++ Pressure increase: 1523741.95999442 Pa Energy demand: 11564.9520363334 W Isentropic efficiency: 0.75  $ $not all material ports are connectedInletOutlet@@:t= @@@033333??033333?K(^&?@@?:t= @@?:t= @@ Mixer_1016Mixer - mix 2 or more inlet streams to a single outletk!^/E a-COUSCOUS0002Number of inletsNumber of inlet ports Pressure drop Pressure drop? _BThermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Last runD+++ specifications +++ Number of inlets: 3 Pressure drop: 0 Pa # $not all material ports are connected Inlet 2Inlet 3Inlet 1 Outlet0@@@@@@@ @Compressor_102@Compressor - unit increasing the pressure due to the work input.ɝBsIEGr־y1COUSCOUS0002Pressure spec.Operation typePa PressurePressure increasePressure increasePressure Energy spec.Operation typespec Efficiency Efficiency Energy demand EfficiencyEnergy specification streamPressure increasePressure increase?%4GLA _BPressurePressure?IpAj@ _B Energy demand Energy demand@?@@@xDIsentropic efficiencyIsentropic efficiency???Thermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Last run+++ specifications +++ Pressure: 439196.211998392 Pa Isentropic efficiency: 0.75 +++ optional parameters +++ Pressure increase: 248211.359999092 Pa Energy demand: 1326.37780791624 W Isentropic efficiency: 0.75 &,*0 $not all material ports are connected InletOutlet@@@:t= @033333?@033333??@K(^&?@?:t= @@?:t= @@ Valve_1031Valve - generates power from pressure difference.tQGt HՐ'aT COUSCOUS0002Pressure spec.Operation typePressurePressure differencePressure differencePressurePressure differencePressure difference?2ef'KA _BPressurePressure?,=Aj@ _BThermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Last run+++ specifications +++ Pressure: 1962938.17199281 Pa +++ optional parameters +++ Pressure difference: 3654222.79998662 Pa  $not all material ports are connectedInletOutlet0@@@@@?MS Sans -C6?-C6?h㈵>-C6?}