FSD100MbP?h㈵>c2dfffffr@ϼ@Harry Kooijman and Ross TaylorMethanol_iecr49p6150 =ChemSep{Adapted from Luyben et al., Ind. Eng. Chem. Res. (2010) 49 pp. 6150-6163 Methanol synthesis from syngas. Note that this flowsheet uses fixed conversion rates in the reactor whereas the original publication uses rate equations. Note that the temperature of the vapor overhead recycle of the methanol column is very dependent on the flowrate and thermodynamic model selection. Restoring flowsheet from file !Loaded Methanol_iecr49p6150.fsd _x temperaturepressure compositionflow ie100323dAUwNA\tPP ie100323dProperty pack for said article.ư>MbP?MbP?MbP?K-C:\Program Files (x86)\COCO\data\ChemSep1.pcdYCarbon monoxideCOCO630-08-0 [C+]#[O-] @3`@8JAfշ? ?=jT@ Q@ Q@@`<@ۡ?= ?=@ W9?A@7Z`|YA0)A 8<ް%C@H 8 8 8`B;@ Q@;@1?`@? 8QQ@p`@i`9$E@`f,` de?@zP@p`@e_`A~? /Կ? 8QQ@`@jЕxmGU@`?`f'@O@d@yv@_0?Q@`@@-K@@Q@ir?H(I@p@`9?j0@4,N/@?pP@Ą@hT@37@?u,@{2@ Q@k`@e 1T>cz?~Z@ l 8 Q@@f !<οg3 'gpCY@P@@_@-D?`?`N@=k@ 8Q@p@f݁`@D %7?`4 Q@Q0`@@zD@(?`"f>I@@@d 8 8 8 8 8 8 8 N4@2@ 8 8tH?٬?@%?VCarbon 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@TSrh?}ͺ? 8 8?`f:@I?[_/ @`}g@ 8 W?`?PHydrogenH2H2 1333-74-0[H][H]JQ@@4A k??c4@`f+@`f+@4@ @@?˿b=@ y? A@@ 8Ӭ 8 8 8 8 8,@@ ?Q@@s? 8+@@ @@i*@-bXh?4?@(*@Q@@ej7AE @ @r`f+@ \O@@jb@+s`mjt=WA<`f+@@3s7@dW@`fQc@ ?+@@@%@`@ 4't?g@o@p@? $J@ j>ி`0@z@hC@tSX@ӫ@=i@+@@@e >0?s `@ 8`f+@@@fտg3`q8 S?.,+@?@ e??*@N? 8$@@fyj@? ]9>cD`f+@@ @@@I"@jH`> 8Y@@@ 8 8 8 8 8 8 8n2@Q(a@ H3? 8 8 4@#=@ jM#^SJ9 8 8+@@@ MSt?@HztbX9@@U0???@v? 8+HͿ`r?_?@I?@Px?@z@@?B?@f(>@?@?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˿$@ u7?&eN@_@`?6?@^?@3@@^r@ 8I@@@f@d5X@Ֆ3?`7@3O@̌_@@@`]\AC? P`>4AI@@@d 8 8 8 8 8 8 8zt4@V@@ 8 8S@ ;\@ \@Cqd? 8 8@3O@@_@ QkwjA@R빍bX9@?rh?rh?= ?`@`? 8ZT?`?@"???2@`֡?lD @֜W@0?`?JMethaneCH4CH474-82-8Cg@6QA=?M?=[@jV@jV@@ 0@L2?+?9=@ u?*AWđTA,A 8@@@-P$ 8 8`f&7@)V@M? ;6?g@p ? 8 V@Gg@iCF@(U?@T@g@e kAq@@ʡ@`_@V@g@j1@@`.@?@M6@@V@d@@ tH oͿ8b?p-V@g@@K2@"@b?@̧I@p@?Т9Ͽ]?yٿY@p@hF@]@31@ V@g@e >o?\@ 8V@@@fp??G?/وվ)V@f@`cU>X?L`^@ 8Q[@@fפ'@}iv@7(>V@$h@@ΧR`TR?`{2Yx>I@@@d 8 8 8 8 8 8 8t4@,@S? 8 8@ \@ _e@ n ⑘@> 8 8 V@g@ 6@`frp@Q:@eFpAO?| :? :`fq@=:@j)hp࣐a@MоI =@33 @`fq@d0q@@a@eпf'?q@@3@@/@`0;@@`3c?I@@@4?`6l2vG)@`fq@@@h`f`@@Qx2@`T@q@@ 9@e@r>?`ff@ 8`q@Đ@f}@ K? R?sq@@3Ƀ@`1>P? /M@> 8`q@Đ@fJ@d@l v?ϧp@8@@fA`? k !@6l>I@@@d 8 8 8 8 8 8 8f7@&@B 8 8tx@@3@ ZWt l> 8 8q@@ 9@ :#J{#Q@\yf8TBfm?w-! b=@p?`ff???`X@B?`i?8? AN?έ?`? ?Q8*@ ?@1(@8@y ?(?B?gMethanolCH3OHCH4O67-56-1COM@:^A?5?@?@ u@@ e@@ e@ {?@`@@ڤ?z?`T=@9`%;?VA3Y@H ALHA 8`•>@W 8 8 8dd@̔e@6??@? 8@ e@q@i`f^@@3.`U>@@ e@@e(A?-??@ e@@3 @j@3Ɍ@o2w?>9@@3c@d@̘@_?@@ e@y@ @3s-@ 1&@@qO?@הY@p@L0hC@?W@R`fq@p@h|@@ @vо@@ e@u@e Q> bJ?כi@M8@ 8n@@@f @O*@ڊ2`_b@z@K> C? [@@ 8q@b@f2@@@@qP?¾q@`fr@@#@@ M]h?58`U!>I@@@d 8 8 8 8 8 8 8Z7@ƫ@ ݔB 8 8`f>s@|@ @*? 8 8@ e@u@ 㥛 u@ X4?#~jL|sj1@G?G?Q?@?@֤?@?ۿ`?6?!S? k??@?@ڤ?D @z@)Տ?@?֤?compressibilityFactorcompressibilityFactordensitydensity enthalpyenthalpy enthalpyF enthalpyFentropyentropy!entropyFentropyFfugacityfugacityfugacityCoefficientfugacityCoefficientgibbsFreeEnergy gibbsEnergyGG heatCapacityheatCapacityCpKKidealGasEnthalpyidealGasEnthalpy logFugacityCoefficientlogFugacityCoefficientmolecularWeightmolecularWeightHHHsurfaceTensionsurfaceTensionsurfaceTension (pure)surfaceTension (pure)thermalConductivitythermalConductivity04thermalConductivity (pure)thermalConductivity (pure)RS vaporPressure vaporPressureN viscosity viscosity& viscosity (pure)viscosity (pure)" volumevolumeVapor Vapor phaseLiquid Liquid phase A oŏ1?Methanol/Water p61 1/1aimported from NRTL.IPDoŏ1?Methanol/Water p61 1/1aimported from NRTL.IPD] {Gz?Carbon dioxide/carbon dioxideimported from HAYDENO.IPD333333?Water/carbon dioxideimported from HAYDENO.IPD333333?Carbon dioxide/methanolimported from HAYDENO.IPD333333?Water/carbon dioxideimported from HAYDENO.IPD333333? Water/waterimported from HAYDENO.IPD?Water/methanolimported from HAYDENO.IPD333333?Carbon dioxide/methanolimported from HAYDENO.IPD?Water/methanolimported from HAYDENO.IPDGz?Methanol/methanolimported from HAYDENO.IPDiI&†?*Hydrogen/Carbon Monoxide T=68.2-88.2K p215imported from PR.IPDL7A`?&Nitrogen/Carbon Monoxide T=83.82K p265imported from PR.IPDQ?Carbon Monoxide/Methane p353imported from PR.IPD47ĿHydrogen/Carbon Dioxide p242imported from PR.IPDAǘ-Nitrogen/Carbon Dioxide T=223.15-273.15K p306imported from PR.IPD:M?1Methane/Carbon Dioxide T=173-220K P=26-66bar p398imported from PR.IPD o_y?$Carbon Dioxide/Water T=523-623K p633imported from PR.IPDI +?'Carbon Dioxide/Methanol T=213-247K p621imported from PR.IPDI&†?*Hydrogen/Carbon Monoxide T=68.2-88.2K p215imported from PR.IPD47ĿHydrogen/Carbon Dioxide p242imported from PR.IPD߾3? Hydrogen/Nitrogen T=90-113K p210imported from PR.IPD c?!Hydrogen/Methane T=90.3-127K p219imported from PR.IPDL7A`?&Nitrogen/Carbon Monoxide T=83.82K p265imported from PR.IPDAǘ-Nitrogen/Carbon Dioxide T=223.15-273.15K p306imported from PR.IPD߾3? Hydrogen/Nitrogen T=90-113K p210imported from PR.IPDj+?%Nitrogen/Methane T=88.71-188.71K p285imported from PR.IPDk g˿Nitrogen/Methanol p340imported from PR.IPDQ?Carbon Monoxide/Methane p353imported from PR.IPD:M?1Methane/Carbon Dioxide T=173-220K P=26-66bar p398imported from PR.IPD c?!Hydrogen/Methane T=90.3-127K p219imported from PR.IPDj+?%Nitrogen/Methane T=88.71-188.71K p285imported from PR.IPD o_y?$Carbon Dioxide/Water T=523-623K p633imported from PR.IPD g곿Methanol/Water p730imported from PR.IPDI +?'Carbon Dioxide/Methanol T=213-247K p621imported from PR.IPDk g˿Nitrogen/Methanol p340imported from PR.IPD g곿Methanol/Water p730imported from PR.IPD (\?Carbon monoxide/Methanolimported from UNIQUACP.IPDq= ף#@Hydrogen/Waterimported from UNIQUACP.IPDQ@Hydrogen/Methanolimported from UNIQUACP.IPDGz@Nitrogen/Waterimported from UNIQUACP.IPDHydrogen/Waterimported from UNIQUACP.IPD@Nitrogen/Waterimported from UNIQUACP.IPDGzX@Methanol/Waterimported from UNIQUACP.IPD@@Carbon monoxide/Methanolimported from UNIQUACP.IPD@k@Hydrogen/Methanolimported from UNIQUACP.IPDfffffIMethanol/Waterimported from UNIQUACP.IPD†W2Methanol/Water p730imported from SRK.IPD†W2Methanol/Water p730imported from SRK.IPD†W2Methanol/Water p730imported from SRK.IPD†W2Methanol/Water p730imported from SRK.IPDH}8?Methanol/Waterimported from VANLAAR.IPD?ܵ?Methanol/Waterimported from VANLAAR.IPD:M?Methanol/Waterimported from MARGULES.IPDH?Methanol/Waterimported from MARGULES.IPDPgkYn@Methanol/Waterimported from WILSON.IPD-QY@Methanol/Waterimported from WILSON.IPD\Ux@Methanol/Water p61 1/1aimported from NRTL.IPD4ЄWMethanol/Water p61 1/1aimported from NRTL.IPD u`Iq@Methanol/Water (Kojima+Kato)imported from UNIQUAC.IPDG} o8eMethanol/Water (Kojima+Kato)imported from UNIQUAC.IPDH2OCH3OHH2Oq= ףp?ffffff?kt2@CH3OH?x?L7A`@@r@fH2OCH2OHH2Oq= ףp?ffffff?kt2@CH3ͪ?A`"? rh.@OH?333333?5^I 1@ffffffu@^P@$@{G<@33333t@ V瞯< ie100323dNew Reaction PackagebKrx-NJ ie100323dReaction pack for said article.-C:\Program Files (x86)\COCO\data\ChemSep1.pcdCarbon monoxide630-08-0Carbon monoxideCO`<@Carbon dioxide124-38-9Carbon dioxideCO2@7F@Hydrogen 1333-74-0HydrogenH2 @Nitrogen 7727-37-9NitrogenN2<@Methane74-82-8MethaneCH4 0@Water 7732-18-5WaterH2O2@Methanol67-56-1MethanolCH4O@`@@CO->MeOHVapor? CO2->MeOHVapor?? ie100323d630-08-0Carbon monoxide`<@=jT@CO ie100323dCarbon monoxide124-38-9Carbon dioxide@7F@CO2 ie100323dCarbon dioxide 1333-74-0Hydrogen @c4@H2 ie100323dHydrogen 7727-37-9Nitrogen<@`fVS@N2 ie100323dNitrogen74-82-8Methane 0@=[@CH4 ie100323dMethane 7732-18-5Water2@`fRw@H2O ie100323dWater67-56-1Methanol@`@@@ u@CH4O ie100323dMethanol ????????????thermalConductivity.Dmoles?? / molgibbsFreeEnergy.Dpressure??enthalpyF.DmolFraction??viscosity.Dtemperature???? thermalConductivity.Dtemperature??thermalConductivity.Dpressure??enthalpyF.Dpressure??heatCapacity.DmolFraction??entropyF.Dmoles??enthalpy.Dmoles??density.Dpressure?@?@molecularWeight#logFugacityCoefficient.DmolFractionentropy.Dtemperature??viscosity.Dmoles???? / mol volume.Dmoles@@@@ enthalpyF??enthalpy??vaporPressure.Dtemperature??fugacity.Dtemperature??volume.Dpressure@@@@surfaceTension.DmolFraction??fugacityCoefficient.Dmoles / molgibbsFreeEnergy??gibbsFreeEnergy.DmolFraction??"compressibilityFactor.DtemperaturecompressibilityFactor.Dpressureenthalpy.DmolFraction??logFugacityCoefficiententhalpy.Dpressure??molecularWeight.Dtemperature fugacityCoefficient.DmolFractionfugacity.Dpressurevolume.DmolFraction@@@@density?@?@enthalpyF.Dtemperature??surfaceTension.Dtemperature??thermalConductivity??entropyF.DmolFraction??surfaceTension??density.DmolFraction?@?@heatCapacity.Dtemperature??#logFugacityCoefficient.Dtemperatureviscosity.DmolFraction????fugacityCoefficient.DpressuresurfaceTension.Dmoles?? / molentropy.Dpressure??enthalpy.Dtemperature??gibbsFreeEnergy.Dmoles?? thermalConductivity.DmolFraction??density.Dmoles?@?@ / mollogFugacityCoefficient.Dmoles / molidealGasEnthalpy.Dtemperature??surfaceTension.Dpressure??enthalpyF.Dmoles??entropyF.Dtemperature??entropy.DmolFraction??volume@@@@entropyF??entropy??molecularWeight.DpressureheatCapacity.Dpressure??gibbsFreeEnergy.Dtemperature??compressibilityFactorfugacityCoefficientviscosity.Dpressure?? logFugacityCoefficient.DpressureidealGasEnthalpy?? heatCapacity?? fugacityCoefficient.DtemperatureentropyF.Dpressure??entropy.Dmoles?? viscosity????"compressibilityFactor.DmolFractionvolume.Dtemperature@@@@fugacity.Dmoles?? / moldensity.Dtemperature?@?@heatCapacity.Dmoles??molecularWeight.DmolFractioncompressibilityFactor.Dmoles / molmolecularWeight.Dmoles / mol@ &{429DC999-9073-4549-8647-BA72D6BE7931}Pressure increase??Pressure?? Energy demand??Isentropic efficiency?TotalMassBalancePropertiesFraction? TotalFlowMass??&{779B2C7A-F54B-4A1D-B345-7FA14B889642}Outlet temperature?? Heat duty?? Pressure drop??&{5E216BDD-C82F-45FE-830C-61FDDD2D9BC7} Pressure drop??&{7A1D05E4-54D2-483F-8BC8-3D4D2DA1897E} Temperature?? Heat exchange?? Heat transfer??Pressure drop stream 1??Pressure drop stream 2?? Tolerance?&{71F5AC07-65A1-4357-8F1B-A8CD58148763}RelativePerturbationTemperature?RelativePerturbationPressure?PerturbationComposition?Temperature profile??Pressure profile??Vapour Flow profile??Liquid Flow profile??Duties profile??Vapour Density profile@?@?Vapour Viscosity profile????Vapour Heat capacity profile??#Vapour Thermal conductivity profile??Liquid Density profile@?@?Liquid Viscosity profile????Liquid Heat capacity profile??Liquid Thermal cond. profile??Surface tension profile??&{603DF4B9-4F88-475D-A458-85F56125DA70} Pressure drop?? Temperature?? Heat duty??,Conversion Carbon monoxide reaction CO->MeOH?,Conversion Carbon dioxide reaction CO2->MeOH?&{BD25A684-3814-4212-84CD-76D752E106EE} Pressure drop??Pressure?? Heat duty?? Temperature??Vapor fraction?&{33C43C04-EDAD-41A9-A952-62CDDCF67932} Split factors? Pressure drop??&{74475174-0CAC-48E0-93D5-90276104D854}Pressure difference??Pressure??XidealGasEnthalpyidealGasEnthalpy.Dtemperature vaporPressurevaporPressure.DtemperaturecompressibilityFactorcompressibilityFactor.Dmoles"compressibilityFactor.DmolFractioncompressibilityFactor.Dpressure"compressibilityFactor.Dtemperaturedensitydensity.Dmolesdensity.DmolFractiondensity.Dpressuredensity.Dtemperatureenthalpyenthalpy.Dmolesenthalpy.DmolFractionenthalpy.Dpressureenthalpy.Dtemperature enthalpyFenthalpyF.DmolesenthalpyF.DmolFractionenthalpyF.DpressureenthalpyF.Dtemperatureentropyentropy.Dmolesentropy.DmolFractionentropy.Dpressureentropy.DtemperatureentropyFentropyF.DmolesentropyF.DmolFractionentropyF.DpressureentropyF.Dtemperaturefugacityfugacity.Dmolesfugacity.DmolFractionfugacity.Dpressurefugacity.DtemperaturefugacityCoefficientfugacityCoefficient.Dmoles fugacityCoefficient.DmolFractionfugacityCoefficient.Dpressure fugacityCoefficient.DtemperaturegibbsFreeEnergygibbsFreeEnergy.DmolesgibbsFreeEnergy.DmolFractiongibbsFreeEnergy.DpressuregibbsFreeEnergy.Dtemperature heatCapacityheatCapacity.DmolesheatCapacity.DmolFractionheatCapacity.DpressureheatCapacity.DtemperaturelogFugacityCoefficientlogFugacityCoefficient.Dmoles#logFugacityCoefficient.DmolFraction logFugacityCoefficient.Dpressure#logFugacityCoefficient.DtemperaturemolecularWeightmolecularWeight.DmolesmolecularWeight.DmolFractionmolecularWeight.DpressuremolecularWeight.DtemperaturethermalConductivitythermalConductivity.Dmoles thermalConductivity.DmolFractionthermalConductivity.Dpressure thermalConductivity.Dtemperature viscosityviscosity.Dmolesviscosity.DmolFractionviscosity.Dpressureviscosity.Dtemperaturevolume volume.Dmolesvolume.DmolFractionvolume.Dpressurevolume.DtemperaturesurfaceTensionsurfaceTension.DmolessurfaceTension.DmolFractionsurfaceTension.DpressuresurfaceTension.DtemperaturebubblePointTemperaturebubblePointPressuredewPointTemperaturedewPointPressureVapor Vapor phase ie100323dVaporLiquid Liquid phase ie100323dLiquid VaporLiquiddefaultdefault material template ie100323dSyngas rkson\SudefaultSAfffff2t@rq٨@fA@Af?p'>-j=?oŏ?n*?6-j=?oŏ?n*?6-j=?oŏ?n*?6-j=?oŏ?n*?6-j=?oŏ?n*?6g`>z\}4?OI?add>/>)o`&Ed>r؁o>Е5>2X;ۼ><3?"?249BA9B9AAB defaultdAhzDv@rq٨@fA@Af?p'>-j=?oŏ?n*?6-j=?oŏ?n*?6%E >.>+|'z?b_?ww>B->%>%櫙> +Q72?_"?yf {U?xV-H?X9v?Ts??M'+>(E >0>+|'z?b_?ww>E->%>%櫙> +Q72?a"?zf {U?xV-H?Z9v?Ws?`̐L> / +=E?D?"AR! ?A$>0 I=+LdW.>+>le~vM>3.Y>em?Y"]`?%uO?k?l?CzS?%E >.>+|'z?b_?ww>B->%>%櫙> +Q72?_"?yf {U?xV-H?X9v?Ts??M'+>%E >.>+|'z?b_?ww>B->%>%櫙> +Q72?_"?yf {U?xV-H?X9v?Ts?27D0BA&AD0D0A0AB defaultdA,HCs@" @h@P _@ Kt?ՉK?hiz>gd?IIj?-gC\ ? ȶ?^Ѥ?S*?=??Q7V?9?HB?{{?5>#i?? 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D/Qu?*?211Sn S  S S defaultdA33333@CYZ @p1=n?d@?굜?OK1?1~$nb?UO.V?‡?!?#@آ?b0ISF;?Q/2?m??:4?H^?\???굜?OK1?1~$nb?UO.V?‡?!?#@آ?b0ISF;?Q/2?m??:4?H^?\?212Wd#W"Wd#WW#d# defaulthdA輄{@+Bm @p?d@?]/?)n]b?V?c'[?"?o[آ?,C;?8 BG$?:R?M̘?~<4?z^????]/?)n]b?V?c'[?"?o[آ?,C;?8 BG$?:R?M̘?~<4?z^??213h#m=t-h#t=h#t#t=m= default1PdAfffffrs@+Bm @p?d@?]/?)n]b?V?c'[?"?o[آ?,C;?8 BG$?:R?M̘?~<4?z^??p`?O?6??(?F!?tɏ?#?s_< ({?&c^?T7eG?236?!v@?b"/x?wx??Nå;?jm$":?#/?2cs?XsHq?b/3?!3|.K?8>iKAJ?Wdﺉ?!YUA{?!R?[? hy?K&??HpZ??]L??>db??._{X??eh??$Gɡh?fffffs@cA98@qF^b@214i8i5i7i5i8i8i5 default2PdA7_cfrs@x5Ӿ@"7_@ ?*5?k򶿵?4]v'?~!?fh?)k?>*&{?TX?MkcG?Tzf36?_t@?F$x?*C?? ?*5?k򶿵?4]v'?~!?fh?)k?>*&{?TX?MkcG?Tzf36?_t@?F$x?*C?A^Շ;?aa":?L# /?b n?vNq?`ؑ/3?Ѻ(K?ZLDAJ?꺉?la;{?jN?Z? ?Y:(?2Ventk/..k./k/k.. default2PdA7_cfrs@pC5m@SҳX@ ?*5?k򶿵?4]v'?~!?fh?)k?>*&{?TX?MkcG?Tzf36?_t@?F$x?*C?? ?*5?k򶿵?4]v'?~!?fh?)k?>*&{?TX?MkcG?Tzf36?_t@?F$x?*C?d16g/_.d._.g/g/g._. default2PdA7_cfrs@GI@3W _@ ?*5?k򶿵?4]v'?~!?fh?)k?>*&{?TX?MkcG?Tzf36?_t@?F$x?*C?? ?*5?k򶿵?4]v'?~!?fh?)k?>*&{?TX?MkcG?Tzf36?_t@?F$x?*C?217[.J.S.J.[.[.J. defaultdAM=s@GI@3W _@ ?*5?k򶿵?4]v'?~!?fh?)k?>*&{?TX?MkcG?Tzf36?_t@?F$x?*C?? ?*5?k򶿵?4]v'?~!?fh?)k?>*&{?TX?MkcG?Tzf36?_t@?F$x?*C?219iBcHiHcBiHiBiHcH CalcEquilibrium failed: CalcEquilibrium failed: CalcEquilibrium failed: PVF flash failed: Trivial solution for equilibrium calculation default2PdAF_cfrs@ m@:A@Ԇ;?T~":?"S# /?Gk n?4Nq?56S/3?r6(K? 8AJ?0꺉?;{?qN?juZ?k?V=<(?5== ?5?X?t.)'?M!?ܛ?l]l?%3&{?7SX?ipcG?ʹw36?t@?{x?XR?2?sx;??{":?yL# /?c] n?Nq?z/3?[(K?AJ?-꺉?B;{?N? Z?K!?>(?220YCX2Y:X2YCYCY2X2 defaultjA&5Ges@2!5DN@)?riT΀?Gt}? M?~6T?,f^u?Ͼu?MGҐ?Y.!S? lV?0D}1?v2{G?r? +1ӿ?Ԯ??qiT΀?Gt}? M?}6T?,f^u?Ͼu?LGҐ?X.!S?lV?0D}1?u2{G?r? +1ӿ?Ԯ?(.>r)>qu?6W?=‰v>Vè>:%#>A 2g>6> -?3}Ax ?(-?סFл?E?7BD?221T2J2O2J2T2T2J2 defaultdAp$@2!5DN@)?riT΀?Gt}? M?~6T?,f^u?Ͼu?MGҐ?Y.!S? lV?0D}1?v2{G?r? +1ӿ?Ԯ??riT΀?Gt}? M?~6T?,f^u?Ͼu?MGҐ?Y.!S? lV?0D}1?v2{G?r? +1ӿ?Ԯ?2F1YM7<CK7<YNYMYNCNC<7<  defaultjA&5Ges@0}z@J13@@{{>$>Oqu?QW?/‰v>Vè>ae,%#> 2g>ȍ -?SuAx ?h-?VHл??!D?ExqT΀?RGt}?͚M?.1T?)Pf^u?u?GҐ? S?l3DV?}1??%|G?Jr?7,1ӿ????}{>$>Oqu?QW?/‰v>Vè>ce,%#> 2g>ʍ -?SuAx ?i-?VHл??!D?2Water)NNNN)N)NN &p@fdefaultAoQaw@?1h@9~Ke @7rok;=p ;E4;o}I;\%u;yHIP;z% r;hi;H.?<?-C6?2,O'??w?ƭkO?k\??H.?<?-C6?2,O'?dMethanol)0000)0)00 defaultj@JBu@XKH@{JT=@M'+>%E >.>+|'z?b_?ww>C->%>%櫙> +Q72?_"?yf {U?xV-H?X9v?Ts??M'+>(E >0>+|'z?b_?ww>F->%>%櫙> +Q72?a"?zf {U?xV-H?Z9v?Ws?`̐L> / +=E?D?"AR! ?A$>0 I=+LdW.>+>le~vM>3.Y>em?Y"]`?%uO?k?b28`H\H^H\H`H`H\H defaultjA='5Ges@ m@:A@Ԇ;?T~":?"S# /?Gk n?4Nq?56S/3?r6(K? 8AJ?0꺉?;{?qN?juZ?k?V=<(?H?7T΀?Gt}?ƳM?3T?]]~f^u?q̻u?GҐ?>*!S?DhV??}1?t{G?Nr?@+1ӿ?߮?BΟ~[?Ū>AJ>Rqu?MW?_2‰v>Vè>.+%#>ޓ2g> -?tAx ?H-?EHл??+D?2 Compressor_1@Compressor - unit increasing the pressure due to the work input.ɝBsIEGr־y1COUSCOUS0002Pressure spec.Type of pressure specificationPressurePressure increasePressure increasePressure Energy spec.Type of energy specification Efficiency Efficiency Energy demand EfficiencyEnergy specification streamPressure increaseCompressor pressure increase??o(BA _BPressureCompressor outlet pressure?7\Aj@ _B Energy demand!Energy consumed by the compressor@?@z8QA@xDIsentropic efficiency6Isentropic efficiency at which the compressor operates???Thermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++ Pressure: 7500000 Pa Isentropic efficiency: 0.75 +++ optional parameters +++ Pressure increase: 2380000 Pa Energy demand: 4624609.92161026 W Isentropic efficiency: 0.75  # $not all material ports are connectedInletOutlet@@?K(^&? @? @@?:t= @@?:t= @@?:t= @@?:t= @@?:t= @@@solving Compressor_1 HeaterCooler_2MHeaterCooler - heat or cool stream specifying heat duty or outlet temperaturez,wKJEKB COUSCOUS0002TypeType of heat duty specification Temperature Heat duty Heat duty Temperature Energy inletOutlet temperature!Temperature of the product stream?fffffrs@r@ _B Heat duty Heat duty@?@5A`W@x@xD Pressure dropPressure drop along the unit?? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++ Heat duty: -6128269.02363344 W Pressure drop: 0 Pa +++ optional parameters +++ Outlet temperature: 311.15 K * . $not all material ports are connectedInletOutlet B4twp0tw   (8B4twp0tw   (8B4twp0tw   (8B4twp0tw   (8@@ ɿ@????@@@@@ɿ@@@solving HeaterCooler_2 Compressor_3@Compressor - unit increasing the pressure due to the work input.ɝBsIEGr־y1COUSCOUS0002Pressure spec.Type of pressure specificationPressurePressure increasePressure increasePressure Energy spec.Type of energy specification Efficiency Efficiency Energy demand EfficiencyEnergy specification streamPressure increaseCompressor pressure increase??JA _BPressureCompressor outlet pressure?dAj@ _B Energy demand!Energy consumed by the compressor@?@loQA@xDIsentropic efficiency6Isentropic efficiency at which the compressor operates???Thermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++ Pressure: 11000000 Pa Isentropic efficiency: 0.75 +++ optional parameters +++ Pressure increase: 3500000 Pa Energy demand: 4472805.74233548 W Isentropic efficiency: 0.75 5 9 $not all material ports are connectedInletOutlet@@?K(^&? @? @@?:t= @@?:t= @@?:t= @@?:t= @@?:t= @@@solving Compressor_3 Compressor_4@Compressor - unit increasing the pressure due to the work input.ɝBsIEGr־y1COUSCOUS0002Pressure spec.Type of pressure specificationPressurePressure increasePressure increasePressure Energy spec.Type of energy specification Efficiency Efficiency Energy demand EfficiencyEnergy specification streamPressure increaseCompressor pressure increase??CdA _BPressureCompressor outlet pressure?dAj@ _B Energy demand!Energy consumed by the compressor@?@ @@@xDIsentropic efficiency6Isentropic efficiency at which the compressor operates???Thermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++ Pressure: 11000000 Pa Isentropic efficiency: 0.75 +++ optional parameters +++ Pressure increase: 10900000 Pa Energy demand: 4582.81348470413 W Isentropic efficiency: 0.75  $ $not all material ports are connectedInletOutlet@@?K(^&? @? @@?:t= @@?:t= @@?:t= @@?:t= @@?:t= @@@Mixer_56Mixer - mix 2 or more inlet streams to a single outletk!^/E a-COUSCOUS0002Number of inletsNumber of inlet ports Pressure dropPressure drop along the mixer?? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last runD+++ specifications +++ Number of inlets: 3 Pressure drop: 0 Pa BH $not all material ports are connectedInlet 1Inlet 2Inlet 3Outlet0@@@@@@@ @HeatExchanger_6;HeatExchanger - transfers heat from a hot to a cold stream.zT?H=M-~L COUSCOUS0002 Type#Type of heat transfer specification Temperature Heat transfer Heat exchange Temperature Heat transferMax. heat transfer TemperatureTemperature of outlet stream 1?gffff"z@ _B Heat exchange/Heat transferred from hot stream to cold stream@?@ϳA@xD Heat transfer8Heat transferred from hot stream to cold stream per area@?@r]4A@xDModeOperation modecounter-currentcounter-current co-currentcounter-currentPressure drop stream 1Pressure drop along stream 1??j@ _BPressure drop stream 2Pressure drop along stream 2??i@ _BAdapt outlet temperaturesEContinues calculation with limiting outlet temperatures if necessary.Thermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1 Tolerance4Relative termination tolerance on iterative solution-C6?-C6?|=?Maximum iterations/Maximum iterations to obtain iterative solutiondd Last runY+++ specifications +++ Pressure drop stream 1: 100000 Pa Pressure drop stream 2: 50000 Pa Temperature: 418.15 K Adapt outlet temperatures: true Tolerance: 0.0001 Maximum iterations: 100 +++ solution +++ +++ optional parameters +++ Heat exchange: 43932414.5877988 W Heat transfer: 362112.551138989 W/K Mode: counter-current O[ $not all material ports are connectedInlet1 Inlet2Outlet1 Outlet2   ?(@@@@@@$@$@@$@@ $@@$@@$@@$@@$@@@ @HeaterCooler_7MHeaterCooler - heat or cool stream specifying heat duty or outlet temperaturez,wKJEKBCOUSCOUS0002TypeType of heat duty specification Temperature Heat duty Heat duty Temperature Energy inletOutlet temperature!Temperature of the product stream?fffffrz@r@ _B Heat duty Heat duty@?@cY[BA@x@xD Pressure dropPressure drop along the unit??i@ _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++ Heat duty: 2406088.84538561 W Pressure drop: 50000 Pa +++ optional parameters +++ Outlet temperature: 423.15 K dh $not all material ports are connectedInlet Outlet 8 xw%swsw[(88 xw%swsw[(88 xw%swsw[(88 xw%swsw[(8@@ ɿ@????@@@@@ɿ@@@ReactorGFixedConversionReactor - perform reactions using a specified conversion=`O]GXa%pCOUSCOUS0002 Pressure dropPressure drop over the reactor??i@ _BHeat duty typeType of heat duty specification Isothermal Isothermal Isothermal Heat duty Energy inlet TemperatureReactor effluent temperature?33333@r@ _B Heat dutyReactor heat duty@?@Ǔ{ _ _B Enthalpy TypeEnthalpy calculation type Use EnthalpyF Use EnthalpyF Use EnthalpyF"Use Enthalpy (no heat of reaction)!Use Enthalpy and heat of reactionThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1CO->MeOHCarbon monoxide|Gz? CO2->MeOHCarbon dioxide(\?Last run+++ specifications +++ Using enthalpyF in enthalpy calculations Heat duty type: Isothermal Temperature: 540.15 K Pressure drop: 100000 Pa +++ optional parameters +++ Heat duty: -28916856.5362831 W s $not all material ports are connected ie100323d Inlet Outlet  @@ @@ @@ @@ @@!@@HeaterCooler_9MHeaterCooler - heat or cool stream specifying heat duty or outlet temperaturez,wKJEKBCOUSCOUS0002TypeType of heat duty specification Temperature Heat duty Heat duty Temperature Energy inletOutlet temperature!Temperature of the product stream?fffffrs@r@ _B Heat duty Heat duty@?@Շ@x@xD Pressure dropPressure drop along the unit??i@ _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++ Heat duty: -100180291.774402 W Pressure drop: 50000 Pa +++ optional parameters +++ Outlet temperature: 311.15 K d!h% $not all material ports are connected Inlet Outlet 8 xw%swswXi(88 xw%swswXi(88 xw%swswXi(88 xw%swswXi(8@@ ɿ@????@@@@@ɿ@@@ HP Separator=Flash - separate input stream into vapor and remaining phases%8BvR COUSCOUS0002 Pressure spec.#Type of pressure drop specification Pressure drop Pressure drop Pressure dropPressure Pressure dropPressure drop over the flash?? _BPressurePressure inside the flash?2PdA _BFlash specification6Heat dury, temperature or vapor fraction specification Heat duty Heat duty Heat duty TemperatureEnergy inlet streamVapor fraction Heat dutyFlash heat duty@?@ _ _B TemperatureFlash temperature?F_cfrs@ _BTP Outlet FlashDPerform a T-P flash at outlet (TRUE) or P-VF flash at outlet (FALSE)Thermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Vapor fractionFlash vapor fractionto`?? 3-phase flash?3-phase flash: additional outlet port for lightest liquid phaseLast run+++ specifications +++ Pressure drop: 0 Pa Heat duty: 0 W +++ optional parameters +++ Pressure: 10650000 Pa Vapor fraction: 0.900070398034547 Temperature: 311.14999711169 K f8mB $not all material ports are connected Inlet VaporLiquid  @$@@@$@@ @$@@@$@@@$@@?@@@333333?@@%@@)@pmessage: TEA warning: PVF inside-out flash failed: Post-flash fugacity mismatch. Converged to invalid solution message: WARNING: Flash HP Separator: temperature post-check failed for liquid product (temperature deviation too high). Using TP flash. Splitter_119Splitter - split input stream in number of output streams<3ARby2COUSCOUS0002Number of outletsNumber of outlet ports Split factors!Split factors for (n - 1) outletsI +?? Pressure drop Pressure drop along the splitter?? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run_+++ specifications +++ Number of outlets: 2 Split factors: [ 0.022] Pressure drop: 0 Pa f/l5 $not all material ports are connected InletOutlet1Outlet20@@@@@@@@ Compressor_12@Compressor - unit increasing the pressure due to the work input.ɝBsIEGr־y1COUSCOUS0002Pressure spec.Type of pressure specificationPressurePressure increasePressure increasePressure Energy spec.Type of energy specification Efficiency Efficiency Energy demand EfficiencyEnergy specification streamPressure increaseCompressor pressure increase??\A _BPressureCompressor outlet pressure?dAj@ _B Energy demand!Energy consumed by the compressor@?@W7,T1A@xDIsentropic efficiency6Isentropic efficiency at which the compressor operates???Thermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++ Pressure: 11000000 Pa Isentropic efficiency: 0.75 +++ optional parameters +++ Pressure increase: 349999.999999993 Pa Energy demand: 1135660.02819397 W Isentropic efficiency: 0.75 [,_0 $not all material ports are connectedInletOutlet@@@:t= @033333?@033333??@K(^&?@?:t= @@?:t= @@?:t= @@?:t= @@Mixer_136Mixer - mix 2 or more inlet streams to a single outletk!^/E a-COUSCOUS0002Number of inletsNumber of inlet ports Pressure dropPressure drop along the mixer?? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last runD+++ specifications +++ Number of inlets: 2 Pressure drop: 0 Pa D-J3 $not all material ports are connectedInlet 1Inlet 2Outlet0@@@@@@@Flash_14=Flash - separate input stream into vapor and remaining phases%8BvR COUSCOUS0002 Pressure spec.#Type of pressure drop specification Pressure drop Pressure drop Pressure dropPressure Pressure dropPressure drop over the flash?? _BPressurePressure inside the flash?jA _BFlash specification6Heat dury, temperature or vapor fraction specification Heat duty Heat duty Heat duty TemperatureEnergy inlet streamVapor fraction Heat dutyFlash heat duty@?@ _ _B TemperatureFlash temperature?xb&5Ges@ _BTP Outlet FlashDPerform a T-P flash at outlet (TRUE) or P-VF flash at outlet (FALSE)Thermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Vapor fractionFlash vapor fraction0eH?? 3-phase flash?3-phase flash: additional outlet port for lightest liquid phaseLast run+++ specifications +++ Pressure drop: 0 Pa Heat duty: 0 W +++ optional parameters +++ Pressure: 200000 Pa Vapor fraction: 0.0513312224176822 Temperature: 310.329884672108 K VC]M $not all material ports are connectedInletVaporLiquid   @$@@@@@@@@@@@@@ @@ @@ @ @@ @ @@ @ @@ @ @@ @?@@@333333?@@@333333?@@@333333?@@@333333?@ @(@ Compressor_15@Compressor - unit increasing the pressure due to the work input.ɝBsIEGr־y1COUSCOUS0002Pressure spec.Type of pressure specificationPressurePressure increasePressure increasePressure Energy spec.Type of energy specification Efficiency Efficiency Energy demand EfficiencyEnergy specification streamPressure increaseCompressor pressure increase??odA _BPressureCompressor outlet pressure?dAj@ _B Energy demand!Energy consumed by the compressor@?@Bf3A@xDIsentropic efficiency6Isentropic efficiency at which the compressor operates???Thermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++ Pressure: 11000000 Pa Isentropic efficiency: 0.75 +++ optional parameters +++ Pressure increase: 10800000 Pa Energy demand: 1271315.72757802 W Isentropic efficiency: 0.75 T0X4 $not all material ports are connectedInletOutlet@@@:t= @033333?@033333??@K(^&?@?:t= @@?:t= @@?:t= @@?:t= @@C1ChemSep Unit OperationqeWCXc CSUOl[ChemSep] Version=6.90 Compiled=2012-1-31 20:40 41769b34bc6e Name=C:\windows\profiles\harry\Temp\CS_1~JPE.sep Title=ChemSep CO Unit Operation "C1" in COFE Flowsheet User=harry Date=2012-02-05 Time=13:29:36 [Cape-Open] unitname=C1 CO_ID=CS_17_34_1CCE401_D0B4ECC0 7 components Carbon monoxide 630-08-0 28.0100002289 Mw Carbon dioxide 124-38-9 44.0094985962 Mw Hydrogen 1333-74-0 2.01588010788 Mw Nitrogen 7727-37-9 28.013999939 Mw Methane 74-82-8 16.0429992676 Mw Water 7732-18-5 18.0149993896 Mw Methanol 67-56-1 32.0419998169 Mw 1 thermo exe=C:\Program Files\ChemSepL\bin\co-col2.exe mode=COFE NoWarnings=TRUE WilsonEstimate=TRUE Status= 0 only K-values and ethalpies 0 use only perturbed derivative 0 use only perturbed mole derivative 0.001 relative T perturbation 0.001 relative P perturbation 0.001 X perturbation 0 write all values to log 0 use initial guess 0 inlet reflash 3 outlet reflash 0 expose energy ports 0 clear log 0 update icon CO Thermo Version=Auto 2 number of run levels normal simplified 1 current run level [Paths] Device drivers path=c:\program files\chemsepl\bin\ Help and Info path=c:\program files\chemsepl\help\ Component data path=c:\program files\chemsepl\pcd\ Property data path=c:\program files\chemsepl\ipd\ Section data path=c:\program files\chemsepl\ild\ Executables path=C:\Program Files\ChemSepL\bin\ Temporary path=C:\windows\profiles\harry\Temp\ Scripts path=c:\program files\chemsepl\bin\ [Units] Temperature=K Flow=kmol/h Mass flow=kg/s Pressure=bar Heat=J/s Enthalpy=J/kmol Entropy=J/kmol/K Fraction=_ Length=m 1/Length=1/m Area=m2 Volume=m3 Mass=kg Angle=rad Velocity=m/s Surface tension=N/m Density=kg/m3 Molar density=kmol/m3 Viscosity=N/m2.s Molecular weight=kg/kmol Heat capacity=J/kmol/K Thermal conductivity=J/s/m/K Diffusivity=m2/s Interaction parameter=J/mol Time=s [Components] 7 5 908 Library Offset, Index DT=2012-01-31,09:17:24 CHK=61212 CAS=630-08-0 CID=Carbon monoxide Name=Carbon monoxide Lib=c:\program files\chemsepl\pcd\chemsep1.pcd 6 909 Library Offset, Index DT=2012-01-31,09:17:24 CHK=62069 CAS=124-38-9 CID=Carbon dioxide Name=Carbon dioxide Lib=c:\program files\chemsepl\pcd\chemsep1.pcd 13 902 Library Offset, Index DT=2012-01-31,09:17:24 CHK=38624 CAS=1333-74-0 CID=Hydrogen Name=Hydrogen Lib=c:\program files\chemsepl\pcd\chemsep1.pcd 21 905 Library Offset, Index DT=2012-01-31,09:17:24 CHK=45277 CAS=7727-37-9 CID=Nitrogen Name=Nitrogen Lib=c:\program files\chemsepl\pcd\chemsep1.pcd 31 1 Library Offset, Index DT=2012-01-31,09:17:24 CHK=21170 CAS=74-82-8 CID=Methane Name=Methane Lib=c:\program files\chemsepl\pcd\chemsep1.pcd 14 1921 Library Offset, Index DT=2012-01-31,09:17:24 CHK=26350 CAS=7732-18-5 CID=Water Name=Water Lib=c:\program files\chemsepl\pcd\chemsep1.pcd 32 1101 Library Offset, Index DT=2012-01-31,09:17:24 CHK=37880 CAS=67-56-1 CID=Methanol Name=Methanol Lib=c:\program files\chemsepl\pcd\chemsep1.pcd [Operation] 2 Operation Column 11 Operation kind Complex Column 3 Condenser Partial (Vapour product) 1 Reboiler Partial (Liquid product) 42 Stages 1 Feed stages 1 Sidestream stages F=27 S=1 0 Pumparound stages P= [Properties] 350 BIP estimation temperature [Thermodynamics] 4 K model DECHEMA 6 1 Activity coefficient NRTL * Wilson model * * UNIQUAC model * * Equation of State * * Cubic EOS * * Virial EOS * 1 Vapour pressure Antoine 0 Henry's law * Henry's default * [Enthalpy] 3 Enthalpy Excess 1 Enthalpy reference state Vapour 298.15 Enthalpy reference temperature 1 Formation enthalpies Excluded 298.15 Exergy surroundings temperature [Physical property models] 0 No Check T range * Cubic EOS * * Virial EOS * * Vapour model * * Liquid mixture density * * Liquid component density * * Vapour mixture viscosity * * Vapour mixture viscosity pressure correction * * Vapour component viscosity * * Liquid mixture viscosity * * Liquid component viscosity * Vapour mixture Cp * Vapour component Cp * Liquid mixture Cp * Liquid component Cp * Vapour mixture conductivity * * Vapour component conductivity * * Liquid mixture conductivity * * Liquid component conductivity * Mixture surface tension * * Component surface tension * * Vignes MS D-model * * D mixture model * * Vapour Diffusion Coefficients * [Property Data] [NRTL Data] i j Aij Aji aij Component Component 1 2 0 0 1 Carbon monoxide/Carbon dioxide 1 3 0 0 1 Carbon monoxide/Hydrogen 1 4 0 0 1 Carbon monoxide/Nitrogen 1 5 0 0 1 Carbon monoxide/Methane 1 6 0 0 1 Carbon monoxide/Water 1 7 0 0 1 Carbon monoxide/Methanol 2 3 0 0 1 Carbon dioxide/Hydrogen 2 4 0 0 1 Carbon dioxide/Nitrogen 2 5 0 0 1 Carbon dioxide/Methane 2 6 0 0 1 Carbon dioxide/Water 2 7 0 0 1 Carbon dioxide/Methanol 3 4 0 0 1 Hydrogen/Nitrogen 3 5 0 0 1 Hydrogen/Methane 3 6 0 0 1 Hydrogen/Water 3 7 0 0 1 Hydrogen/Methanol 4 5 0 0 1 Nitrogen/Methane 4 6 0 0 1 Nitrogen/Water 4 7 0 0 1 Nitrogen/Methanol 5 6 0 0 1 Methane/Water 5 7 0 0 1 Methane/Methanol 6 7 3317.083 -790.9722 0.2999 Water/Methanol [Reaction data] 0 Number of reactions [Specifications] Top Bottom [Heaters/Coolers] 0 Number 0 Column duty Qcolumn 2 First stage 41 Last stage 0 Qcolumn lost to surroundings [Efficiencies] 1 Default efficiency 0 Number [Pressures] 2 Column pressure Bottom & top pressures 100000 Condenser pressure 100000 Top pressure * Pressure Drop 140000 Bottom pressure [Feeds] 1 Number 1 Feed state T & p 27 Stage Feed1{split} 310.329884674 Temperature 200000 Pressure 0 Vapour fraction 7 componentflows 1.94122904388e-006 Component 1 flow 0.00587590046222 Component 2 flow 1.30498279075e-005 Component 3 flow 7.4403229865e-006 Component 4 flow 0.000253690632327 Component 5 flow 0.199695962375 Component 6 flow 0.91287941875 Component 7 flow [SideStreams] 1 Number 1 Stage Sidestream1 1 Phase Vapour 2 Specification Total flow 0.000185833 Value [Condenser] 7 Type Mole fraction of a component 0.992 Value Qcondenser 7 1st comp. 1 Type Reflux ratio 0.5 Initialization guess [Reboiler] 7 Type Mole fraction of a component 0.0001 Value Qreboiler 7 1st comp. 1 Type Boilup ratio 0.5 Initialization guess [Monitored Variables] * [Solve options] 1 Initialization Automatic 3 Method 2-pass ideal H first 0.5 Flow Step limit 10 Temperature Step limit 1 Composition Step limit 1 Flux Step limit 0.000001 Accuracy 30 Maximum iterations 1 Iteration count & function vector 0 T/V/L profiles 0 X/Y profiles 0 Variable and function vectors 0 Jacobian 1 History Screen History file= 1 Feeds type Stage below 1 Interactive 0 Log thermodynamics 0 Log enthalpy/entropy 0 Log physical properties 0 Log timing 0 CO numeric differencing 0 Log from iteration 0 CS K-value 0 CS enthalpy 0 CS entropy 0 CS flash 0 CS activity coefficient 0 CS vapor pressuure 0 CS density 0 CS viscosity 0 CS thermal conductivity 0 CS heat capacity 0 CS surface tension 0 CS diffusivity [Programs] Temporary file=SCRATCH.TMP User program= 8 DOS extender NT 1 Show windows Hidden [FlowSheet] [CoCo] [Settings] ComboBox=ComboBox14 -1 ComboBox=ComboBox20 -1 ComboBox=ComboBox21 -1 CheckBox=CheckBox3 0 Show settings CheckBox=CheckBox1 1 Auto colors CheckBox=CheckBox2 1 Auto points Edit=Edit9 0.2 StringGrid=StringGrid5 2 8 Title Labels Stages Axis color Commands Box Labels box Import data StringGrid=StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 y1 x2 y2 StringGrid=StringGrid3 1 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage CheckBox=CheckBox10 0 Show settings ComboBox=ComboBox22 6 ComboBox=ComboBox23 5 StringGrid=StringGrid7 16 2 Title McCabe-Thiele diagram Methanol - Water Xlabel X Methanol/(Methanol+Water) Ylabel Y Methanol/(Methanol+Water) X interval 0.2 Y interval 0.2 X min 0 X max 1 Y min 0 Y max 1 X tics 0 Y tics 0 Axis color Black Grid Off y Fractions Vertical Commands set label "ChemSep" at 1,0.02 right Stage numbers On StringGrid=StringGrid11 5 3 CheckBox=CheckBox45 0 Lumped ComboBox=ComboBox75 -1 ComboBox=ComboBox76 -1 ComboBox=ComboBox77 -1 Edit=Edit55 0.95 Edit=Edit56 0.95 Edit=Edit57 1.2 Edit=Edit1 1 CheckBox=CheckBox2 0 Use old results CheckBox=CheckBox3 1 Automatic CheckBox=CheckBox1 0 Keep sep-files CheckBox=CheckBox4 1 Restore original StringGrid=StringGrid1 1 6 Name Variable Units Value Start/Valuelist End StringGrid=StringGrid2 4 1 Name Variable Units Current Value StringGrid=StringGrid3 1 1 None ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Title ComboBox=ComboBox4 0 ComboBox=ComboBox15 0 Edit=Edit17 Plot font CheckBox=CheckBox2 1 Color=Edit18 3404024 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 3404024 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 3404024 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 3404024 SpinEdit=SpinEdit3 1 ComboBox=ComboBox14 0 RadioButton=RadioButton3 TRUE DrawSetColors=BVLEcolors 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 ComboBox=ComboBox7 -1 ComboBox=ComboBox11 -1 ComboBox=ComboBox6 -1 Memo=Memo1 Memo1, ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox4 0 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Ternary Phase Diagram Edit=Edit4 27 Edit=Edit6 Edit=Edit7 chemsep1.pcd Edit=Edit8 Edit=Edit5 StringGrid=StringGrid1 8 7 Identifier L# File Loc. CAS SMILES Name Carbon monoxide 908 c:\program files\chemsepl\pcd\chemsep1.pcd 5 630-08-0 [C+]#[O-] Carbon monoxide Carbon dioxide 909 c:\program files\chemsepl\pcd\chemsep1.pcd 6 124-38-9 O=C=O Carbon dioxide Hydrogen 902 c:\program files\chemsepl\pcd\chemsep1.pcd 13 1333-74-0 [H][H] Hydrogen Nitrogen 905 c:\program files\chemsepl\pcd\chemsep1.pcd 21 7727-37-9 N#N Nitrogen Methane 1 c:\program files\chemsepl\pcd\chemsep1.pcd 31 74-82-8 C Methane Water 1921 c:\program files\chemsepl\pcd\chemsep1.pcd 14 7732-18-5 O Water Methanol 1101 c:\program files\chemsepl\pcd\chemsep1.pcd 32 67-56-1 CO Methanol 0 0 ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 Edit=Edit3 21 Edit=Edit4 Binary Property Diagram Memo=Memo1 StringGrid=StringGrid1 13 4 Axis Left Right X/Y Property -click to select- -click to select- x Title x Units - Minimum 0 Maximum 1 Interval 0.2 Grid Off Off Off Log Off Off Off Color Blue Red Black Line Normal Normal Style Solid Solid Point None None Edit=Edit5 ComboBox=ComboBox7 -1 ComboBox=ComboBox6 -1 [End Settings] [End of Input] [Results] 1 Converged 12 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow Duties 1 337.2914594 1.000000000E+05 9.200355059E-01 8.235170029E-01 -2.922124988E+07 2 337.3976322 1.000000000E+05 1.743738342E+00 8.228276123E-01 0.000000000E+00 3 337.6814468 1.010000000E+05 1.743048951E+00 8.226123088E-01 0.000000000E+00 4 337.9657604 1.020000000E+05 1.742833648E+00 8.223659212E-01 0.000000000E+00 5 338.2513531 1.030000000E+05 1.742587260E+00 8.220873240E-01 0.000000000E+00 6 338.5385172 1.040000000E+05 1.742308663E+00 8.217742392E-01 0.000000000E+00 7 338.8275535 1.050000000E+05 1.741995578E+00 8.214242847E-01 0.000000000E+00 8 339.1187754 1.060000000E+05 1.741645624E+00 8.210349860E-01 0.000000000E+00 9 339.4125090 1.070000000E+05 1.741256325E+00 8.206037824E-01 0.000000000E+00 10 339.7090923 1.080000000E+05 1.740825121E+00 8.201280349E-01 0.000000000E+00 11 340.0088759 1.090000000E+05 1.740349374E+00 8.196050360E-01 0.000000000E+00 12 340.3122215 1.100000000E+05 1.739826375E+00 8.190320209E-01 0.000000000E+00 13 340.6195022 1.110000000E+05 1.739253360E+00 8.184061818E-01 0.000000000E+00 14 340.9311012 1.120000000E+05 1.738627521E+00 8.177246838E-01 0.000000000E+00 15 341.2474106 1.130000000E+05 1.737946023E+00 8.169846838E-01 0.000000000E+00 16 341.5688305 1.140000000E+05 1.737206023E+00 8.161833521E-01 0.000000000E+00 17 341.8957671 1.150000000E+05 1.736404691E+00 8.153178974E-01 0.000000000E+00 18 342.2286304 1.160000000E+05 1.735539236E+00 8.143855946E-01 0.000000000E+00 19 342.5678322 1.170000000E+05 1.734606933E+00 8.133838177E-01 0.000000000E+00 20 342.9137825 1.180000000E+05 1.733605157E+00 8.123100764E-01 0.000000000E+00 21 343.2668864 1.190000000E+05 1.732531415E+00 8.111620580E-01 0.000000000E+00 22 343.6275389 1.200000000E+05 1.731383397E+00 8.099376760E-01 0.000000000E+00 23 343.9961200 1.210000000E+05 1.730159015E+00 8.086351252E-01 0.000000000E+00 24 344.3729878 1.220000000E+05 1.728856464E+00 8.072529457E-01 0.000000000E+00 25 344.7584704 1.230000000E+05 1.727474285E+00 8.057900964E-01 0.000000000E+00 26 345.1528564 1.240000000E+05 1.726011435E+00 8.042460407E-01 0.000000000E+00 27 345.5563834 1.250000000E+05 1.724467380E+00 2.033580070E+00 0.000000000E+00 28 345.8612188 1.260000000E+05 1.835074006E+00 2.034813080E+00 0.000000000E+00 29 346.0766682 1.270000000E+05 1.836307015E+00 2.035578639E+00 0.000000000E+00 30 346.2927970 1.280000000E+05 1.837072575E+00 2.036242048E+00 0.000000000E+00 31 346.5174928 1.290000000E+05 1.837735983E+00 2.036679016E+00 0.000000000E+00 32 346.7657294 1.300000000E+05 1.838172951E+00 2.036557633E+00 0.000000000E+00 33 347.0748456 1.310000000E+05 1.838051568E+00 2.035050572E+00 0.000000000E+00 34 347.5388949 1.320000000E+05 1.836544508E+00 2.030098920E+00 0.000000000E+00 35 348.3990242 1.330000000E+05 1.831592856E+00 2.016592017E+00 0.000000000E+00 36 350.2991376 1.340000000E+05 1.818085952E+00 1.982154447E+00 0.000000000E+00 37 355.0502892 1.350000000E+05 1.783648383E+00 1.905846197E+00 0.000000000E+00 38 365.9645997 1.360000000E+05 1.707340132E+00 1.825540019E+00 0.000000000E+00 39 377.3206642 1.370000000E+05 1.627033954E+00 1.814222260E+00 0.000000000E+00 40 381.1325306 1.380000000E+05 1.615716195E+00 1.816821667E+00 0.000000000E+00 41 381.9979671 1.390000000E+05 1.618315602E+00 1.817887452E+00 0.000000000E+00 42 382.3152839 1.400000000E+05 1.619381387E+00 1.985060647E-01 6.531711727E+07 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 0.1780084E+07 -0.3369172E+08 0.6143991E+04 -0.1047194E+06 2 0.1785597E+07 -0.3369417E+08 0.6062811E+04 -0.1046225E+06 3 0.1798475E+07 -0.3367623E+08 0.6062401E+04 -0.1044821E+06 4 0.1811327E+07 -0.3365960E+08 0.6065506E+04 -0.1043401E+06 5 0.1824190E+07 -0.3364432E+08 0.6071561E+04 -0.1041960E+06 6 0.1837075E+07 -0.3363046E+08 0.6080813E+04 -0.1040493E+06 7 0.1849990E+07 -0.3361811E+08 0.6093468E+04 -0.1038997E+06 8 0.1862945E+07 -0.3360735E+08 0.6109698E+04 -0.1037469E+06 9 0.1875949E+07 -0.3359828E+08 0.6129657E+04 -0.1035909E+06 10 0.1889015E+07 -0.3359099E+08 0.6153479E+04 -0.1034314E+06 11 0.1902150E+07 -0.3358558E+08 0.6181285E+04 -0.1032685E+06 12 0.1915367E+07 -0.3358216E+08 0.6213178E+04 -0.1031022E+06 13 0.1928677E+07 -0.3358082E+08 0.6249250E+04 -0.1029323E+06 14 0.1942090E+07 -0.3358167E+08 0.6289577E+04 -0.1027591E+06 15 0.1955619E+07 -0.3358482E+08 0.6334218E+04 -0.1025825E+06 16 0.1969273E+07 -0.3359039E+08 0.6383216E+04 -0.1024027E+06 17 0.1983066E+07 -0.3359847E+08 0.6436596E+04 -0.1022199E+06 18 0.1997008E+07 -0.3360918E+08 0.6494363E+04 -0.1020343E+06 19 0.2011111E+07 -0.3362263E+08 0.6556500E+04 -0.1018460E+06 20 0.2025387E+07 -0.3363891E+08 0.6622966E+04 -0.1016555E+06 21 0.2039845E+07 -0.3365813E+08 0.6693698E+04 -0.1014631E+06 22 0.2054497E+07 -0.3368038E+08 0.6768603E+04 -0.1012691E+06 23 0.2069353E+07 -0.3370575E+08 0.6847560E+04 -0.1010740E+06 24 0.2084421E+07 -0.3373432E+08 0.6930416E+04 -0.1008782E+06 25 0.2099710E+07 -0.3376613E+08 0.7016986E+04 -0.1006824E+06 26 0.2115227E+07 -0.3380125E+08 0.7107048E+04 -0.1004870E+06 27 0.2130976E+07 -0.3383970E+08 0.7200342E+04 -0.1002927E+06 28 0.2146253E+07 -0.3380888E+08 0.6990934E+04 -0.1002352E+06 29 0.2156235E+07 -0.3378640E+08 0.6950257E+04 -0.1001889E+06 30 0.2166161E+07 -0.3376551E+08 0.6918647E+04 -0.1001401E+06 31 0.2176327E+07 -0.3374800E+08 0.6894195E+04 -0.1000842E+06 32 0.2187187E+07 -0.3373870E+08 0.6886538E+04 -0.1000102E+06 33 0.2199866E+07 -0.3374968E+08 0.6919665E+04 -0.9989206E+05 34 0.2217190E+07 -0.3381109E+08 0.7050556E+04 -0.9967123E+05 35 0.2246355E+07 -0.3399854E+08 0.7406071E+04 -0.9923735E+05 36 0.2306313E+07 -0.3450223E+08 0.8230146E+04 -0.9849207E+05 37 0.2447525E+07 -0.3574034E+08 0.9825282E+04 -0.9795479E+05 38 0.2716898E+07 -0.3731975E+08 0.1151654E+05 -0.9924680E+05 39 0.2842950E+07 -0.3757407E+08 0.9600767E+04 -0.1002581E+06 40 0.2838715E+07 -0.3751443E+08 0.6939653E+04 -0.1005668E+06 41 0.2840759E+07 -0.3748509E+08 0.6013909E+04 -0.1006352E+06 42 0.2847126E+07 -0.3746560E+08 0.5769313E+04 -0.1006274E+06 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.3209510E+02 0.1144520E+01 0.1103817E-04 0.4683909E+05 0.1909413E-01 2 0.3205005E+02 0.1142554E+01 0.1102372E-04 0.4686107E+05 0.1910088E-01 3 0.3203703E+02 0.1152541E+01 0.1103427E-04 0.4686947E+05 0.1913030E-01 4 0.3202295E+02 0.1162462E+01 0.1104503E-04 0.4687653E+05 0.1943542E-01 5 0.3200751E+02 0.1172302E+01 0.1105591E-04 0.4688238E+05 0.1946802E-01 6 0.3199062E+02 0.1182055E+01 0.1106693E-04 0.4688693E+05 0.1950102E-01 7 0.3197216E+02 0.1191715E+01 0.1107811E-04 0.4689011E+05 0.1953444E-01 8 0.3195204E+02 0.1201275E+01 0.1108945E-04 0.4689183E+05 0.1956835E-01 9 0.3193013E+02 0.1210728E+01 0.1110099E-04 0.4689200E+05 0.1960279E-01 10 0.3190633E+02 0.1220066E+01 0.1111273E-04 0.4689053E+05 0.1963780E-01 11 0.3188050E+02 0.1229282E+01 0.1112470E-04 0.4688731E+05 0.1967345E-01 12 0.3185254E+02 0.1238367E+01 0.1113691E-04 0.4688225E+05 0.1970977E-01 13 0.3182231E+02 0.1247312E+01 0.1114939E-04 0.4687525E+05 0.1974683E-01 14 0.3178969E+02 0.1256110E+01 0.1116216E-04 0.4686620E+05 0.1978468E-01 15 0.3175455E+02 0.1264751E+01 0.1117523E-04 0.4685499E+05 0.1982338E-01 16 0.3171676E+02 0.1273226E+01 0.1118863E-04 0.4684152E+05 0.1986297E-01 17 0.3167620E+02 0.1281525E+01 0.1120238E-04 0.4682567E+05 0.1990353E-01 18 0.3163273E+02 0.1289639E+01 0.1121650E-04 0.4680735E+05 0.1994510E-01 19 0.3158624E+02 0.1297559E+01 0.1123101E-04 0.4678645E+05 0.1998775E-01 20 0.3153660E+02 0.1305275E+01 0.1124593E-04 0.4676286E+05 0.2003152E-01 21 0.3148372E+02 0.1312777E+01 0.1126128E-04 0.4673650E+05 0.2007647E-01 22 0.3142749E+02 0.1320058E+01 0.1127708E-04 0.4670726E+05 0.2012265E-01 23 0.3136781E+02 0.1327107E+01 0.1129334E-04 0.4667507E+05 0.2017011E-01 24 0.3130462E+02 0.1333918E+01 0.1131008E-04 0.4663985E+05 0.2021888E-01 25 0.3123785E+02 0.1340483E+01 0.1132732E-04 0.4660155E+05 0.2026902E-01 26 0.3116747E+02 0.1346796E+01 0.1134506E-04 0.4656012E+05 0.2032053E-01 27 0.3109346E+02 0.1352852E+01 0.1136331E-04 0.4651554E+05 0.2037346E-01 28 0.3105079E+02 0.1360603E+01 0.1135188E-04 0.4656106E+05 0.2040248E-01 29 0.3104811E+02 0.1370429E+01 0.1135911E-04 0.4657449E+05 0.2042610E-01 30 0.3104470E+02 0.1380206E+01 0.1136692E-04 0.4658592E+05 0.2045024E-01 31 0.3103749E+02 0.1389764E+01 0.1137524E-04 0.4659416E+05 0.2047582E-01 32 0.3102072E+02 0.1398779E+01 0.1138489E-04 0.4659466E+05 0.2050511E-01 33 0.3098017E+02 0.1406442E+01 0.1139795E-04 0.4657592E+05 0.2054387E-01 34 0.3088032E+02 0.1410725E+01 0.1141959E-04 0.4650930E+05 0.2060648E-01 35 0.3063278E+02 0.1406537E+01 0.1146284E-04 0.4632310E+05 0.2072931E-01 36 0.3001702E+02 0.1381094E+01 0.1156092E-04 0.4583645E+05 0.2100633E-01 37 0.2848817E+02 0.1302862E+01 0.1179840E-04 0.4458468E+05 0.2168529E-01 38 0.2492553E+02 0.1114126E+01 0.1229161E-04 0.4140557E+05 0.2319926E-01 39 0.2026255E+02 0.8848999E+00 0.1263609E-04 0.3664387E+05 0.2479472E-01 40 0.1843188E+02 0.8027173E+00 0.1265414E-04 0.3463135E+05 0.2533050E-01 41 0.1808134E+02 0.7913606E+00 0.1265519E-04 0.3423976E+05 0.2544483E-01 42 0.1802515E+02 0.7939173E+00 0.1266219E-04 0.3417837E+05 0.2548080E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.3199971E+02 0.7554502E+03 0.3453886E-03 0.9029290E+05 0.1929270E+00 0.1905582E-01 2 0.3197210E+02 0.7554057E+03 0.3452174E-03 0.9029616E+05 0.1938080E+00 0.1913772E-01 3 0.3194224E+02 0.7551504E+03 0.3443938E-03 0.9034353E+05 0.1947254E+00 0.1921180E-01 4 0.3190951E+02 0.7549061E+03 0.3435857E-03 0.9038777E+05 0.1957400E+00 0.1929531E-01 5 0.3187367E+02 0.7546728E+03 0.3427881E-03 0.9042885E+05 0.1968591E+00 0.1938888E-01 6 0.3183450E+02 0.7544516E+03 0.3419998E-03 0.9046655E+05 0.1980902E+00 0.1949322E-01 7 0.3179177E+02 0.7542434E+03 0.3412204E-03 0.9050063E+05 0.1994414E+00 0.1960906E-01 8 0.3174523E+02 0.7540493E+03 0.3404498E-03 0.9053087E+05 0.2009210E+00 0.1973716E-01 9 0.3169464E+02 0.7538706E+03 0.3396877E-03 0.9055700E+05 0.2025377E+00 0.1987830E-01 10 0.3163972E+02 0.7537087E+03 0.3389337E-03 0.9057874E+05 0.2043005E+00 0.2003331E-01 11 0.3158021E+02 0.7535651E+03 0.3381876E-03 0.9059582E+05 0.2062186E+00 0.2020303E-01 12 0.3151583E+02 0.7534415E+03 0.3374490E-03 0.9060794E+05 0.2083016E+00 0.2038829E-01 13 0.3144629E+02 0.7533399E+03 0.3367173E-03 0.9061478E+05 0.2105593E+00 0.2058998E-01 14 0.3137132E+02 0.7532623E+03 0.3359922E-03 0.9061602E+05 0.2130016E+00 0.2080897E-01 15 0.3129062E+02 0.7532110E+03 0.3352730E-03 0.9061132E+05 0.2156387E+00 0.2104614E-01 16 0.3120390E+02 0.7531886E+03 0.3345590E-03 0.9060034E+05 0.2184807E+00 0.2130237E-01 17 0.3111087E+02 0.7531978E+03 0.3338496E-03 0.9058271E+05 0.2215378E+00 0.2157854E-01 18 0.3101124E+02 0.7532417E+03 0.3331440E-03 0.9055808E+05 0.2248199E+00 0.2187548E-01 19 0.3090475E+02 0.7533236E+03 0.3324413E-03 0.9052606E+05 0.2283370E+00 0.2219403E-01 20 0.3079113E+02 0.7534471E+03 0.3317404E-03 0.9048629E+05 0.2320985E+00 0.2253494E-01 21 0.3067012E+02 0.7536161E+03 0.3310404E-03 0.9043839E+05 0.2361135E+00 0.2289895E-01 22 0.3054150E+02 0.7538348E+03 0.3303401E-03 0.9038199E+05 0.2403904E+00 0.2328670E-01 23 0.3040507E+02 0.7541077E+03 0.3296382E-03 0.9031672E+05 0.2449369E+00 0.2369875E-01 24 0.3026065E+02 0.7544395E+03 0.3289333E-03 0.9024226E+05 0.2497594E+00 0.2413554E-01 25 0.3010811E+02 0.7548351E+03 0.3282242E-03 0.9015826E+05 0.2548632E+00 0.2459737E-01 26 0.2994739E+02 0.7552998E+03 0.3275092E-03 0.9006445E+05 0.2602518E+00 0.2508441E-01 27 0.2977845E+02 0.7558388E+03 0.3267867E-03 0.8996059E+05 0.2659269E+00 0.2559658E-01 28 0.2977680E+02 0.7554705E+03 0.3257544E-03 0.9003904E+05 0.2659405E+00 0.2556921E-01 29 0.2977421E+02 0.7552267E+03 0.3249728E-03 0.9008972E+05 0.2660072E+00 0.2555518E-01 30 0.2976811E+02 0.7550038E+03 0.3242031E-03 0.9013620E+05 0.2661927E+00 0.2555254E-01 31 0.2975325E+02 0.7548252E+03 0.3234411E-03 0.9017402E+05 0.2666746E+00 0.2557763E-01 32 0.2971657E+02 0.7547557E+03 0.3226888E-03 0.9019059E+05 0.2678954E+00 0.2567157E-01 33 0.2962553E+02 0.7549619E+03 0.3219498E-03 0.9015423E+05 0.2709582E+00 0.2593666E-01 34 0.2939913E+02 0.7558908E+03 0.3212239E-03 0.8998492E+05 0.2786146E+00 0.2662699E-01 35 0.2883573E+02 0.7588562E+03 0.3204602E-03 0.8947711E+05 0.2977425E+00 0.2837165E-01 36 0.2743946E+02 0.7684249E+03 0.3192223E-03 0.8808779E+05 0.3454259E+00 0.3269621E-01 37 0.2420590E+02 0.8030550E+03 0.3143230E-03 0.8450644E+05 0.4573065E+00 0.4252813E-01 38 0.2001831E+02 0.8836617E+03 0.2916750E-03 0.7918951E+05 0.6070255E+00 0.5412899E-01 39 0.1838642E+02 0.9289866E+03 0.2648202E-03 0.7677701E+05 0.6693271E+00 0.5712468E-01 40 0.1807425E+02 0.9381954E+03 0.2566509E-03 0.7626448E+05 0.6818194E+00 0.5734123E-01 41 0.1802419E+02 0.9395224E+03 0.2548145E-03 0.7618370E+05 0.6838954E+00 0.5732375E-01 42 0.1801640E+02 0.9395734E+03 0.2540965E-03 0.7617514E+05 0.6842750E+00 0.5728501E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.210952405E-05 0.114299433E-05 0.112982044E-05 0.112994881E-05 0.113028666E-05 2 0.638531211E-02 0.341161770E-02 0.339345060E-02 0.339399470E-02 0.339472466E-02 3 0.141811838E-04 0.804041677E-05 0.780256760E-05 0.779754706E-05 0.780183678E-05 4 0.808536237E-05 0.438310716E-05 0.433161665E-05 0.433209381E-05 0.433340237E-05 5 0.275684362E-03 0.148425816E-03 0.147127652E-03 0.147149177E-03 0.147187575E-03 6 0.131462745E-02 0.214876481E-02 0.306314377E-02 0.406752593E-02 0.516872376E-02 7 0.992000000E+00 0.994277625E+00 0.993383014E+00 0.992378071E+00 0.991276098E+00 Component Mole fractions on stages: 6 to 10 1 0.113065033E-05 0.113103886E-05 0.113145396E-05 0.113189750E-05 0.113237138E-05 2 0.339552134E-02 0.339638869E-02 0.339733168E-02 0.339835551E-02 0.339946559E-02 3 0.780667863E-05 0.781173886E-05 0.781701831E-05 0.782253192E-05 0.782829580E-05 4 0.433481068E-05 0.433631448E-05 0.433792040E-05 0.433963553E-05 0.434146723E-05 5 0.147229066E-03 0.147273713E-03 0.147321738E-03 0.147373374E-03 0.147428863E-03 6 0.637383166E-02 0.769026443E-02 0.912574677E-02 0.106882978E-01 0.123862108E-01 7 0.990070146E+00 0.988752794E+00 0.987316313E+00 0.985752679E+00 0.984053593E+00 Component Mole fractions on stages: 11 to 15 1 0.113287759E-05 0.113341818E-05 0.113399526E-05 0.113461098E-05 0.113526752E-05 2 0.340066750E-02 0.340196703E-02 0.340337007E-02 0.340488268E-02 0.340651099E-02 3 0.783432674E-05 0.784064208E-05 0.784725969E-05 0.785419790E-05 0.786147537E-05 4 0.434342314E-05 0.434551114E-05 0.434773931E-05 0.435011592E-05 0.435264938E-05 5 0.147488458E-03 0.147552417E-03 0.147621007E-03 0.147694498E-03 0.147773167E-03 6 0.142280267E-01 0.162225025E-01 0.183785717E-01 0.207052978E-01 0.232118195E-01 7 0.982210507E+00 0.980214658E+00 0.978057108E+00 0.975728786E+00 0.973220547E+00 Component Mole fractions on stages: 16 to 20 1 0.113596709E-05 0.113671192E-05 0.113750422E-05 0.113834616E-05 0.113923986E-05 2 0.340826121E-02 0.341013954E-02 0.341215220E-02 0.341430527E-02 0.341660472E-02 3 0.786911103E-05 0.787712391E-05 0.788553301E-05 0.789435710E-05 0.790361448E-05 4 0.435534819E-05 0.435822087E-05 0.436127593E-05 0.436452173E-05 0.436796645E-05 5 0.147857294E-03 0.147947159E-03 0.148043039E-03 0.148145211E-03 0.148253943E-03 6 0.259072869E-01 0.288007866E-01 0.319012570E-01 0.352173897E-01 0.387575174E-01 7 0.970523234E+00 0.967627755E+00 0.964525163E+00 0.961206763E+00 0.957664213E+00 Component Mole fractions on stages: 21 to 25 1 0.114018738E-05 0.114119064E-05 0.114225142E-05 0.114337129E-05 0.114455158E-05 2 0.341905626E-02 0.342166532E-02 0.342443687E-02 0.342737538E-02 0.343048462E-02 3 0.791332277E-05 0.792349858E-05 0.793415716E-05 0.794531199E-05 0.795697428E-05 4 0.437161794E-05 0.437548361E-05 0.437957027E-05 0.438388400E-05 0.438842990E-05 5 0.148369492E-03 0.148492102E-03 0.148621996E-03 0.148759376E-03 0.148904408E-03 6 0.425294856E-01 0.465405054E-01 0.507969855E-01 0.553043392E-01 0.600667638E-01 7 0.953889663E+00 0.949875897E+00 0.945616500E+00 0.941106053E+00 0.936340357E+00 Component Mole fractions on stages: 26 to 30 1 0.114579331E-05 0.114709713E-05 0.516266519E-07 0.234194479E-08 0.107082812E-09 2 0.343376752E-02 0.343722598E-02 0.720161654E-04 0.152083055E-05 0.323721902E-07 3 0.796915245E-05 0.798185144E-05 0.100020105E-05 0.126328078E-06 0.160824751E-07 4 0.439321189E-05 0.439823243E-05 0.201856213E-06 0.933759407E-08 0.435379805E-09 5 0.149057225E-03 0.149217908E-03 0.507915940E-05 0.174257575E-06 0.602603862E-08 6 0.650869864E-01 0.703659739E-01 0.707179929E-01 0.708564310E-01 0.710983213E-01 7 0.931316681E+00 0.926034055E+00 0.929203658E+00 0.929141736E+00 0.928901624E+00 Component Mole fractions on stages: 31 to 35 1 0.493552225E-11 0.229366688E-12 0.107555639E-13 0.509888606E-15 0.245539089E-16 2 0.694598077E-09 0.150272309E-10 0.328042396E-12 0.723969955E-14 0.162302704E-15 3 0.206384042E-08 0.267044231E-09 0.348654968E-10 0.460201394E-11 0.617041535E-12 4 0.204631179E-10 0.969748715E-12 0.463716169E-13 0.224173766E-14 0.110085968E-15 5 0.210059531E-09 0.738306614E-11 0.261840461E-12 0.938806958E-14 0.341924806E-15 6 0.716127895E-01 0.728078190E-01 0.756993011E-01 0.828172043E-01 0.100465146E+00 7 0.928387208E+00 0.927192181E+00 0.924300699E+00 0.917182796E+00 0.899534854E+00 Component Mole fractions on stages: 36 to 40 1 0.121425812E-17 0.631276628E-19 0.303945222E-20 0.892262695E-19 0.357157907E-19 2 0.373837581E-17 0.905688003E-19 0.232209117E-20 0.266927452E-22 0.535093834E-19 3 0.850030946E-13 0.123194792E-13 0.190691511E-14 0.275614399E-15 0.362267994E-16 4 0.555435344E-17 0.294831147E-18 0.167146177E-19 0.884820223E-21 0.425937635E-22 5 0.127950463E-16 0.503797130E-18 0.212636970E-19 0.920433332E-21 0.119049884E-21 6 0.144362771E+00 0.253356515E+00 0.507340487E+00 0.839769408E+00 0.970280318E+00 7 0.855637229E+00 0.746643485E+00 0.492659513E+00 0.160230592E+00 0.297196820E-01 Component Mole fractions on stages: 41 to 42 1 0.254101782E-19 0.249470381E-23 2 0.528251910E-19 0.527418527E-19 3 0.467081212E-17 0.597141304E-18 4 0.201405739E-23 0.000000000E+00 5 0.899486854E-22 0.889099389E-22 6 0.995270259E+00 0.999276364E+00 7 0.472974104E-02 0.723635917E-03 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.629665091E-07 0.341545250E-07 0.341397245E-07 0.345273287E-07 0.349267364E-07 2 0.887269146E-04 0.474583512E-04 0.477353629E-04 0.482795800E-04 0.488339746E-04 3 0.117854895E-05 0.668948586E-06 0.656444674E-06 0.663395036E-06 0.671237579E-06 4 0.246101809E-06 0.133560010E-06 0.133472188E-06 0.134987093E-06 0.136549024E-06 5 0.622349549E-05 0.335436820E-05 0.336234289E-05 0.340062827E-05 0.343983544E-05 6 0.308085362E-02 0.501862265E-02 0.714707616E-02 0.948142881E-02 0.120369620E-01 7 0.996822708E+00 0.994929728E+00 0.992801002E+00 0.990466058E+00 0.987909921E+00 Component Mole fractions on stages: 6 to 10 1 0.353328717E-07 0.357462057E-07 0.361673209E-07 0.365968334E-07 0.370353905E-07 2 0.493975265E-04 0.499709872E-04 0.505551639E-04 0.511509080E-04 0.517591137E-04 3 0.679245727E-06 0.687400939E-06 0.695713682E-06 0.704196225E-06 0.712861535E-06 4 0.138137292E-06 0.139753719E-06 0.141400586E-06 0.143080301E-06 0.144795395E-06 5 0.347969591E-05 0.352026029E-05 0.356158573E-05 0.360373258E-05 0.364676426E-05 6 0.148296914E-01 0.178763508E-01 0.211943684E-01 0.248018338E-01 0.287174541E-01 7 0.985116579E+00 0.982069295E+00 0.978750642E+00 0.975142528E+00 0.971226245E+00 Component Mole fractions on stages: 11 to 15 1 0.374836701E-07 0.379423791E-07 0.384122510E-07 0.388940433E-07 0.393885331E-07 2 0.523807171E-04 0.530166940E-04 0.536680564E-04 0.543358486E-04 0.550211416E-04 3 0.721723210E-06 0.730795451E-06 0.740093026E-06 0.749631206E-06 0.759425700E-06 4 0.146548521E-06 0.148342443E-06 0.150180030E-06 0.152064246E-06 0.153998131E-06 5 0.369074713E-05 0.373575042E-05 0.378184593E-05 0.382910777E-05 0.387761199E-05 6 0.329604972E-01 0.375507227E-01 0.425082961E-01 0.478536872E-01 0.536075492E-01 7 0.966982526E+00 0.962391608E+00 0.957433325E+00 0.952087207E+00 0.946332599E+00 Component Mole fractions on stages: 16 to 20 1 0.398965123E-07 0.404187811E-07 0.409561403E-07 0.415093813E-07 0.420792745E-07 2 0.557250258E-04 0.564486022E-04 0.571929717E-04 0.579592210E-04 0.587484068E-04 3 0.769492548E-06 0.779848006E-06 0.790508390E-06 0.801489885E-06 0.812808318E-06 4 0.155984782E-06 0.158027329E-06 0.160128905E-06 0.162292607E-06 0.164521449E-06 5 0.392743603E-05 0.397865812E-05 0.403135652E-05 0.408560852E-05 0.414148934E-05 6 0.597905760E-01 0.664233364E-01 0.735260797E-01 0.811185106E-01 0.892195281E-01 7 0.940148806E+00 0.933515258E+00 0.926411704E+00 0.918818439E+00 0.910716563E+00 Component Mole fractions on stages: 21 to 25 1 0.426665554E-07 0.432719071E-07 0.438959408E-07 0.445391720E-07 0.452019929E-07 2 0.595615362E-04 0.603995428E-04 0.612632593E-04 0.621533851E-04 0.630704481E-04 3 0.824478872E-06 0.836515759E-06 0.848931812E-06 0.861738012E-06 0.874942940E-06 4 0.166818307E-06 0.169185856E-06 0.171626488E-06 0.174142219E-06 0.176734586E-06 5 0.419907071E-05 0.425841921E-05 0.431959434E-05 0.438264615E-05 0.444761262E-05 6 0.978469214E-01 0.107017017E+00 0.116744268E+00 0.127040777E+00 0.137915737E+00 7 0.902088284E+00 0.892917276E+00 0.883189084E+00 0.872891606E+00 0.862015649E+00 Component Mole fractions on stages: 26 to 30 1 0.458846412E-07 0.465871633E-07 0.211347651E-08 0.966402835E-10 0.445437557E-11 2 0.640147612E-04 0.649863731E-04 0.137246602E-05 0.292153109E-07 0.626884157E-09 3 0.888552129E-06 0.902567337E-06 0.114004150E-06 0.145141403E-07 0.186264389E-08 4 0.179404519E-06 0.182152203E-06 0.842666566E-08 0.392922329E-09 0.184682406E-10 5 0.451451651E-05 0.458336189E-05 0.157257888E-06 0.543838988E-08 0.189581567E-09 6 0.149374784E+00 0.161419248E+00 0.161489219E+00 0.161673435E+00 0.162108240E+00 7 0.850555573E+00 0.838510051E+00 0.838509127E+00 0.838326516E+00 0.837891757E+00 Component Mole fractions on stages: 31 to 35 1 0.207011336E-12 0.970720496E-14 0.460152620E-15 0.221534338E-16 0.109519753E-17 2 0.135625934E-10 0.296067654E-12 0.653351355E-14 0.146432526E-15 0.337040213E-17 3 0.241016615E-09 0.314671090E-10 0.415311715E-11 0.556706310E-12 0.766357027E-13 4 0.875231612E-12 0.418517119E-13 0.202307061E-14 0.993215999E-16 0.500760288E-17 5 0.666347145E-11 0.236318512E-12 0.847232385E-14 0.308490827E-15 0.115354795E-16 6 0.163167379E+00 0.165782410E+00 0.172272719E+00 0.188413212E+00 0.228578779E+00 7 0.836832620E+00 0.834217590E+00 0.827727281E+00 0.811586788E+00 0.771421221E+00 Component Mole fractions on stages: 36 to 40 1 0.571272860E-19 0.289995638E-20 0.163721003E-21 0.453608473E-22 0.300308914E-19 2 0.815175132E-19 0.210029719E-20 0.549144119E-22 0.768793205E-24 0.943844312E-21 3 0.110857314E-13 0.170830464E-14 0.245652028E-15 0.322702779E-16 0.416734285E-17 4 0.265304818E-18 0.149736989E-19 0.788610980E-21 0.379377441E-22 0.179393024E-23 5 0.453274022E-18 0.189765816E-19 0.744621967E-21 0.295527813E-22 0.372443084E-23 6 0.328120320E+00 0.558643709E+00 0.857181732E+00 0.973521203E+00 0.995776105E+00 7 0.671879680E+00 0.441356291E+00 0.142818268E+00 0.264787965E-01 0.422389520E-02 Component Mole fractions on stages: 41 to 42 1 0.764985020E-22 0.169760885E-23 2 0.960960171E-21 0.173384972E-22 3 0.539150583E-18 0.693183116E-19 4 0.000000000E+00 0.000000000E+00 5 0.283527910E-23 0.738858497E-20 6 0.999344463E+00 0.999900000E+00 7 0.655537360E-03 0.100000000E-03 [Reaction rates] Component reaction rates on stages: 1 to 5 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 4 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 5 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 6 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 7 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 6 to 10 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 4 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 5 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 6 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 7 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 11 to 15 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 4 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 5 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 6 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 7 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 16 to 20 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 4 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 5 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 6 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 7 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 21 to 25 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 4 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 5 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 6 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 7 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 26 to 30 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 4 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 5 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 6 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 7 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 31 to 35 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 4 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 5 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 6 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 7 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 36 to 40 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 4 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 5 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 6 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 7 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 41 to 42 1 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 4 0.000000000E+00 0.000000000E+00 5 0.000000000E+00 0.000000000E+00 6 0.000000000E+00 0.000000000E+00 7 0.000000000E+00 0.000000000E+00 [Condenser Heat Duty] -2.922124988E+07 [Reboiler Heat Duty] 6.531711727E+07 [UA Column] 0.000000000E+00 [K-values] Component K-values on stages: 1 to 5 1 0.335023186E+02 0.334653850E+02 0.330940116E+02 0.327262157E+02 0.323616454E+02 2 0.719658983E+02 0.718865618E+02 0.710888195E+02 0.702987618E+02 0.695156329E+02 3 0.120327491E+02 0.120194839E+02 0.118861009E+02 0.117540027E+02 0.116230630E+02 4 0.328537300E+02 0.328175114E+02 0.324533277E+02 0.320926521E+02 0.317351397E+02 5 0.442973506E+02 0.442485164E+02 0.437574800E+02 0.432711738E+02 0.427891325E+02 6 0.426708833E+00 0.428158273E+00 0.428586977E+00 0.428999259E+00 0.429404343E+00 7 0.995161920E+00 0.999344574E+00 0.100058623E+01 0.100193042E+01 0.100340737E+01 Component K-values on stages: 6 to 10 1 0.319999553E+02 0.316408079E+02 0.312838740E+02 0.309288347E+02 0.305753830E+02 2 0.687386912E+02 0.679672112E+02 0.672004861E+02 0.664378309E+02 0.656785859E+02 3 0.114931578E+02 0.113641658E+02 0.112359688E+02 0.111084523E+02 0.109815060E+02 4 0.313804518E+02 0.310282572E+02 0.306782334E+02 0.303300676E+02 0.299834585E+02 5 0.423108997E+02 0.418360286E+02 0.413640844E+02 0.408946453E+02 0.404273053E+02 6 0.429802042E+00 0.430192074E+00 0.430574132E+00 0.430947885E+00 0.431312983E+00 7 0.100502841E+01 0.100680553E+01 0.100875164E+01 0.101088062E+01 0.101320737E+01 Component K-values on stages: 11 to 15 1 0.302232254E+02 0.298720841E+02 0.295216998E+02 0.291718339E+02 0.288222721E+02 2 0.649221205E+02 0.641678385E+02 0.634151824E+02 0.626636401E+02 0.619127508E+02 3 0.108550244E+02 0.107289080E+02 0.106030633E+02 0.104774049E+02 0.103518557E+02 4 0.296381184E+02 0.292937751E+02 0.289501740E+02 0.286070814E+02 0.282642869E+02 5 0.399616763E+02 0.394973912E+02 0.390341069E+02 0.385715081E+02 0.381093114E+02 6 0.431669056E+00 0.432015721E+00 0.432352585E+00 0.432679256E+00 0.432995351E+00 7 0.101574794E+01 0.101851954E+01 0.102154070E+01 0.102483132E+01 0.102841279E+01 Component K-values on stages: 16 to 20 1 0.284728271E+02 0.281233425E+02 0.277736969E+02 0.274238076E+02 0.270736354E+02 2 0.611621125E+02 0.604113893E+02 0.596603200E+02 0.589087273E+02 0.581565269E+02 3 0.102263484E+02 0.101008270E+02 0.997524768E+01 0.984958085E+01 0.972381240E+01 4 0.279216070E+02 0.275788883E+02 0.272360117E+02 0.268928960E+02 0.265495030E+02 5 0.376472691E+02 0.371851745E+02 0.367228670E+02 0.362602372E+02 0.357972334E+02 6 0.433300507E+00 0.433594399E+00 0.433876757E+00 0.434147390E+00 0.434406214E+00 7 0.103230811E+01 0.103654198E+01 0.104114095E+01 0.104613351E+01 0.105155023E+01 Component K-values on stages: 21 to 25 1 0.267231891E+02 0.263725307E+02 0.260217805E+02 0.256711220E+02 0.253208078E+02 2 0.574037377E+02 0.566504930E+02 0.558970509E+02 0.551438060E+02 0.543913006E+02 3 0.959794553E+01 0.947200248E+01 0.934602643E+01 0.922008334E+01 0.909426391E+01 4 0.262058412E+02 0.258619714E+02 0.255180115E+02 0.251741416E+02 0.248306093E+02 5 0.353338672E+02 0.348702206E+02 0.344064525E+02 0.339428057E+02 0.334796142E+02 6 0.434653283E+00 0.434888831E+00 0.435113314E+00 0.435327463E+00 0.435532342E+00 7 0.105742385E+01 0.106378936E+01 0.107068409E+01 0.107814767E+01 0.108622199E+01 Component K-values on stages: 26 to 30 1 0.249711646E+02 0.246225978E+02 0.244273568E+02 0.242336258E+02 0.240399117E+02 2 0.536402365E+02 0.528914848E+02 0.524720900E+02 0.520559389E+02 0.516398243E+02 3 0.896868545E+01 0.884349364E+01 0.877337055E+01 0.870378978E+01 0.863421512E+01 4 0.244877350E+02 0.241459163E+02 0.239544551E+02 0.237644746E+02 0.235745108E+02 5 0.330173098E+02 0.325564288E+02 0.322982777E+02 0.320421231E+02 0.317859911E+02 6 0.435729411E+00 0.435920592E+00 0.437911542E+00 0.438268854E+00 0.438585487E+00 7 0.109495101E+01 0.110438039E+01 0.110816165E+01 0.110832918E+01 0.110861769E+01 Component K-values on stages: 31 to 35 1 0.238417928E+02 0.236284949E+02 0.233739016E+02 0.230160592E+02 0.224177337E+02 2 0.512142475E+02 0.507560650E+02 0.502091765E+02 0.494404997E+02 0.481552445E+02 3 0.856305839E+01 0.848644994E+01 0.839500980E+01 0.826648651E+01 0.805159092E+01 4 0.233802273E+02 0.231710587E+02 0.229213942E+02 0.225704795E+02 0.219837373E+02 5 0.315240347E+02 0.312420084E+02 0.309053808E+02 0.304322353E+02 0.296411189E+02 6 0.438891583E+00 0.439176984E+00 0.439415489E+00 0.439550939E+00 0.439520882E+00 7 0.110940609E+01 0.111145125E+01 0.111667299E+01 0.113011056E+01 0.116607481E+01 Component K-values on stages: 36 to 40 1 0.213489993E+02 0.200785822E+02 0.216132133E+02 0.237799675E+02 0.242013941E+02 2 0.458595100E+02 0.431305434E+02 0.464270646E+02 0.510814414E+02 0.519867024E+02 3 0.766774249E+01 0.721145734E+01 0.776263802E+01 0.854085311E+01 0.869221338E+01 4 0.209356931E+02 0.196898706E+02 0.211947920E+02 0.233195989E+02 0.237328669E+02 5 0.282280197E+02 0.265482520E+02 0.285773680E+02 0.314422882E+02 0.319995058E+02 6 0.439969006E+00 0.453520752E+00 0.591870391E+00 0.862610290E+00 0.974396065E+00 7 0.127349770E+01 0.169170237E+01 0.344955529E+01 0.605127925E+01 0.703608412E+01 Component K-values on stages: 41 to 42 1 0.241264165E+02 0.239695103E+02 2 0.518256440E+02 0.514885958E+02 3 0.866528431E+01 0.860892961E+01 4 0.236593408E+02 0.235054722E+02 5 0.319003691E+02 0.316929050E+02 6 0.995923124E+00 0.999376302E+00 7 0.721505947E+01 0.723635917E+01 [Molecular weights] 1 28.010 2 44.009 3 2.016 4 28.014 5 16.043 6 18.015 7 32.042 [Feed stream 1] 27 Stage Number 1.1187274035995E+00 Flow rate 3.1032988467400E+02 Temperature [K] 2.0000000000000E+05 Pressure [Pa] -3.7448752764308E+07 Enthalpy [J/kmol] -1.0777501649556E+05 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.7352118466341E-06 Mole fraction of component 1 5.2523076160595E-03 Mole fraction of component 2 1.1664886249780E-05 Mole fraction of component 3 6.6507023628463E-06 Mole fraction of component 4 2.2676715660201E-04 Mole fraction of component 5 1.7850278962729E-01 Mole fraction of component 6 8.1599808479959E-01 Mole fraction of component 7 1.1187274035995E+00 Flow rate 1.7352118466341E-06 Mole fraction of component 1 5.2523076160595E-03 Mole fraction of component 2 1.1664886249780E-05 Mole fraction of component 3 6.6507023628463E-06 Mole fraction of component 4 2.2676715660201E-04 Mole fraction of component 5 1.7850278962729E-01 Mole fraction of component 6 8.1599808479959E-01 Mole fraction of component 7 2.9596986010976E+01 Molar mass 7.9903960045382E+02 Density 4.9286185204110E-04 Viscosity 2.7436451704021E-01 Thermal conductivity 8.1895864071040E+04 Heat capacity 2.9827990325893E-02 Surface tension [Reflashed Feed stream 1] 27 Stage Number 1.1187274035995E+00 Flow rate 3.1032988467400E+02 Temperature [K] 1.2500000000000E+05 Pressure [Pa] -3.7448752764308E+07 Enthalpy [J/kmol] -1.0777501649556E+05 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.7352118466341E-06 Mole fraction of component 1 5.2523076160595E-03 Mole fraction of component 2 1.1664886249780E-05 Mole fraction of component 3 6.6507023628463E-06 Mole fraction of component 4 2.2676715660201E-04 Mole fraction of component 5 1.7850278962729E-01 Mole fraction of component 6 8.1599808479959E-01 Mole fraction of component 7 1.1187274035995E+00 Flow rate 1.7352118466341E-06 Mole fraction of component 1 5.2523076160595E-03 Mole fraction of component 2 1.1664886249780E-05 Mole fraction of component 3 6.6507023628463E-06 Mole fraction of component 4 2.2676715660201E-04 Mole fraction of component 5 1.7850278962729E-01 Mole fraction of component 6 8.1599808479959E-01 Mole fraction of component 7 2.9596986010976E+01 Molar mass 7.9900754314725E+02 Density 4.9286185204110E-04 Viscosity 2.7436451704021E-01 Thermal conductivity 8.1895864071040E+04 Heat capacity 2.9827990325893E-02 Surface tension [Top product] 1 Stage Number 9.2003550585436E-01 Flow rate 3.3729145938265E+02 Temperature [K] 1.0000000000000E+05 Pressure [Pa] 1.7800836505154E+06 Enthalpy [J/kmol] 6.1439906720330E+03 Entropy [J/kmol/K] 1.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.1095240480913E-06 Mole fraction of component 1 6.3853121136435E-03 Mole fraction of component 2 1.4181183761449E-05 Mole fraction of component 3 8.0853623713648E-06 Mole fraction of component 4 2.7568436159374E-04 Mole fraction of component 5 1.3146274545818E-03 Mole fraction of component 6 9.9200000000000E-01 Mole fraction of component 7 9.2003550585436E-01 Flow rate 2.1095240480913E-06 Mole fraction of component 1 6.3853121136435E-03 Mole fraction of component 2 1.4181183761449E-05 Mole fraction of component 3 8.0853623713648E-06 Mole fraction of component 4 2.7568436159374E-04 Mole fraction of component 5 1.3146274545818E-03 Mole fraction of component 6 9.9200000000000E-01 Mole fraction of component 7 3.2095098198340E+01 Molar mass 1.1445198891928E+00 Density 1.1038165051948E-05 Viscosity 1.9094127958074E-02 Thermal conductivity 4.6839091342633E+04 Heat capacity * Surface tension [Bottom product] 42 Stage Number 1.9850606474513E-01 Flow rate 3.8231528386155E+02 Temperature [K] 1.4000000000000E+05 Pressure [Pa] -3.7465603513782E+07 Enthalpy [J/kmol] -1.0062736974886E+05 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.6976088462550E-24 Mole fraction of component 1 1.7338497192436E-23 Mole fraction of component 2 6.9318311563803E-20 Mole fraction of component 3 0.0000000000000E+00 Mole fraction of component 4 7.3885849725737E-21 Mole fraction of component 5 9.9990000000000E-01 Mole fraction of component 6 1.0000000000000E-04 Mole fraction of component 7 1.9850606474513E-01 Flow rate 1.6976088462550E-24 Mole fraction of component 1 1.7338497192436E-23 Mole fraction of component 2 6.9318311563803E-20 Mole fraction of component 3 0.0000000000000E+00 Mole fraction of component 4 7.3885849725737E-21 Mole fraction of component 5 9.9990000000000E-01 Mole fraction of component 6 1.0000000000000E-04 Mole fraction of component 7 1.8016402089691E+01 Molar mass 9.3957338263305E+02 Density 2.5409646852935E-04 Viscosity 6.8427501875054E-01 Thermal conductivity 7.6175141559675E+04 Heat capacity 5.7285013869292E-02 Surface tension [Side stream 1 from stage 1] 1 Stage Number 1.8583300000000E-04 Flow rate 3.3729145938265E+02 Temperature [K] 1.0000000000000E+05 Pressure [Pa] 1.7800836505154E+06 Enthalpy [J/kmol] 6.1439906720330E+03 Entropy [J/kmol/K] 1.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.1095240480913E-06 Mole fraction of component 1 6.3853121136435E-03 Mole fraction of component 2 1.4181183761449E-05 Mole fraction of component 3 8.0853623713648E-06 Mole fraction of component 4 2.7568436159374E-04 Mole fraction of component 5 1.3146274545818E-03 Mole fraction of component 6 9.9200000000000E-01 Mole fraction of component 7 1.8583300000000E-04 Flow rate 2.1095240480913E-06 Mole fraction of component 1 6.3853121136435E-03 Mole fraction of component 2 1.4181183761449E-05 Mole fraction of component 3 8.0853623713648E-06 Mole fraction of component 4 2.7568436159374E-04 Mole fraction of component 5 1.3146274545818E-03 Mole fraction of component 6 9.9200000000000E-01 Mole fraction of component 7 3.2095098198340E+01 Molar mass 1.1445198891928E+00 Density 1.1038165051948E-05 Viscosity 1.9094127958074E-02 Thermal conductivity 4.6839091342633E+04 Heat capacity * Surface tension [End of Results] GUIArguments /kpldUseCOSEThermo:UseCOSEDiffusionCoefficients8UsePerturbedDerivativesOnly"UsePerturbed_ddX"SuppressWarnings@RelativePerturbationTemperatureMbP?:RelativePerturbationPressureMbP?0PerturbationCompositionMbP?InletReflash<none>OutletFlashPVFDUseOnlyKValuesAndEnthalpyFromCOSE*RestartDataAvailable,OmitStageFromPortNameWilsonEstimate"LogPropertyCallsEnergyPorts UseInitialGuess(Temperature profile4Temperature at each stage*Tѩu@b픳\u@l4u@Z\-su@Ԋ$u@V%6ĝ(u@ #=-u@1u@ 6u@*qX;u@C[$@u@Du@͌#{Iu@C4_Nu@:dSu@zYu@SU^u@Yxcu@ډ7iu@fڞnu@{*Etu@|:f zu@Dnu@,u@۱"u@oru@Gu@5K]ǝu@J:o:u@5Ku@Gu@_xm@u@L2u@7BPu@3gbu@Du@yU 0v@Sov@p!w@ hw@Yw@Iw!g w@"Pressure profile.Pressure at each stage*j@j@@@%@d@@@@^@@@@X@@@@R@@@ @L@@@@F@@@@@@~@@@A@<A[AzAA@AAAA(Vapour Flow profile4Vapour Flow at each stage*:QH@>@m6 2<@AҧU;@xZY:@I'<9@xx7@ 6u6@z5@L3@J@Le1@|?5N/@up-@6rݔ*@@'@|$@GQg!@Mc{-(@t'm@Fk@j@+ @!9 @KԢ@m@@ܝ @8ܘ@Ԗ:K@#b:@QJ@ @>#@=4@Q-@_@Xh@!ޛ@J!K\@F^"l@<8b>@6+-CI@zPPM@(Liquid Flow profile4Liquid Flow at each stage*j"@$2󞶉@m'洉@Nh@?ֲ@@ZR1@u`d@nG@4݋Ԥ@a)7@9Gל@Or,A@Y>?@''̍@5o@:INw@ z@$s@k@U {b@qKY@QF\O@VE@O)e:@R.@/!@QƟ@!$ @˟@PΟ@@PnП@eOҟ@(%;ҟ@_x%3̟@HKe@V9^@ݷZ'@cwbǝ@࠽(@ X@cIc@7g@ 1h@Duties profile*Duties at each stage*z{(G%A4Vapour Moleweight profile@Vapour Moleweight at each stage*<, @@ h@@F|'f@@@@M2r@@vöE?@zNz?@{?@J?@9b->?@ rh?@'@?@|,}?@n)?@a2U0*?@W}?@"uq?@2?@g?@^?@k{?@]om?@J$(^?@ M?@ZӼ@ʦ\>@>@`7l[>@i㈵|<@w8@z6C4@ n2@Mۿ2@~:p2@.Vapour Density profile:Vapour Density at each stage*4O?G?Cp?{ q??(,?7qrC? h"l8?R$_?tbc?8#?O!WY?~m?bۢ?.UikVapour Viscosity at each stage*Ru&>/yHP>ch#>@])>{8/>NEG5>QG؃;>|gA> rG>K#>N>7- T>\A[>R~a>Lh>&o>v>MS3b;~>f͈Ѕ>B>ޚٜ>mڝ>V>a> >v6O>h,>d3o>Ӂ~>]0`>RȖ> >N]7>9Q:>r>7 >>>"7>">N>`c9£> 4>ck$>:Vapour Heat capacity profileFVapour Heat capacity at each stage*H3MgkG@Ȱ7nG@3mJoG@@"2pG@~RpG@qG@qG@E|'rG@V-rG@ qG@_qG@rhpG@y&1pG@?nG@4OpmG@wgkG@iG@z6>WgG@7ddG@eaG@ʡE^G@n~ZG@_AhVG@=,ԚQG@Tt$LG@GG@6AG@gGG@hIG@B 3mJG@KTo LG@LG@`IG@) 0AG@6>W[)G@^)F@ PSJF@D@pUjRB@0*PA@qtA@4KA@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stage*_i?$[.?s_s䖓?E"?Wߴl?&L?^?ݏ% ?g?s?eF%?)?F.?"2T8? O?foB?I/L?֩4ZV?_'Ia?Ҟ}l?QH2w?)($?F펔?.?{:+y?2nrB?Hf?H&Δ?ܔ?mAc?v]?N=_?V?MgJ?"s ?e"v?r:?ko񮂕?Ij-4?1? ~c?]=?h"Ϣ5?#?4Liquid Moleweight profile@Liquid Moleweight at each stage*{?@ q?@6?@b?@M֨?@ʡ?@4Op?@dǾ?@R~Rӱ?@ݘģ?@~?@KTo ?@'@r?@Y_?@CfJ?@W24?@a?@4h?@V->@m~>@Ae>@v>@9⪲g>@гYB>@^>@&=@:H=@fc]=@u@J4@?W[?@ea@u@{@ed@.!@gj@&S@y&1@H}@ 0@ @4@@1*@h@ǘ@U0*@8팇@U@Liquid Viscosity at each stage*G ͽ6?iqɟ6?YK6?LIXi6?0Эw6? i6?c3ou\6?%O6?teC6?1(]66?(Ց)6?Hkt6?1-6?J6?65?"W5? 5?wK:5?)p5?3+5?GI5?/5?LIi5?ĕ5?j45?Mv5?%s0j5?d~@Y5?O#L5?69?5?Yp25?%5?k5?g+%> 5?2#n5?V4?`w4?~3?+Z1?D80? 0?[S(0?:Liquid Heat capacity profileFLiquid Heat capacity at each stage*?߾V@IV@y@eV@C9јV@8EGrV@۝V@`YiR V@\*V@S㥣V@8 V@`5!V@{,}V@6XV@k&lV@V@ÞvkV@WCKV@O#-V@V@̗`V@.9V@Y/rV@N#EV@AH0V@ V@V@VzNz}V@ϠV@sV@m4V@f6$#V@u/C6?'{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 4.6 MW\fs29 \par } @Q@;@$I$IR>@`_uC@m۶m[#@XuP(@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 98.3\super o\nosupersub C \par \b 75 bar\b0 \par } O@H@$I$IB@_OE@-@3@F{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 11450 kmol/h \par 50\super o\nosupersub C \par 51.2 bar \par 0.6746 H\sub 2\nosupersub \par 0.0030 N\sub 2\nosupersub \par 0.2297 CO \par 0.0686 CO\sub 2\nosupersub \par 0.0023 H\sub 2\nosupersub O \par } \@e@p۶m6.@m۶m:@m۶.@m۶m{@@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 38\super o\nosupersub C \par } G@;@$I$IG@J@,@,1@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 83.1\super o\nosupersub C \par \b 110 bar\b0\fs29 \par } Q@H@$I$IM@GP@-@jfffff3@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 -6.1 MW\fs29 \par } R@;@$I$9D@`_H@m۶m#@XuP(@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 4.5 MW\fs29 \par } @Q@;@$I$I@`_5N@m۶m[#@XuP(@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 2.9 kW\fs29 \par } O@;@$I$I>@`_C@ܶm۶3@:6@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 0.669 kmol/h\b0 \par 324\super o\nosupersub C \par \b 110 bar \par } ]@@Q@$I$IF@+K@8@?@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 52.9\super o\nosupersub C \par \b 110 bar\b0 \par } Q@H@$I$R@gT@8@=@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 145\super o\nosupersub C\b0 \par \b 109 bar\b0 \par } Q@H@$I$9W@X@@2@@7@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 150\super o\nosupersub C \par 75 bar\b0 \par } N@H@$I$Z@O\@2@7@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 267\super o\nosupersub C \par 107.5 bar\b0 \par } @U@H@$I$Z@\@#@-@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 173.5\super o\nosupersub C \par \b 107 bar\b0 \par } R@H@$I$U@W|WW@>@A@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 38\super o\nosupersub C \par 106.5 bar\b0 \par } @U@H@$I$I]@o_@A@@D@@R.R.uK@۶m۶ N@0 0 G@۶m۶ N@0 0 G@R.R.uK@۶m۶ N@۶m۶ N@ @ @{{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 41 \par } ;@;@H@hffffFJ@n۶mvQ@*R@{{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 27 \par } ;@;@H@hffffFJ@ܶm۶L@BA$N@z{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 2 \par } 1@;@@I@hffffJ@ܶm۶F@BATH@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 499.4\super o\nosupersub C \par \b 110 bar\b0 \par } R@H@$I$1S@W|WU@@I@K@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 41.4\super o\nosupersub C \par \b 110 bar \par \b0 37365 kmol/h \par } \@@Q@$I$AS@$I$!V@C@G@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 2.2%\b0 \par } H@;@$I$1[@$I$q\@E@hffff&G@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 218.1 kmol/h \par 37.2\super o\nosupersub C \par \b 2 bar\b0 \par } @[@@Q@$I$yV@$I$9Y@L@P@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 CO conversion 64% \par CO\sub 2\nosupersub conversion 17%\b0 \par } @g@H@$I$\@`@7@jffff;@H{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 840.5 kmol/h \par 0.535 H\sub 2\nosupersub \par 0.041 N\sub 2\nosupersub \par 0.038 CO \par 0.085 CO\sub 2\nosupersub \par 0.295 CH\sub 4\nosupersub \par 0.006 MeOH \par 339 ppm H\sub 2\nosupersub O \par } \@e@n۶m&^@꠆`@m۶mKG@ܶm۶P@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 1132 MW\fs29 \par } U@;@I$ItV@X@n۶m۶D@AAF@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 1.3 MW\fs29 \par } @Q@;@I$I|V@X@n۶m6I@AAJ@/{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 3312 kmol/h \par 0.006 CO\sub 2\nosupersub \par 0.992 MeOH \par 0.001 H\sub 2\nosupersub O \par 2 ppm CO \par 276 ppm CH\sub 4\nosupersub \par 8 ppm N\sub 2\nosupersub \par } \@ c@p۶m۶/@ <@m۶mH@PP@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 715 kmol/h \par 0.0001 MeOH \par 0.9999 H\sub 2\nosupersub O \par } ]@@Q@m۶m{0@ =@ܶm۶Q@ܶm۶MS@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 +64.8 MW\fs29 \par } V@;@$I$F@__K@m۶mS@꠆T@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 -28.9 MW\fs29 \par } @U@;@$I$@@`_5E@n۶m&C@AAD@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 1 bar\b0\fs29 \par } I@;@$I$)J@`_uN@n۶mD@AA]F@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 RR=0.88\fs29 \par } S@;@$I$C@`_H@n۶mvH@AAI@"{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 4027.4 kmol/h \par 0.005 CO\sub 2\nosupersub \par 226 ppm CH\sub 4\nosupersub \par 0.816 MeOH \par 0.179 H\sub 2\nosupersub O \par 12 ppm H\sub 2\nosupersub \par \par } ]@ c@n۶mQ@n۶mT@ܶm۶P@vPuPS@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 64.1\super o\nosupersub C \par } O@;@H$I?@C@F@hffffVH@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 109.2\super o\nosupersub C \par } R@;@$I$I@@C@R@43333S@-http://pubs.acs.org/doi/pdf/10.1021/ie100323dMethanol Reactor/Column ProcessN@*@gfffff=@@http://www.chemsep.com/Copyright (c) 2012 ChemSep.orgVUUUUN@T@<@@ׁ?ׁ?ׁ?ׁ??N