FSD100MbP?h㈵>dk 3k&dgffffr@м@0=rSaved DME3_ie101583j.fsd lx temperaturepressure compositionflowDehydraion of MethanolAUwNA\tQ1M1Dehydraion of MethanolUNIQUAQư>MbP?MbP?MbP?K'C:\Program Files\COCO\data\ChemSep1.pcdwMethanolCH3OHCH4O67-56-1COM@:^A?5?@?@ u@@ e@@ e@ {?@`@@ڤ?z?`T=@9`%;?VA3Y@H ALHA ?`•>@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 Ԫ6~@?XB?f@@yZ7@ƫ@ ݔB 8 8`f>s@|@ @*? 8 8@ e@u@ 㥛 u@ X4?#~jL|sj1@G?G?Q?@?@֤?@?ۿ`?6?`nL k??@?@ڤ?D @z@)Տ?@?֤?bWaterHOHH2O 7732-18-5OT9@ uAz?@O?`fRw@`fq@`q@@2@ ??=^@ I9@qU?AӬ`@ AVA@?{J@` 8 8 8$m@`fq@ B@@; I@ p Р@@3o@Q:@jX@Y%@ó>@`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> ? Hth@z 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|?`h@ yY.?m@؃@yf7@&@B 8 8tx@@3@ ZWt l> 8 8q@@ 9@ :#J{#Q@\yf8TBfm?w-! b=@p?`ff???`X@B?`i?8? AN?`? ?Q8*@ ?@1(@8@y ?(?B?Dimethyl etherCH3OCH3C2H6O115-10-6COCy=y@pTA`?? o@u`@t`@e@G@@? r?=@`9 ȟ?AټA@I0GAJRA?q8@ 8 8 8zTJ@t`@??y@ ? 8t`@y@i`]@`f=O.'>@t`@y@e@E^AF@+G@@t`@y@jg@e?`>4@zt`@d@v@ V ?@rzt`@@o@@@R`;'@UE;?`@b@p@?G\@F ߌ@i@p@hnR%G|@}?`Rc@t`@ o@e>J?@@ 8t`@@@fÿ'^b|΢>^@zt@ ??`fҏ@0A 8 o@p@fbG@@ c?`tt`@y@`@@Y@@@d t-@`Dl v> 8`c@@Z5@{@`f4 8 8`>n@ \[v@ j`O? 8 8t`@ o@ i^@ ? ?? @? 8 8=?+? ,? s?ۗ?`I@@?SE @{@4g"???activityactivityBactivityCoefficientactivityCoefficientBdensitydensity enthalpyenthalpy enthalpyF enthalpyFentropyentropy!entropyFentropyF excessEnthalpyexcessEnthalpyfugacityfugacityfugacityCoefficientfugacityCoefficientgibbsFreeEnergy gibbsEnergyGG heatCapacityheatCapacityCpKK heatOfVaporizationheatOfVaporizationOidealGasEnthalpyidealGasEnthalpy logFugacityCoefficientlogFugacityCoefficientmolecularWeightmolecularWeightHHHsurfaceTensionsurfaceTensionsurfaceTension (pure)surfaceTension (pure)thermalConductivitythermalConductivity04thermalConductivity (pure)thermalConductivity (pure)RS vaporPressure vaporPressureNB viscosity viscosity& viscosity (pure)viscosity (pure)" volumevolumeVapor Vapor phaseLiquid Liquid phase  oŏ1?Methanol/Water p61 1/1aimported from NRTL.IPDoŏ1?Methanol/Water p61 1/1aimported from NRTL.IPD Gz?Methanol/methanolimported from HAYDENO.IPD?Water/methanolimported from HAYDENO.IPD?Water/methanolimported from HAYDENO.IPD333333? Water/waterimported from HAYDENO.IPD g곿Methanol/Water p730imported from PR.IPD g곿Methanol/Water p730imported from PR.IPD†W2Methanol/Water p730imported from SRK.IPD†W2Methanol/Water p730imported from SRK.IPD†W2Methanol/Water p730imported from SRK.IPD†W2Methanol/Water p730imported from SRK.IPD?ܵ?Methanol/Waterimported from VANLAAR.IPDH}8?Methanol/Waterimported from VANLAAR.IPDH?Methanol/Waterimported from MARGULES.IPD:M?Methanol/Waterimported from MARGULES.IPD-QY@Methanol/Waterimported from WILSON.IPDPgkYn@Methanol/Waterimported from WILSON.IPD4ЄWMethanol/Water p61 1/1aimported from NRTL.IPD\Ux@Methanol/Water p61 1/1aimported from NRTL.IPD G} o8eMethanol/Water (Kojima+Kato)imported from UNIQUAC.IPDFitted to T=350Ku`Iq@Methanol/Water (Kojima+Kato)imported from UNIQUAC.IPDZp?XH@ Manual entry~Uf@Fitted to 350K+'ט=z@ Manual entry fffffIMethanol/Waterimported from UNIQUACP.IPDGzX@Methanol/Waterimported from UNIQUACP.IPD :CH3OHH2OCH2CH2OCH3OH?x?L7A`@@H2Oq= ףp?ffffff?kt2@CH3ͪ?A`"? rh.@CH3ORQ? rh?cX9?@f(\0@33333`r@r@@Ʌ@@po@m@33333sףp= T@4CH2OHH2OCH2OCH3ͪ?A`"? rh.@OH?333333?5^I 1@H2Oq= ףp?ffffff?kt2@CH3ORQ? rh?)\?@$@P@̰@33333t@{G<@hp@ffffffu@^{GP@@33333#a@j@CH2OHH2OOCH3?? rh.@OH??5^I 1@H2O??kt2@O??0@@ h"?#?+ DӚ?( 0gsѿ_vOV8gDi 9#a4?1%ӿ{fffff@33333q33333w@Tq@7@33333@fffff}33333w@V瞯<Dehydraion of MethanolNew Reaction PackagebKrx-ZVMeOH Dehydration'C:\Program Files\COCO\data\ChemSep1.pcdMethanol67-56-1MethanolCH4O@`@@Water 7732-18-5WaterH2O2@Dimethyl ether115-10-6Dimethyl etherC2H6OG@MeOH DehydrationVapor_1e3*exp(-8-9680/T)*P*(x(Methanol)-x("dimethyl ether")*x(water)/x(methanol)/exp(-2.8086+3061/T))160960??@@ @c]Fx@AMeOH Dehydration67-56-1Methanol@`@@@ u@CH4ODehydraion of MethanolMethanol 7732-18-5Water2@`fRw@H2ODehydraion of MethanolWater115-10-6Dimethyl etherG@ o@C2H6ODehydraion of MethanolDimethyl ether ????????????thermalConductivity.Dmoles?? / molexcessEnthalpy.Dpressure??gibbsFreeEnergy.Dpressure??enthalpyF.DmolFraction??viscosity.Dtemperature???? thermalConductivity.Dtemperature??thermalConductivity.Dpressure??enthalpyF.Dpressure??activityCoefficientheatCapacity.DmolFraction??entropyF.Dmoles??enthalpy.Dmoles??density.Dpressure?@?@heatOfVaporization??molecularWeight#logFugacityCoefficient.DmolFractionentropy.Dtemperature??viscosity.Dmoles???? / mol volume.Dmoles@@@@ enthalpyF??enthalpy??vaporPressure.Dtemperature??fugacity.Dtemperature??activity.DmolFractionvolume.Dpressure@@@@excessEnthalpy.Dtemperature??surfaceTension.DmolFraction?? activityCoefficient.DtemperaturefugacityCoefficient.Dmoles / molgibbsFreeEnergy??gibbsFreeEnergy.DmolFraction??activityCoefficient.Dmoles / molactivity.Dmoles / molenthalpy.DmolFraction??logFugacityCoefficiententhalpy.Dpressure??activitymolecularWeight.Dtemperature fugacityCoefficient.DmolFractionfugacity.Dpressurevolume.DmolFraction@@@@density?@?@activity.DtemperatureenthalpyF.Dtemperature??surfaceTension.Dtemperature??thermalConductivity??entropyF.DmolFraction??surfaceTension??density.DmolFraction?@?@heatCapacity.Dtemperature??#logFugacityCoefficient.DtemperatureexcessEnthalpy??viscosity.DmolFraction????fugacityCoefficient.DpressuresurfaceTension.Dmoles?? / molentropy.Dpressure??enthalpy.Dtemperature??gibbsFreeEnergy.Dmoles?? thermalConductivity.DmolFraction??density.Dmoles?@?@ / mollogFugacityCoefficient.Dmoles / molidealGasEnthalpy.Dtemperature??surfaceTension.Dpressure??enthalpyF.Dmoles??heatOfVaporization.Dtemperature??entropyF.Dtemperature??entropy.DmolFraction??volume@@@@entropyF??entropy??molecularWeight.DpressureheatCapacity.Dpressure??gibbsFreeEnergy.Dtemperature??fugacityCoefficientviscosity.Dpressure?? logFugacityCoefficient.DpressureidealGasEnthalpy?? heatCapacity?? fugacityCoefficient.DtemperatureentropyF.Dpressure??entropy.Dmoles??activityCoefficient.Dpressure viscosity???? activityCoefficient.DmolFractionexcessEnthalpy.Dmoles??volume.Dtemperature@@@@fugacity.Dmoles?? / moldensity.Dtemperature?@?@heatCapacity.Dmoles??molecularWeight.DmolFractionactivity.DpressuremolecularWeight.Dmoles / molexcessEnthalpy.DmolFraction??@&{E813F646-A25E-4B14-8873-4853D1AA3252}Pressure increase??Pressure?? Energy demand??Adiabatic efficiency?TotalMassBalancePropertiesFraction? TotalFlowMass??&{779B2C7A-F54B-4A1D-B345-7FA14B889642}Outlet temperature?? Heat duty?? Pressure drop??&{43312205-B251-4EEB-B585-4D82BB019C56}Length??Diameter?? Roughness?? Temperature?? Heat duty?? Tolerance?Catalyst loading@?@?Catalyst porosity?Catalyst particle diameter??Wall heat transfer coefficient??Ambient Temperature??Heating/cooling tube diameter??Tube heat transfer coefficient?? Heating/Cooling tube temperature??Position??Methanol flow profile??Water flow profile??Dimethyl ether flow profile??Pressure profile??Total flow profile??Density profile?@?@Viscosity profile????Superficial velocity profile??MeOH Dehydration rate profile??Temperature profile??EnthalpyF profile??&{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??dheatOfVaporizationheatOfVaporization.DtemperatureidealGasEnthalpyidealGasEnthalpy.Dtemperature vaporPressurevaporPressure.Dtemperatureactivityactivity.Dmolesactivity.DmolFractionactivity.Dpressureactivity.DtemperatureactivityCoefficientactivityCoefficient.Dmoles activityCoefficient.DmolFractionactivityCoefficient.Dpressure activityCoefficient.Dtemperaturedensitydensity.Dmolesdensity.DmolFractiondensity.Dpressuredensity.Dtemperatureenthalpyenthalpy.Dmolesenthalpy.DmolFractionenthalpy.Dpressureenthalpy.Dtemperature enthalpyFenthalpyF.DmolesenthalpyF.DmolFractionenthalpyF.DpressureenthalpyF.Dtemperatureentropyentropy.Dmolesentropy.DmolFractionentropy.Dpressureentropy.DtemperatureentropyFentropyF.DmolesentropyF.DmolFractionentropyF.DpressureentropyF.DtemperatureexcessEnthalpyexcessEnthalpy.DmolesexcessEnthalpy.DmolFractionexcessEnthalpy.DpressureexcessEnthalpy.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 phaseDehydraion of MethanolVaporLiquid Liquid phaseDehydraion of MethanolLiquid VaporLiquiddefaultdefault material templateDehydraion of MethanolMethanol Gat least one compound needs to be present for materials of type defaultdefaultм@t@qq\a@>"@@@@@Gz?AaR?|Gz?iV!w??Gz?AaR?|Gz?iV!w?Gz?AaR?|Gz?iV!w?t@м@qq\a@>"@3 defaultм@|c$6t@)nd@Z@ɨ{?nwy?g8%?$Υ!Zs?"f]2?tgH??ɨ{?nwy?g8%?$Υ!Zs?"f]2?tgH?25    defaultp4AJ@t@)nd@Z@ɨ{?nwy?g8%?$Υ!Zs?"f]2?tgH??ɨ{?nwy?g8%?$Υ!Zs?"f]2?tgH?267' 5!'8!788!'!' 8!  defaultdv2AÖ́@)nd@Z@t?nK?dO?>%CI?YjM?Ȱ#~??t?nK?eO?>%CI?YjM?Ȱ#~?27'+''+''+ default3A@)nd@Z@ɨ{?nwy?g8%?$Υ!Zs?"f]2?tgH??ɨ{?nwy?g8%?$Υ!Zs?"f]2?tgH?28! !!! default 3Az@)nd@Z@ɨ{?nwy?g8%?$Υ!Zs?"f]2?tgH??ɨ{?nwy?g8%?$Υ!Zs?"f]2?tgH?29!  ! !!! !!! defaultev1A5|@)nd@Z@t?nK?cO?>%CI?YjM?Ȱ#~??t?nK?cO?>%CI?YjM?Ȱ#~?210 default 3Ay@)nd@Z@ɨ{?nwy?g8%?$Υ!Zs?"f]2?tgH??ɨ{?nwy?g8%?$Υ!Zs?"f]2?tgH?211 !00 !0 0!0 defaultg~`1A^>yy@B)d@r0Z@/Ҳw?2Ёb?et?HOBI?12M?`}?z0?^?\?"T?oZ?\PC?L]?]>?CGEwi?l4xC?dHf?**2?Ͳ!@?mrOl?212%050-0%050%050 defaultg~>0Au@B)d@r0Z@/Ҳw?2Ёb?et?HOBI?12M?`}?xL-?f%w?k&T,?Z`^?,?DL?Co??y@?$(EQwY?gynb?5l׊?NTY(?k?2DMEC*a*a*C*a*C*V*a*V* n: Cdefault.AS-6Ѱs@( -Q@Y2S @UHXҧ>݈>%iܝ>C)>U?'@?cq>g>v h>~կR> ???UHXҧ>݈>%iܝ>C)>S?"@?d14C;J;F;C;J;C;J; defaultn/A7 Jz@vHX@Va@#o?d?L?oٿ[?,C6?KsRM_+? 0K ?<܅?-? 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profile along the reactor?e3Aa;3A7y3A^k23A} 3AePԗ 3A/d 3A03AXsyU3Au3AP3A`3AR^T3A/2ABFZa2AWy=\2Ao!u2A~l2Aٍ2A[2A2AVOB2Ao2A6wj2A5Ӭ2AWQ2A%:x/2A2AFTc2ACj2A!2ADQ2Abla2A_O 2A7E2A'IY2A͂Z2A7Y!x2A~Q2A2A3&2Acá=J2A{iT{2A2ALB2A =2Aov}2A;2A[g2Ak'2A]V42AXF~ܞ2A*Tm2A,2A,Ԛ2A:Z3|2A'c$2Afw3̖2At2As2A->Ē2AkKk2A5ۨ2AMH2Ab2AX 2Aɱ2A{P(Y2Adv2ATotal flow profile$Total flow profile along the reactor?e)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@)nd@Density profile!Density profile along the reactor@?eal@3h@ĭIh@UwWi@kn. ?3i@ UsQi@)a mi@x!Di@peɣi@ pDi@ i@e?4i@;'oj@IYIj@W-j@4WAj@GScTj@Dfj@,3pxj@:>^j@#Hj@Fj@J]j@Q6+j@)"j@zvj@ᔎ.j@iOj@ j@ k@_ek@%3dk@׎A"k@*k@y`2k@9k@[X@k@bFk@lLk@5URk@v;Wk@2M\k@?mmak@NBek@"2ik@rmk@Jqk@`Ztk@!w&[wk@=67#zk@q|k@vvqk@3޽1k@ *k@jk@ Vk@n~k@Tm7k@Tk@%Lk@kE^ k@1ӌk@qZ/dk@1I׍k@6 [,k@GSek@93k@ Ǘk@sk@_z}Hk@K. k@AKk@'ʩBFk@ zȌk@35,8k@ak@TQk@R6#k@!1Rk@rk@:څk@wk@oă+k@rk@<*Uk@Xr,k@Dk@] ik@1q~w~k@(}k@ k{k@-rzk@"]g yk@+Kwk@qN'vk@TNtk@LD(sk@qqk@%aHpk@F~nk@flk@Viscosity profile#Viscosity profile along the reactor?eW".>}!l)>ɛă>JX{>d $>;0>H,B>5&>r>T]X>FC?>l8('>F>be>Wy>Tڤ?{>^>&0>r֦> >d z>j>{zY\>r4N>?x9KA>aƬ4>0b(>"#>t,>O6>">d6>x">'z>o[8> X>6O>C7Э>x.ܼ>lM]>q*>Ps@>¤>}u=>^ɟS">YlE>>sIH4>yf#>>,K&>jT}|>qy>$%tٹu>jer>Ůؐo>l>Mi>G~Ucg>U̟d>֤wb>!OS`>1^>Mx)\>=:Z>_[bX>PhƐV>{o T>f_S>x.Q>" jP>Y O>'M>q|L>f1uMK>'F,J>EI>$H>zG>\VD+F>ǴIE>582rD>H1C>K'B>ۥvA>@>8̆-@>ꪔ?>0?>^[x>>}=> W4w=>K<>O<>^7Q!<>T;>{%X;> :>ၫ:>TL:>3l9>Superficial velocity profile.Superficial velocity profile along the reactor?e* ? ?# ^?/u̾?N  ?,"?t@q`?c G?mP2?cw?}?P~.^?zxs ?p~a"?V#?J97%?9'?;7ܶ(?kxxZ*?MeOH Dehydration rate profile/MeOH Dehydration rate profile along the reactor?e)X?y B&?6?HM?Cӧr?43?+?ĪG?ه?w\?S3h?6QCJ?.0?KH.?H5 ?h' ?-f?+?=?W/d?N_u! ?i ?#F?NF?m?WՍ ?rDtY?E]>#O0:>](m>Rז>g>'K>P”>-J>,{L=>dܻ<>Dˁq>ݹ>+&>U>Z*>->*X> x> ;j>T> >T>/5<>+8>D>8vy>&>|B>vv(>{`>-D>EA%T>:ta> >|Uش>"o>}κ{>0F>#-#>6K">>>J>2A>t92>G9>r>;[k>/!Z>3KO>/#L0>n4>)g>IH>C >\.N >1A>~Ea>/*>ˤ>kO>D >ZG>>n>}8>Wv3 >q>l<>D>Bͱ> ~*>yN>MJ>+rȮ>EnthalpyF profile#EnthalpyF profile along the reactor@?eyzOF8ˊ'/ۓ1w}ɿ;*EL%N`V^J" f\1nh+ M7u's{)$&m-xu5ox[opGH\{έOHnD77x`Wv2NDQZaXH&u$ʼnYEQ>9X2\o;מRfUDF;j< /gE=?nv]WI-n*_{R|Zor7 v`J@K!L3Gu6Tx^.bKP e2bv[JT[8z,h競vEB:w<R.{CʤM /s'c3Ro2ߠ8t~F0OC|FY $yMxr;k~|A7Zk Ԝ5c0paE "] YKqIBkރJ.Lkߐ5"ۭ`Pd_j$x#xLast runC+++ specifications +++ Using enthalpyF in enthalpy calculations Length: 10 m Diameter: 3 m Cross section area: 7.06858 m Total reactor volume: 70.6858 m Number of heating/cooling tubes: 300 Heating/cooling tube diameter: 0.0245 m Total tube cross section area: 0.141431 m Total tube perimeter: 23.0907 m Tube heat transfer coefficient: 280 W/m/K Heating/Cooling tube temperature: 665 K Nett cross section area: 6.92715 m Net reactor volume: 69.2715 m Hydraulic diameter: 0.852167 m Catalyst loading: 2500 kg/m Catalyst porosity: 0.4 Catalyst particle diameter: 0.001 m Heat duty: 0 W/m Wall heat transfer coefficient: 0 W/m/K Flow direction: Horizontal Reaction phase: Vapor Tolerance: 1E-05 Report Intervals: 100 kinetic reaction "MeOH Dehydration": heterogeneous Compound equations: 3 Inert compounds: 0 Number of equations: 6 +++ solution +++ Solution obtained using 360 function evaluations +++ Heat Transfer results +++ Minimum temperature: 658 K Maximum temperature: 772.128191281 K Heat duty heating/cooling tubes: -1285743.34809 W ProfilesCPosition Methanol flow Water flow Dimethyl ether flow Temperature Pressure Total flow Density Viscosity Superficial velocity r[MeOH Dehydration] EnthalpyF m mol/s mol/s mol/s K Pa mol/s mol/m Pa s m/s mol/s/kg.cat J/mol 0 165.804667916 1.40005004986 0.0098499005359 658 1250000 167.214567866 228.4806557 2.14993216777e-005 0.10565009717 0.16977108286 -180809.963613 0.1 35.4994498668 66.5526590745 65.1624589252 756.771445081 1249595.52493 167.214567866 198.595791786 2.49498426128e-005 0.121548413786 9.21228231676e-005 -181142.652478 0.2 35.1864877896 66.7091401131 65.3189399638 752.590129096 1249187.69154 167.214567866 199.633993992 2.48235267354e-005 0.120916297839 8.85563693059e-005 -181489.349569 0.3 34.8857650255 66.8595014952 65.4693013458 748.590294711 1248783.19695 167.214567866 200.635681376 2.47024942919e-005 0.120312614939 8.50820962945e-005 -181820.226356 0.4 34.5969336493 67.0039171833 65.613717034 744.764780033 1248381.88159 167.214567866 201.601446238 2.45865537716e-005 0.119736261454 8.18167845467e-005 -182135.973385 0.5 34.3196428737 67.1425625711 65.7523624217 741.106671823 1247983.59308 167.214567866 202.531915346 2.44755189498e-005 0.119186170906 7.88003134803e-005 -182437.251915 0.6 34.0535075986 67.2756302086 65.8854300593 737.609285143 1247588.18645 167.214567866 203.427750042 2.43692085276e-005 0.118661310816 7.562256955e-005 -182724.69811 0.7 33.7981637742 67.4033021208 66.0131019715 734.266140555 1247195.52417 167.214567866 204.289647363 2.42674454279e-005 0.118160679153 7.22151900841e-005 -182998.922314 0.8 33.5532930553 67.5257374803 66.135537331 731.070966165 1246805.47497 167.214567866 205.11833431 2.41700569384e-005 0.117683304896 6.90160977345e-005 -183260.508109 0.9 33.3185677876 67.6431001141 66.2528999648 728.0177033 1246417.91194 167.214567866 205.914561004 2.40768751862e-005 0.117228249225 6.62336035399e-005 -183510.015691 1 33.0936693732 67.7555493213 66.365349172 725.100517228 1246032.71363 167.214567866 206.679092846 2.39877375486e-005 0.116794607253 6.40661853339e-005 -183747.980563 1.1 32.878234332 67.8632668419 66.4730666926 722.313857432 1245649.76607 167.214567866 207.412688584 2.39024887889e-005 0.116381517645 6.21417606698e-005 -183974.912623 1.2 32.6719040806 67.9664319676 66.5762318183 719.652292471 1245268.95847 167.214567866 208.116141869 2.38209759492e-005 0.115988136526 6.0209541878e-005 -184191.306503 1.3 32.4742628421 68.0652525868 66.6750524375 717.110531726 1244890.18707 167.214567866 208.790271926 2.37430492884e-005 0.115613640681 5.75638051433e-005 -184397.643961 1.4 32.284920373 68.1599238214 66.7697236721 714.683445538 1244513.35264 167.214567866 209.435913399 2.36685627694e-005 0.115257231124 5.38027589936e-005 -184594.387924 1.5 32.1035229024 68.2506225567 66.8604224074 712.36590856 1244138.36031 167.214567866 210.053958578 2.35973692781e-005 0.114918107898 4.89365603181e-005 -184781.994189 1.6 31.9298267383 68.3374706387 66.9472704894 710.153079657 1243765.11992 167.214567866 210.645271963 2.35293291638e-005 0.114595515253 4.36782747986e-005 -184960.886051 1.7 31.7636989761 68.4205345199 67.0303343705 708.040265135 1243393.54539 167.214567866 211.210726099 2.34643061076e-005 0.114288719717 3.93737041108e-005 -185131.465074 1.8 31.6051593774 68.4998043192 67.1096041699 706.023478836 1243023.5541 167.214567866 211.751029982 2.34021844703e-005 0.113997100644 3.78560685648e-005 -185294.066386 1.9 31.4542534277 68.5752572941 67.1850571448 704.098880981 1242655.06781 167.214567866 212.266890643 2.33428523525e-005 0.1137200597 4.08034593248e-005 -185449.009286 2 31.3108160513 68.6469759823 67.2567758329 702.263451865 1242288.01043 167.214567866 212.758805787 2.32862232048e-005 0.11345712995 4.79361757894e-005 -185596.560393 2.1 31.1737460284 68.7155109937 67.3253108444 700.514172721 1241922.30992 167.214567866 213.227305844 2.32322123625e-005 0.11320784353 5.33268771398e-005 -185737.039012 2.2 31.0388333485 68.7829673336 67.3927671843 698.846949217 1241557.89624 167.214567866 213.673281512 2.31807091541e-005 0.112971557817 3.40363136657e-005 -185871.026961 2.3 30.9131053407 68.8458313376 67.4556311883 697.253022527 1241194.70495 167.214567866 214.099092107 2.31314279077e-005 0.112746874537 3.63704537835e-005 -185998.792732 2.4 30.7922780825 68.9062449666 67.5160448173 695.733312599 1240832.6751 167.214567866 214.504170286 2.30844129299e-005 0.11253395887 3.40597979521e-005 -186120.538349 2.5 30.6770206389 68.9638736885 67.5736735391 694.283867698 1240471.74733 167.214567866 214.889462824 2.30395436851e-005 0.112332187717 3.26674733055e-005 -186236.540003 2.6 30.5669296509 69.0189191825 67.6287190331 692.901582488 1240111.86512 167.214567866 215.255683223 2.29967283173e-005 0.112141073884 3.11840841542e-005 -186347.071475 2.7 30.4615650809 69.0716014674 67.6814013181 691.583529957 1239752.97463 167.214567866 215.603513577 2.29558802224e-005 0.111960158143 2.84663097988e-005 -186452.393693 2.8 30.3615345201 69.1216167478 67.7314165985 690.326392782 1239395.02473 167.214567866 215.933780195 2.29168975966e-005 0.111788917206 2.88289329723e-005 -186552.733378 2.9 30.2657778907 69.1694950625 67.7792949132 689.128149206 1239037.9665 167.214567866 216.246925261 2.28797229658e-005 0.111627036764 2.76320666192e-005 -186648.317271 3 30.1741638253 69.2153020953 67.825101946 687.985989105 1238681.75315 167.214567866 216.5436552 2.28442715984e-005 0.111474074149 2.53574590975e-005 -186739.37517 3.1 30.0868337882 69.2589671138 67.8687669645 686.89698534 1238326.34013 167.214567866 216.824731618 2.28104541355e-005 0.111329566955 2.37416609866e-005 -186826.128239 3.2 30.0033873218 69.300690347 67.9104901977 685.858855854 1237971.68513 167.214567866 217.090729503 2.27782024758e-005 0.111193156574 2.17065578323e-005 -186908.780334 3.3 29.9237793517 69.3404943321 67.9502941827 684.869167764 1237617.74786 167.214567866 217.342286 2.27474426834e-005 0.111064459294 1.9887764325e-005 -186987.524582 3.4 29.8483015918 69.378233212 67.9880330627 683.9255411 1237264.49008 167.214567866 217.580035389 2.27181014302e-005 0.11094309932 2.0306479009e-005 -187062.529235 3.5 29.7765018554 69.4141330802 68.0239329309 683.026278491 1236911.87513 167.214567866 217.804407149 2.26901284072e-005 0.110828811007 2.14585641335e-005 -187133.954893 3.6 29.7079194645 69.4484242757 68.0582241263 682.169588185 1236559.86801 167.214567866 218.015871058 2.26634702026e-005 0.110721312899 2.1956937231e-005 -187201.969084 3.7 29.6418474576 69.4814602791 68.0912601298 681.353728071 1236208.43515 167.214567866 218.214890801 2.26380754033e-005 0.110620331122 1.94978857618e-005 -187266.749675 3.8 29.5783547955 69.5132066102 68.1230064609 680.576295708 1235857.54462 167.214567866 218.402151123 2.26138698465e-005 0.110525484077 1.52547510759e-005 -187328.477057 3.9 29.5177694757 69.5434992701 68.1532991208 679.835072121 1235507.16626 167.214567866 218.578288025 2.25907843371e-005 0.110436419346 1.12834173123e-005 -187387.301871 4 29.461114944 69.5718265359 68.1816263866 679.127795238 1235157.27171 167.214567866 218.743960491 2.25687465056e-005 0.110352776927 1.22243125963e-005 -187443.335962 4.1 29.407703015 69.5985325004 68.2083323511 678.453773759 1234807.83376 167.214567866 218.899329148 2.25477373103e-005 0.110274451595 1.54183004698e-005 -187496.675571 4.2 29.3569755667 69.6238962245 68.2336960752 677.812049197 1234458.82637 167.214567866 219.044645513 2.2527728928e-005 0.110201294443 1.89419511674e-005 -187547.428832 4.3 29.3074567061 69.6486556548 68.2584555055 677.201912471 1234110.22404 167.214567866 219.180085189 2.25087035019e-005 0.110133196889 1.74945885809e-005 -187595.739736 4.4 29.2594777306 69.6726451426 68.2824449933 676.621031567 1233762.00254 167.214567866 219.306354031 2.2490587773e-005 0.110069786089 1.31650629271e-005 -187641.765015 4.5 29.2134307803 69.6956686177 68.3054684684 676.067367784 1233414.13901 167.214567866 219.424069618 2.24733174482e-005 0.110010736371 8.06416833352e-006 -187685.635515 4.6 29.1712607404 69.7167536377 68.3265534884 675.53844665 1233066.61243 167.214567866 219.533997093 2.24568107278e-005 0.109955650587 9.89162595095e-006 -187727.421468 4.7 29.1316759849 69.7365460154 68.3463458661 675.034483048 1232719.40273 167.214567866 219.636032568 2.24410780107e-005 0.109904568909 1.37599726791e-005 -187767.185995 4.8 29.091928823 69.7564195964 68.3662194471 674.556006487 1232372.49005 167.214567866 219.729971004 2.2426143037e-005 0.109857582769 9.81285272508e-006 -187805.055707 4.9 29.0538963242 69.7754358458 68.3852356965 674.099896094 1232025.85536 167.214567866 219.816798789 2.24119037006e-005 0.109814188949 5.67568391913e-006 -187841.152147 5 29.0201753751 69.7922963204 68.402096171 673.663713542 1231679.48145 167.214567866 219.897285674 2.23982775561e-005 0.109773994719 1.09464837398e-005 -187875.502808 5.1 28.9869393621 69.8089143268 68.4187141775 673.249828551 1231333.35165 167.214567866 219.970634951 2.23853486149e-005 0.109737390546 1.16703320365e-005 -187908.161745 5.2 28.9529034755 69.8259322701 68.4357321208 672.856727252 1230987.44856 167.214567866 220.037318106 2.23730727074e-005 0.109704134208 4.04548313072e-006 -187939.319342 5.3 28.9244215114 69.8401732522 68.4499731029 672.479451231 1230641.75772 167.214567866 220.098937537 2.2361279073e-005 0.109673421173 1.08826712836e-005 -187968.96498 5.4 28.8945875487 69.8550902335 68.4648900842 672.122447419 1230296.26445 167.214567866 220.154021128 2.23501242855e-005 0.109645980358 7.70476513775e-006 -187997.182538 5.5 28.8670679639 69.8688500259 68.4786498766 671.781603749 1229950.95438 167.214567866 220.203898791 2.23394705511e-005 0.109621144806 7.91628100627e-006 -188024.058755 5.6 28.8406534881 69.8820572639 68.4918571145 671.457174139 1229605.81446 167.214567866 220.248473372 2.23293289596e-005 0.109598959333 7.41595892146e-006 -188049.64793 5.7 28.815575113 69.8945964514 68.5043963021 671.148146793 1229260.832 167.214567866 220.28806373 2.23196673422e-005 0.109579262115 7.2315566123e-006 -188074.012004 5.8 28.7916110102 69.9065785028 68.5163783535 670.853907504 1228915.9949 167.214567866 220.322859803 2.23104670907e-005 0.109561956022 6.79873985315e-006 -188097.210437 5.9 28.7687697146 69.9179991506 68.5277990013 670.57370004 1228571.29168 167.214567866 220.353099416 2.23017045617e-005 0.109546920557 6.34320544916e-006 -188119.299362 6 28.7470771419 69.9288454369 68.5386452876 670.306812546 1228226.71143 167.214567866 220.379007038 2.22933574481e-005 0.109534042288 6.12889142839e-006 -188140.330509 6.1 28.7264068454 69.9391805852 68.5489804359 670.052680554 1227882.24396 167.214567866 220.400759789 2.2285408426e-005 0.109523231677 5.89381488037e-006 -188160.353742 6.2 28.7066997178 69.949034149 68.5588339997 669.810721858 1227537.87942 167.214567866 220.41854152 2.22778394384e-005 0.109514396157 5.59885958865e-006 -188179.416157 6.3 28.6879567818 69.958405617 68.5682054677 669.580374857 1227193.60943 167.214567866 220.432530333 2.22706329216e-005 0.109507446291 5.38888714897e-006 -188197.559678 6.4 28.6700875552 69.9673402303 68.577140081 669.361046898 1226849.42337 167.214567866 220.442914859 2.22637705381e-005 0.109502287664 5.12881938419e-006 -188214.833938 6.5 28.6530422404 69.9758628877 68.5856627384 669.152192605 1226505.31215 167.214567866 220.449869076 2.22572353309e-005 0.109498833352 4.80068670037e-006 -188231.282601 6.6 28.6368375168 69.9839652495 68.5937651002 668.95342611 1226161.27037 167.214567866 220.453515638 2.22510151978e-005 0.109497022111 4.55205460636e-006 -188246.933529 6.7 28.621395038 69.9916864889 68.6014863396 668.764133535 1225817.28733 167.214567866 220.454051867 2.22450910729e-005 0.109496755772 4.29295429777e-006 -188261.837071 6.8 28.6066742703 69.9990468727 68.6088467234 668.583811672 1225473.35473 167.214567866 220.451639527 2.22394472762e-005 0.109497953964 4.02332900724e-006 -188276.033101 6.9 28.5926810162 70.0060434998 68.6158433505 668.412238245 1225129.46926 167.214567866 220.446349042 2.22340768583e-005 0.109500581802 3.8148794876e-006 -188289.53795 7 28.5793611433 70.0127034363 68.6225032869 668.248827601 1224785.62115 167.214567866 220.438369837 2.22289615608e-005 0.109504545393 3.64595184464e-006 -188302.398334 7.1 28.5666804318 70.019043792 68.6288436427 668.093124894 1224441.80293 167.214567866 220.427848956 2.22240871906e-005 0.109509771976 3.52346332506e-006 -188314.650093 7.2 28.5546091922 70.0250794118 68.6348792625 667.945002427 1224098.0123 167.214567866 220.414826709 2.2219449843e-005 0.109516241882 3.38802784598e-006 -188326.304623 7.3 28.5431122897 70.030827863 68.6406277137 667.803939302 1223754.24075 167.214567866 220.399472259 2.22150332363e-005 0.109523871491 3.26062069919e-006 -188337.402651 7.4 28.5321563363 70.0363058398 68.6461056904 667.669540746 1223410.48176 167.214567866 220.381913744 2.22108250519e-005 0.109532597599 3.13660947315e-006 -188347.975467 7.5 28.5217259999 70.041521008 68.6513208586 667.541670499 1223066.73313 167.214567866 220.362194945 2.22068210686e-005 0.109542398969 3.00272247872e-006 -188358.034189 7.6 28.5117862168 70.0464908995 68.6562907502 667.419909796 1222722.98793 167.214567866 220.3404522 2.22030082082e-005 0.109553208388 2.85544812241e-006 -188367.611945 7.7 28.5023069933 70.0512305113 68.6610303619 667.303912462 1222379.24048 167.214567866 220.316798265 2.21993756634e-005 0.109564970381 2.68891729123e-006 -188376.73619 7.8 28.4932874113 70.0557403022 68.6655401529 667.19352385 1222035.48833 167.214567866 220.291283379 2.21959185903e-005 0.109577660569 2.53730634393e-006 -188385.418494 7.9 28.484700309 70.0600338534 68.6698337041 667.088420158 1221691.72617 167.214567866 220.264013216 2.21926268739e-005 0.109591227018 2.39760818308e-006 -188393.684467 8 28.4765204883 70.0641237638 68.6739236145 666.98829024 1221347.94889 167.214567866 220.235089412 2.21894907906e-005 0.109605619798 2.26964822178e-006 -188401.558655 8.1 28.4687367386 70.0680156386 68.6778154893 666.892987619 1221004.15399 167.214567866 220.204559785 2.21865057707e-005 0.109620815753 2.15507394664e-006 -188409.052611 8.2 28.4613299594 70.0717190282 68.6815188789 666.802262343 1220660.33736 167.214567866 220.172506101 2.21836640001e-005 0.109636774835 2.05707000391e-006 -188416.185986 8.3 28.4542789342 70.0752445408 68.6850443915 666.715836709 1220316.49443 167.214567866 220.139019268 2.21809567931e-005 0.109653452426 1.97923740416e-006 -188422.980593 8.4 28.4475664963 70.0786007598 68.6884006104 666.633567805 1219972.62276 167.214567866 220.104146117 2.21783797007e-005 0.109670825844 1.90505869486e-006 -188429.448058 8.5 28.4411745991 70.0817967083 68.691596559 666.555265363 1219628.71915 167.214567866 220.067949031 2.2175926782e-005 0.109688864655 1.82681528143e-006 -188435.603544 8.6 28.4350841693 70.0848419232 68.6946417739 666.480683847 1219284.77953 167.214567866 220.030508519 2.2173590355e-005 0.109707529373 1.74692986865e-006 -188441.466346 8.7 28.4292836053 70.0877422052 68.6975420559 666.409680718 1218940.80156 167.214567866 219.991871417 2.21713659651e-005 0.109726797271 1.66521384865e-006 -188447.047709 8.8 28.4237606761 70.0905036698 68.7003035205 666.34210687 1218596.78276 167.214567866 219.952086738 2.21692489514e-005 0.109746644527 1.58121779739e-006 -188452.3594 8.9 28.4184967578 70.093135629 68.7029354797 666.277746496 1218252.71954 167.214567866 219.911225328 2.21672325641e-005 0.109767036404 1.49171019967e-006 -188457.418478 9 28.4134837972 70.0956421093 68.70544196 666.216473507 1217908.60978 167.214567866 219.869328698 2.21653128556e-005 0.109787952777 1.40293527349e-006 -188462.234752 9.1 28.4087168865 70.0980255646 68.7078254153 666.158186188 1217564.45181 167.214567866 219.826430406 2.21634866388e-005 0.109809377479 1.32445439866e-006 -188466.816044 9.2 28.4041798808 70.1002940675 68.7100939182 666.102695749 1217220.24248 167.214567866 219.782592489 2.21617480069e-005 0.109831280098 1.25383982073e-006 -188471.177263 9.3 28.3998613213 70.1024533472 68.7122531979 666.049849715 1216875.97925 167.214567866 219.737865111 2.21600921864e-005 0.109853636123 1.19366615305e-006 -188475.330356 9.4 28.3957498617 70.104509077 68.7143089277 665.999496479 1216531.65961 167.214567866 219.692298148 2.21585144298e-005 0.109876421157 1.1466249132e-006 -188479.287198 9.5 28.3918373847 70.1064653155 68.7162651662 665.951576194 1216187.28243 167.214567866 219.645911459 2.21570128746e-005 0.109899625793 1.10329310024e-006 -188483.052705 9.6 28.3881141615 70.1083269272 68.7181267779 665.905979619 1215842.84587 167.214567866 219.598741064 2.21555841041e-005 0.109923232525 1.06117999405e-006 -188486.63553 9.7 28.3845692366 70.1100993896 68.7198992403 665.862559352 1215498.34746 167.214567866 219.550835455 2.21542235012e-005 0.109947217583 1.02317249732e-006 -188490.047207 9.8 28.3811929259 70.111787545 68.7215873957 665.821202647 1215153.78528 167.214567866 219.502231779 2.21529275376e-005 0.109971562843 9.87739211228e-007 -188493.296637 9.9 28.3779757774 70.1133961192 68.7231959699 665.781801141 1214809.15748 167.214567866 219.452965742 2.21516928224e-005 0.109996250881 9.530096141e-007 -188496.392386 10 28.3749122262 70.1149278948 68.7247277455 665.744292911 1214464.46303 167.214567866 219.40305788 2.21505174194e-005 0.110021271852 9.17438028562e-007 -188499.339362 +7 $not all material ports are connectedMeOH DehydrationInletOutlet  @@ @@ @@ @@ @@ ??@@@VUUUUU@message: Warning: temperature out of range for vapor pressure correlation for compound Methanol (T = 665.74 K, range = [175.47 - 512.64] K) message: Warning: temperature out of range for vapor pressure correlation for compound Water (T = 665.74 K, range = [263.15 - 647.29] K) message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 665.74 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0 !(last message repeated 2 times) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Methanol at 6.7e+002 K. Poynting factor based models should not be used at supercritical conditions message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Water at 6.7e+002 K. Poynting factor based models should not be used at supercritical conditions message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 6.7e+002 K. Poynting factor based models should not be used at supercritical conditions HeatExchanger_5;HeatExchanger - transfers heat from a hot to a cold stream.zT?H=M-~B COUSCOUS0002 Type#Type of heat transfer specification Temperature Heat transfer Heat exchange Temperature Heat transferMax. heat transfer TemperatureTemperature of outlet stream 1?@ _B Heat exchange/Heat transferred from hot stream to cold stream@?@5AA@xD Heat transfer8Heat transferred from hot stream to cold stream per area@?@)ǥA@xDModeOperation modecounter-currentcounter-current co-currentcounter-currentPressure drop stream 1Pressure drop along stream 1??j@ _BPressure drop stream 2Pressure drop along stream 2??j@ _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 runT+++ specifications +++ Pressure drop stream 1: 50000 Pa Pressure drop stream 2: 50000 Pa Temperature: 658 K Adapt outlet temperatures: true Tolerance: 0.0001 Maximum iterations: 100 +++ solution +++ +++ optional parameters +++ Heat exchange: 2344043.94487965 W Heat transfer: 152760.99880059 W/K Mode: counter-current ) $not all material ports are connectedInlet1Inlet2Outlet1Outlet2   $@@@@@@@ @@ @@ @@ @@ @@@@@@@ @@ @@ @@@ @@@ @@@ @message: Warning: temperature out of range for vapor pressure correlation for compound Methanol (T = 658.00 K, range = [175.47 - 512.64] K) message: Warning: temperature out of range for vapor pressure correlation for compound Water (T = 658.00 K, range = [263.15 - 647.29] K) message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 658.00 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0 !(last message repeated 2 times) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Methanol at 6.6e+002 K. Poynting factor based models should not be used at supercritical conditions message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Water at 6.6e+002 K. Poynting factor based models should not be used at supercritical conditions message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 6.6e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 456.79 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.6e+002 K. Poynting factor based models should not be used at supercritical conditions VaporizerMHeaterCooler - 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?z@r@ _B Heat duty Heat duty@?@LЉTA@x@xD Pressure dropPressure drop along the unit?? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++ Heat duty: 5384000.23059566 W Pressure drop: 0 Pa +++ optional parameters +++ Outlet temperature: 430 K  $not all material ports are connectedInletOutlet Vs{R{(3ƈ{(h{3Vs{R{(3ƈ{(h{3Vs{R{(3ƈ{(h{3Vs{R{(3ƈ{(h{3@@ ɿ@????@@@@@ɿ@@UUUUUUmessage: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 430.00 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0 message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.3e+002 K. Poynting factor based models should not be used at supercritical conditions Economizer;HeatExchanger - transfers heat from a hot to a cold stream.zT?H=M-~D COUSCOUS0002 Type#Type of heat transfer specification Temperature Heat transfer Heat exchange Temperature Heat transferMax. heat transfer TemperatureTemperature of outlet stream 1?y@ _B Heat exchange/Heat transferred from hot stream to cold stream@?@8A@xD Heat transfer8Heat transferred from hot stream to cold stream per area@?@$P.@@xDModeOperation modecounter-currentcounter-current co-currentcounter-currentPressure drop stream 1Pressure drop along stream 1??j@ _BPressure drop stream 2Pressure drop along stream 2??j@ _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 runU+++ specifications +++ Pressure drop stream 1: 50000 Pa Pressure drop stream 2: 50000 Pa Temperature: 400 K Adapt outlet temperatures: true Tolerance: 0.0001 Maximum iterations: 100 +++ solution +++ +++ optional parameters +++ Heat exchange: 1580542.78842143 W Heat transfer: 21689.2644740758 W/K Mode: counter-current   $not all material ports are connectedInlet1Inlet2Outlet1Outlet2   $@@@@@@@ @@ @@ @@ @@ @@@@@@@ @@ @@ @@@ @@@ @@UUUUUU@UUUUUUmessage: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 415.78 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 415.78 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0 message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions HeaterCooler_8MHeaterCooler - 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?u@r@ _B Heat duty Heat duty@?@ԺJ@x@xD Pressure dropPressure drop along the unit??j@ _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++ Heat duty: -3372578.1746908 W Pressure drop: 50000 Pa +++ optional parameters +++ Outlet temperature: 351 K !.%2 $not all material ports are connectedInlet Outlet Vs{R{(3ƈ{~*{3Vs{R{(3ƈ{~*{3Vs{R{(3ƈ{~*{3Vs{R{(3ƈ{~*{3@@ ɿ@????@@@@@ɿ@@@C1ChemSep Unit OperationqeWCXcCSUOOo[ChemSep] Version=6.93 Compiled=2012-9-11 12:48 70c8de5cb5ef Name=C:\windows\profiles\harry\Temp\CS_7~O1W.sep Title=ChemSep CO Unit Operation "C1" in COFE Flowsheet User=harry Date=2012-09-11 Time=12:55:51 [Cape-Open] unitname=C1 CO_ID=CS_7_4E_1CD900C_FE1030 3 components Methanol 67-56-1 32.0419998169 Mw Water 7732-18-5 18.0149993896 Mw Dimethyl ether 115-10-6 46.0690002441 Mw 0 thermo exe=C:\Program Files\ChemSepL6v93\bin\co-col2.exe mode=COFE NoWarnings=FALSE 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 1 use initial guess 0 inlet reflash 0 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\chemsepl6v93\bin\ Help and Info path=c:\program files\chemsepl6v93\help\ Component data path=c:\program files\chemsepl6v93\pcd\ Property data path=c:\program files\chemsepl6v93\ipd\ Section data path=c:\program files\chemsepl6v93\ild\ Executables path=C:\Program Files\ChemSepL6v93\bin\ Temporary path=C:\windows\profiles\harry\Temp\ Scripts path=c:\program files\chemsepl6v93\bin\ [Units] Temperature=C Flow=mol/s Mass flow=kg/s Pressure=bar Heat=MW Enthalpy=kJ/kmol Entropy=J/kmol/K Fraction=_ Length=m 1/Length=1/m Area=m2 Volume=m3 Mass=kg Angle=deg Velocity=m/s Surface tension=dyn/cm Density=kg/m3 Molar density=kmol/m3 Viscosity=Pa.s Molecular weight=kg/kmol Heat capacity=J/kmol/K Thermal conductivity=J/s/m/K Diffusivity=1e-8 m2/s Interaction parameter=J/mol Time=s [Components] 3 32 1101 Library Offset, Index DT=2012-07-17,01:03:18 CHK=11108 CAS=67-56-1 CID=Methanol Name=Methanol Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd 14 1921 Library Offset, Index DT=2012-07-17,01:03:18 CHK=3189 CAS=7732-18-5 CID=Water Name=Water Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd 53 1401 Library Offset, Index DT=2012-07-17,01:03:18 CHK=40248 CAS=115-10-6 CID=Dimethyl ether Name=Dimethyl ether Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd [Operation] 2 Operation Column 1 Operation kind Simple Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 22 Stages 1 Feed stages 0 Sidestream stages F=12 S= 0 Pumparound stages P= [Properties] 350 BIP estimation temperature [Thermodynamics] * K model * * * Activity coefficient * * Wilson model * * UNIQUAC model * * Equation of State * * Cubic EOS * * Virial EOS * * Vapour pressure * 0 Henry's law * Henry's default * [Enthalpy] * Enthalpy * 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 * 12 Default Liquid Diffusion Coefficients * [Reaction data] 0 Number of reactions [Specifications] Top Bottom [Heaters/Coolers] 0 Number 0 Column duty Qcolumn 2 First stage 21 Last stage 0 Qcolumn lost to surroundings [Efficiencies] 1 Default efficiency 0 Number [Pressures] 2 Column pressure Bottom & top pressures 1000000 Condenser pressure 1000000 Top pressure * Pressure Drop 1030000 Bottom pressure [Feeds] 1 Number 2 Feed state p & VF 12 Stage Feed1{split} 351 Temperature 1064464.49575 Pressure 0.32337519368 Vapour fraction 3 componentflows 0.0283749408276 Component 1 flow 0.0701148174102 Component 2 flow 0.0687246172233 Component 3 flow [Condenser] 1 Type Reflux ratio 0.4 Value Qcondenser * Type * * Initialization guess [Reboiler] 7 Type Mole fraction of a component 0.0001 Value Qreboiler 3 1st comp. * Type * * Initialization guess [Monitored Variables] * [Solve options] 3 Initialization Old Results 1 Method Newton's method 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 0 Trace treshold [Programs] Temporary file=SCRATCH.TMP User program= 1 Compiler Gfortran 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 2 ComboBox=ComboBox23 0 StringGrid=StringGrid7 16 2 Title McCabe-Thiele diagram Dimethyl ether - Dimethyl ether Xlabel X Dimethyl ether/(Dimethyl ether+Dimethyl ether) Ylabel Y Dimethyl ether/(Dimethyl ether+Dimethyl ether) 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 2 ComboBox=ComboBox76 0 ComboBox=ComboBox77 0 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 3404008 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 3404008 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 3404008 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 3404008 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=Edit5 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 3 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow Duties 1 317.2931683 1.000000000E+06 6.871484638E-02 2.748593855E-02 -1.661362357E+06 2 317.2935835 1.000000000E+06 9.620078493E-02 2.746233459E-02 0.000000000E+00 3 317.3547930 1.001500000E+06 9.617718097E-02 2.745122113E-02 0.000000000E+00 4 317.4185449 1.003000000E+06 9.616606751E-02 2.743564611E-02 0.000000000E+00 5 317.4902285 1.004500000E+06 9.615049249E-02 2.740638294E-02 0.000000000E+00 6 317.5864336 1.006000000E+06 9.612122932E-02 2.733505020E-02 0.000000000E+00 7 317.7583914 1.007500000E+06 9.604989658E-02 2.713418240E-02 0.000000000E+00 8 318.1650508 1.009000000E+06 9.584902878E-02 2.653519215E-02 0.000000000E+00 9 319.3019765 1.010500000E+06 9.525003853E-02 2.474371070E-02 0.000000000E+00 10 322.6937855 1.012000000E+06 9.345855708E-02 1.994655280E-02 0.000000000E+00 11 332.1583709 1.013500000E+06 8.866139918E-02 1.202848826E-02 0.000000000E+00 12 346.1717703 1.015000000E+06 2.548708780E-02 1.228626092E-01 0.000000000E+00 13 346.2602175 1.016500000E+06 2.436308016E-02 1.228750782E-01 0.000000000E+00 14 346.5532821 1.018000000E+06 2.437554908E-02 1.227845713E-01 0.000000000E+00 15 347.9989260 1.019500000E+06 2.428504222E-02 1.222068123E-01 0.000000000E+00 16 355.1401255 1.021000000E+06 2.370728323E-02 1.207073438E-01 0.000000000E+00 17 378.4493575 1.022500000E+06 2.220781472E-02 1.223540886E-01 0.000000000E+00 18 408.2415654 1.024000000E+06 2.385455948E-02 1.303631193E-01 0.000000000E+00 19 420.1442495 1.025500000E+06 3.186359020E-02 1.331223309E-01 0.000000000E+00 20 423.3071616 1.027000000E+06 3.462280180E-02 1.337174311E-01 0.000000000E+00 21 424.6827703 1.028500000E+06 3.521790206E-02 1.333900413E-01 0.000000000E+00 22 427.8932419 1.030000000E+06 3.489051220E-02 9.849952908E-02 1.160466333E+06 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.1598259E+08 -0.1598259E+08 -0.6928018E+05 -0.6928018E+05 2 0.1287149E+07 -0.1598274E+08 -0.1485186E+05 -0.6927928E+05 3 0.1291345E+07 -0.1597443E+08 -0.1485075E+05 -0.6925152E+05 4 0.1295712E+07 -0.1596706E+08 -0.1484844E+05 -0.6922005E+05 5 0.1300614E+07 -0.1596250E+08 -0.1484270E+05 -0.6917905E+05 6 0.1307169E+07 -0.1596658E+08 -0.1482698E+05 -0.6911482E+05 7 0.1318834E+07 -0.1599741E+08 -0.1478236E+05 -0.6899793E+05 8 0.1346331E+07 -0.1611324E+08 -0.1465411E+05 -0.6877902E+05 9 0.1423131E+07 -0.1651693E+08 -0.1428468E+05 -0.6845632E+05 10 0.1652403E+07 -0.1803681E+08 -0.1323367E+05 -0.6874078E+05 11 0.2293546E+07 -0.2391376E+08 -0.1052396E+05 -0.7495841E+05 12 0.3243891E+07 -0.3284363E+08 -0.6842997E+04 -0.8915030E+05 13 0.3249961E+07 -0.3283605E+08 -0.6833807E+04 -0.8912836E+05 14 0.3269675E+07 -0.3284361E+08 -0.6767455E+04 -0.8911560E+05 15 0.3366007E+07 -0.3292412E+08 -0.6378594E+04 -0.8913462E+05 16 0.3833468E+07 -0.3313154E+08 -0.4384303E+04 -0.8894007E+05 17 0.5187938E+07 -0.3245601E+08 0.1998211E+04 -0.8624967E+05 18 0.6007537E+07 -0.3015490E+08 0.6681365E+04 -0.8031846E+05 19 0.5754078E+07 -0.2944847E+08 0.4456891E+04 -0.7922540E+05 20 0.5608537E+07 -0.2930254E+08 0.2642759E+04 -0.7911435E+05 21 0.5570256E+07 -0.2938408E+08 0.1932915E+04 -0.7932596E+05 22 0.5585729E+07 -0.2998965E+08 0.1914571E+04 -0.8054600E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.4606900E+02 0.1746278E+02 0.9818515E-05 0.6856630E+05 0.1941335E-01 2 0.4606898E+02 0.1746275E+02 0.9818529E-05 0.6856633E+05 0.1941340E-01 3 0.4606892E+02 0.1748555E+02 0.9820491E-05 0.6857477E+05 0.1942155E-01 4 0.4606874E+02 0.1750815E+02 0.9822539E-05 0.6858340E+05 0.1942998E-01 5 0.4606820E+02 0.1753017E+02 0.9824857E-05 0.6859262E+05 0.1943928E-01 6 0.4606659E+02 0.1755042E+02 0.9828005E-05 0.6860368E+05 0.1945126E-01 7 0.4606175E+02 0.1756523E+02 0.9833716E-05 0.6862053E+05 0.1947154E-01 8 0.4604715E+02 0.1756333E+02 0.9847352E-05 0.6865555E+05 0.1951750E-01 9 0.4600298E+02 0.1750999E+02 0.9885603E-05 0.6874795E+05 0.1964340E-01 10 0.4587036E+02 0.1730164E+02 0.9999756E-05 0.6902024E+05 0.2001742E-01 11 0.4549606E+02 0.1669620E+02 0.1031883E-04 0.6976387E+05 0.2107127E-01 12 0.4487498E+02 0.1582501E+02 0.1079729E-04 0.7076582E+05 0.2267361E-01 13 0.4487221E+02 0.1584337E+02 0.1080024E-04 0.7077343E+05 0.2268520E-01 14 0.4485743E+02 0.1584811E+02 0.1081030E-04 0.7078965E+05 0.2272014E-01 15 0.4477264E+02 0.1577565E+02 0.1086053E-04 0.7084988E+05 0.2288670E-01 16 0.4427340E+02 0.1530855E+02 0.1111322E-04 0.7099918E+05 0.2370489E-01 17 0.4154018E+02 0.1349862E+02 0.1200864E-04 0.6932670E+05 0.2634170E-01 18 0.3419976E+02 0.1031742E+02 0.1342936E-04 0.5905939E+05 0.2942091E-01 19 0.2938537E+02 0.8626483E+01 0.1412334E-04 0.5072942E+05 0.3053101E-01 20 0.2789307E+02 0.8139102E+01 0.1431728E-04 0.4802135E+05 0.3083268E-01 21 0.2734070E+02 0.7963695E+01 0.1439751E-04 0.4710419E+05 0.3097867E-01 22 0.2641292E+02 0.7646868E+01 0.1456918E-04 0.4594745E+05 0.3134609E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.4606898E+02 0.5740452E+03 0.1005241E-03 0.1461100E+06 0.1339614E+00 0.8758232E-02 2 0.4606877E+02 0.5740466E+03 0.1005256E-03 0.1461097E+06 0.1339636E+00 0.8758499E-02 3 0.4606814E+02 0.5739535E+03 0.1005034E-03 0.1461500E+06 0.1339400E+00 0.8751537E-02 4 0.4606626E+02 0.5738690E+03 0.1004909E-03 0.1461888E+06 0.1339281E+00 0.8746022E-02 5 0.4606062E+02 0.5738108E+03 0.1005079E-03 0.1462231E+06 0.1339497E+00 0.8744670E-02 6 0.4604360E+02 0.5738334E+03 0.1006147E-03 0.1462439E+06 0.1340680E+00 0.8755401E-02 7 0.4599187E+02 0.5741072E+03 0.1009992E-03 0.1462243E+06 0.1344701E+00 0.8801814E-02 8 0.4583206E+02 0.5751778E+03 0.1022598E-03 0.1460797E+06 0.1357427E+00 0.8958090E-02 9 0.4531877E+02 0.5789108E+03 0.1064376E-03 0.1455151E+06 0.1400086E+00 0.9490035E-02 10 0.4352237E+02 0.5926619E+03 0.1216786E-03 0.1431657E+06 0.1573444E+00 0.1161592E-01 11 0.3706938E+02 0.6465874E+03 0.1827809E-03 0.1314432E+06 0.2424345E+00 0.2135510E-01 12 0.2658242E+02 0.7600649E+03 0.2784800E-03 0.1059413E+06 0.4499163E+00 0.4215490E-01 13 0.2658134E+02 0.7599893E+03 0.2782435E-03 0.1059682E+06 0.4499476E+00 0.4214300E-01 14 0.2655110E+02 0.7602195E+03 0.2779160E-03 0.1059617E+06 0.4504733E+00 0.4215170E-01 15 0.2636810E+02 0.7619962E+03 0.2769011E-03 0.1058040E+06 0.4535768E+00 0.4225287E-01 16 0.2564282E+02 0.7680675E+03 0.2694471E-03 0.1056078E+06 0.4656746E+00 0.4238717E-01 17 0.2442567E+02 0.7682725E+03 0.2347056E-03 0.1105231E+06 0.4840762E+00 0.4054139E-01 18 0.2384941E+02 0.7488012E+03 0.1945062E-03 0.1113413E+06 0.4853214E+00 0.3612234E-01 19 0.2357603E+02 0.7417287E+03 0.1823837E-03 0.1184044E+06 0.4852660E+00 0.3433232E-01 20 0.2344976E+02 0.7409889E+03 0.1795528E-03 0.1203204E+06 0.4867899E+00 0.3396800E-01 21 0.2319754E+02 0.7446810E+03 0.1783487E-03 0.1199175E+06 0.4951264E+00 0.3437049E-01 22 0.2205858E+02 0.7667271E+03 0.1754980E-03 0.1150885E+06 0.5363130E+00 0.3686585E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.635721098E-07 0.709940779E-06 0.277108312E-05 0.933117391E-05 0.301768855E-04 2 0.449411894E-07 0.441322502E-06 0.155282962E-05 0.466307807E-05 0.133538800E-04 3 0.999999891E+00 0.999998849E+00 0.999995676E+00 0.999986006E+00 0.999956469E+00 Component Mole fractions on stages: 6 to 10 1 0.963018932E-04 0.305534738E-03 0.964170763E-03 0.300750926E-02 0.904500630E-02 2 0.376229748E-04 0.105496063E-03 0.296784697E-03 0.849682245E-03 0.255826598E-02 3 0.999866075E+00 0.999588969E+00 0.998739045E+00 0.996142808E+00 0.988396728E+00 Component Mole fractions on stages: 11 to 15 1 0.238930797E-01 0.360206529E-01 0.361029618E-01 0.366070652E-01 0.395748222E-01 2 0.847638500E-02 0.245513198E-01 0.246089271E-01 0.248834183E-01 0.264219243E-01 3 0.967630535E+00 0.939428027E+00 0.939288111E+00 0.938509516E+00 0.934003254E+00 Component Mole fractions on stages: 16 to 20 1 0.571624169E-01 0.153975473E+00 0.416559319E+00 0.592064417E+00 0.644863836E+00 2 0.354239558E-01 0.844443620E-01 0.214805902E+00 0.298664628E+00 0.325458890E+00 3 0.907413627E+00 0.761580165E+00 0.368634778E+00 0.109270955E+00 0.296772745E-01 Component Mole fractions on stages: 21 to 22 1 0.649502045E+00 0.595250897E+00 2 0.342829286E+00 0.403026009E+00 3 0.766866816E-02 0.172309364E-02 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.709940779E-06 0.792836788E-05 0.309115148E-04 0.103979287E-03 0.335975488E-03 2 0.441322502E-06 0.433398576E-05 0.152308151E-04 0.456944489E-04 0.130846934E-03 3 0.999998849E+00 0.999987738E+00 0.999953858E+00 0.999850326E+00 0.999533178E+00 Component Mole fractions on stages: 6 to 10 1 0.107180328E-02 0.340404754E-02 0.107938386E-01 0.341615866E-01 0.106201061E+00 2 0.369582660E-03 0.104724731E-02 0.304885454E-02 0.966150642E-02 0.376755739E-01 3 0.998558614E+00 0.995548705E+00 0.986157307E+00 0.956176907E+00 0.856123365E+00 Component Mole fractions on stages: 11 to 15 1 0.268737711E+00 0.238107196E+00 0.238186700E+00 0.238922268E+00 0.243276599E+00 2 0.186427449E+00 0.575556199E+00 0.575554743E+00 0.576264948E+00 0.580610782E+00 3 0.544834840E+00 0.186336605E+00 0.186258557E+00 0.184812784E+00 0.176112619E+00 Component Mole fractions on stages: 16 to 20 1 0.263400302E+00 0.313121789E+00 0.362373885E+00 0.380866865E+00 0.383263356E+00 2 0.596402088E+00 0.614927447E+00 0.610842352E+00 0.611340601E+00 0.614643241E+00 3 0.140197610E+00 0.719507643E-01 0.267837628E-01 0.779253441E-02 0.209340215E-02 Component Mole fractions on stages: 21 to 22 1 0.368419563E+00 0.288071347E+00 2 0.631055888E+00 0.711828653E+00 3 0.524548698E-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 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 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 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 Component reaction rates on stages: 21 to 22 1 -0.000000000E+00 -0.000000000E+00 2 -0.000000000E+00 -0.000000000E+00 3 -0.000000000E+00 -0.000000000E+00 [Condenser Heat Duty] -1.661362357E+06 [Reboiler Heat Duty] 1.160466333E+06 [UA Column] 0.000000000E+00 [K-values] Component K-values on stages: 1 to 5 1 0.895456518E-01 0.895443791E-01 0.896456592E-01 0.897406990E-01 0.898187117E-01 2 0.101832989E+00 0.101828323E+00 0.101953153E+00 0.102049115E+00 0.102057263E+00 3 0.100000104E+01 0.100001111E+01 0.100004182E+01 0.100013570E+01 0.100042349E+01 Component K-values on stages: 6 to 10 1 0.898503440E-01 0.897563076E-01 0.893260314E-01 0.880377515E-01 0.851687009E-01 2 0.101798539E+00 0.100736533E+00 0.973430165E-01 0.879451097E-01 0.679025072E-01 3 0.100130935E+01 0.100405833E+01 0.101275835E+01 0.104179760E+01 0.115450269E+01 Component K-values on stages: 11 to 15 1 0.889085480E-01 0.151279144E+00 0.151574214E+00 0.153217469E+00 0.162674184E+00 2 0.454674731E-01 0.426566855E-01 0.427568835E-01 0.431805168E-01 0.455071196E-01 3 0.177600708E+01 0.504156458E+01 0.504292596E+01 0.507816342E+01 0.530344309E+01 Component K-values on stages: 16 to 20 1 0.217017279E+00 0.491743081E+00 0.114952908E+01 0.155451805E+01 0.168256063E+01 2 0.593960963E-01 0.137324106E+00 0.351655221E+00 0.488540476E+00 0.529508612E+00 3 0.647239012E+01 0.105847404E+02 0.137633678E+02 0.140225181E+02 0.141765759E+02 Component K-values on stages: 21 to 22 1 0.176294125E+01 0.206633149E+01 2 0.543262955E+00 0.566184021E+00 3 0.146195543E+02 0.172309364E+02 [Molecular weights] 1 32.042 2 18.015 3 46.069 [Feed stream 1] 12 Stage Number 1.6721437546110E-01 Flow rate 3.5099999644174E+02 Temperature [K] 1.0644644957500E+06 Pressure [Pa] -2.1238074932704E+07 Enthalpy [J/kmol] -9.5306657188939E+04 Entropy [J/kmol/K] 3.2337519368000E-01 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.6969199418026E-01 Mole fraction of component 1 4.1931094271564E-01 Mole fraction of component 2 4.1099706310411E-01 Mole fraction of component 3 5.4072981050813E-02 Flow rate 4.1080212827943E-02 Mole fraction of component 1 2.9271587913797E-02 Mole fraction of component 2 9.2964819925826E-01 Mole fraction of component 3 1.1314139441029E-01 Flow rate 2.3115864352005E-01 Mole fraction of component 1 6.0572008811617E-01 Mole fraction of component 2 1.6312126836378E-01 Mole fraction of component 3 4.4671582928906E+01 Molar mass 1.6293737952324E+01 Density 1.0961380660706E-05 Viscosity 2.3277689687496E-02 Thermal conductivity 7.1101583925603E+04 Heat capacity 2.5833665983129E+01 Molar mass 7.6750619315868E+02 Density 2.7384608532677E-04 Viscosity 4.6739828097259E-01 Thermal conductivity 1.0510267154476E+05 Heat capacity 4.3125647946247E-02 Surface tension [Reflashed Feed stream 1] 12 Stage Number 1.6721437546110E-01 Flow rate 3.4984673647119E+02 Temperature [K] 1.0150000000000E+06 Pressure [Pa] -2.1238074932704E+07 Enthalpy [J/kmol] -9.5874231802610E+04 Entropy [J/kmol/K] 3.3045153375668E-01 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.6969199418026E-01 Mole fraction of component 1 4.1931094271564E-01 Mole fraction of component 2 4.1099706310411E-01 Mole fraction of component 3 5.5256246837286E-02 Flow rate 4.1886587991651E-02 Mole fraction of component 1 2.9258756258964E-02 Mole fraction of component 2 9.2885465574938E-01 Mole fraction of component 3 1.1195812862381E-01 Flow rate 2.3276956754008E-01 Mole fraction of component 1 6.1181880399556E-01 Mole fraction of component 2 1.5541162846437E-01 Mole fraction of component 3 4.4660631883395E+01 Molar mass 1.5583980487128E+01 Density 1.0925327021459E-05 Viscosity 2.3095944986469E-02 Thermal conductivity 7.0928206056269E+04 Heat capacity 2.5639976170720E+01 Molar mass 7.7236285951897E+02 Density 2.8016470489529E-04 Viscosity 4.7051147317014E-01 Thermal conductivity 1.0397707204783E+05 Heat capacity 4.3674928631519E-02 Surface tension [Top product] 1 Stage Number 6.8714846379271E-02 Flow rate 3.1729316826572E+02 Temperature [K] 1.0000000000000E+06 Pressure [Pa] -1.5982589099544E+07 Enthalpy [J/kmol] -6.9280181707164E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 7.0994077915285E-07 Mole fraction of component 1 4.4132250246308E-07 Mole fraction of component 2 9.9999884873672E-01 Mole fraction of component 3 6.8714846379271E-02 Flow rate 7.0994077915285E-07 Mole fraction of component 1 4.4132250246308E-07 Mole fraction of component 2 9.9999884873672E-01 Mole fraction of component 3 4.6068977904939E+01 Molar mass 5.7404523764457E+02 Density 1.0052405118712E-04 Viscosity 1.3396142684207E-01 Thermal conductivity 1.4610997942577E+05 Heat capacity 8.7582320896278E-03 Surface tension [Bottom product] 22 Stage Number 9.8499529081829E-02 Flow rate 4.2789324191874E+02 Temperature [K] 1.0300000000000E+06 Pressure [Pa] -2.9989648983502E+07 Enthalpy [J/kmol] -8.0545998351605E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.8807134723006E-01 Mole fraction of component 1 7.1182865276994E-01 Mole fraction of component 2 1.0000000000000E-04 Mole fraction of component 3 9.8499529081829E-02 Flow rate 2.8807134723006E-01 Mole fraction of component 1 7.1182865276994E-01 Mole fraction of component 2 1.0000000000000E-04 Mole fraction of component 3 2.2058581700407E+01 Molar mass 7.6672714894548E+02 Density 1.7549797037905E-04 Viscosity 5.3631302310594E-01 Thermal conductivity 1.1508853521754E+05 Heat capacity 3.6865854537554E-02 Surface tension [End of Results] GUIArguments /kpldUseCOSEThermo:UseCOSEDiffusionCoefficients8UsePerturbedDerivativesOnly"UsePerturbed_ddX"SuppressWarnings@RelativePerturbationTemperatureMbP?:RelativePerturbationPressureMbP?0PerturbationCompositionMbP?InletReflash<none>OutletFlash AutoDUseOnlyKValuesAndEnthalpyFromCOSE*RestartDataAvailable,OmitStageFromPortNameWilsonEstimate"LogPropertyCallsEnergyPorts UseInitialGuess(Temperature profile4Temperature at each stageK>Ѱs@Ss@l;s@#\s@s@i2bs@I_"s@N s@zOs@Ӿ+t@6쯈t@6u@E)u@eT>ڨu@Qԙu@_}<=2v@fk}0w@Ms݃y@nONBz@d)H"tz@Ҍz@Jz@"Pressure profile.Pressure at each stage.A.A8.A.A.A`.A.A.A.A@.A.A.Ah/A /A/A(/AH4/A@/AK/ApW/A(c/An/A(Vapour Flow profile4Vapour Flow at each stage -Q@M X@V X@3٠ X@@ X@-8X@l1X@|VW@EW@|X]W@9]T*V@G;ɱ|9@E\8@#`8@H8@ۅ7@rX356@6h7@g%R??@q)OA@,6A@2MqA@(Liquid Flow profile4Liquid Flow at each stagexf|;@ G[v;@:\:s;@b〆o;@\h;@U;@Y";@pSMZ:@n/c8@HQ3@6 b(@74^@SG^@Vj6^@F:i<^@E-^@8;c^@|]K`@J}"`@D2`@r7{`@HX@Duties profile*Duties at each stageZd[Y9|?U1A4Vapour Moleweight profile@Vapour Moleweight at each stageFG@ .VG@)^G@xG@)ǺG@hG@ClG@ G@cE aG@gF@Hm~F@S:XoF@AȓoF@M(DmF@mbF@\m"F@D$D@DUA@ ܺb=@ K<;@H}8W;@D i:@.Vapour Density profile:Vapour Density at each stage->xv1@X9vv1@:M|1@`vO1@R81@w;S1@Է鲐1@e61@{Ic1@Z*oG8M1@y):0@g/@P1ί/@5Ry;/@H.!/@\C.@WCK*@Q1߄$@8a@!@˝`8G @_F@Pd@2Vapour Viscosity profile>Vapour Viscosity at each stage˩mF>sYH>dpV>v{o>:Vh>;ϸ^>ڈ¢o>}>CFJ>>=2>8<>ϮU>̆Q>>ŕS]N>s />'/)>"ti> >@ 1>/&č>:Vapour Heat capacity profileFVapour Heat capacity at each stagecZB>$Q@//>$Q@4.$Q@!lV%Q@'o|%Q@Op&Q@ vö'Q@$)Q@Bi/Q@KAQ@P>pQ@ۧ1Q@Q@TR'Q@aodQ@NQ@TQ@mM@/r]]I@ǘH@HVG@/L FF@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stageAWl?j8?]Y(>? ҥs?_n?C?mX?x@e?f8TBf?MQr?$?57?Ki:?` C? po?8=F?YQ?:ك ?9eC?p ?d$Z߸?A> ?4Liquid Moleweight profile@Liquid Moleweight at each stage .VG@ytG@TƿϸG@8*5{G@jeG@ OG@F@',F@ytͨF@4)E@qB@L$z:@MۿҔ:@[Ӽ:@X5;^:@6ُ9@i㈵l8@6 r7@σv7@ x#s7@ߦ?27@3P6@.Liquid Density profile:Liquid Density at each stageLiquid Viscosity at each stageIpIZ?L[(Z?]CX? $W?X?Lb#`?-/ y?о?oT ?4n?4N'?,b~@2?4d&<2?Ȅ!62?1+%2?@{1?i.? (&~)?yλ '?ʈ'?ec`'?MW'?:Liquid Heat capacity profileFLiquid Heat capacity at each stageQCb@ Cb@Db@/L Fb@w#Gb@o_Gb@ŏ1w-Gb@Bb@n{0b@PjMa@2ı.n`@cZB>|Z@.!}Z@ $(~}Z@~jtsZ@1fZ@i"lxz[@[@']@ho^@Q]@l\@:Liquid Thermal cond. profileFLiquid Thermal cond. at each stagep%?]m %?('$?4T$?gC%?V#)?P6?ڕL`?QC?~#?v?!m?y?(?x[f?d֜?g?!C}?L?z!Ӑ'?أ&?mmy)?0Surface tension profile<Surface tension at each stage-?n"?KiS?G3o?P?Z?5,4z?O|X?|o?dʇ?Fiޕ?xS?Zmē? Y蔥?П +?< ių?>g^P?虠~? 1? 8@d?D?-? 1 Converged 3 Iterations ~ ChemSep (TM) - COL2 6.93 Copyright (c) 1988-2012 Harry Kooijman and Ross Taylor License: 2100- 6 LITE free license Build: 5ec8146f100c Checking data file C:\windows\profiles\harry\Temp\CS_7~O1W.SEP Cape Open unit name: C1 Cape-Open unit id: CS_7_4E_1CD900C_FE1030 Cape-Open run level: normal Cape open Initialized Cape Open Thermodynamic-properties enabled Reading configuration Reading component property libraries Reading thermodynamic property options Reading specifications Reading reaction data Checking Component Data 67-56-1 Methanol 7732-18-5 Water 115-10-6 Dimethyl ether Determining feed conditions Run level: Initialization Reading initial temperature profiles Reading initial composition profiles Init 150 milliseconds Run level: Complete model Iteration log(Err/Tol) 0 3.3689 1 3.9251 2 1.0583 3 -3.5960 Run level: Report Convergence obtained in 3 iterations Time 20 milliseconds FixMem driver done run time: 1.2 seconds Using: C:\Program Files\ChemSepL6v93\bin\co-col2.exe Using CAPE-OPEN version 1.1 thermodynamics CAPE-OPEN thermo-properties were enabled CAPE-OPEN diffusion coefficients were disabled CAPE-OPEN supplied derivatives were enabled CAPE-OPEN supplied molar derivatives were enabled Inlet re-flash: <none> Outlet flash: Auto Flash used for TopProduct: PVF Flash used for BottomProduct: PVF CAPE-OPEN supplied d H / d T have been used CAPE-OPEN supplied d H / d x have been used CAPE-OPEN supplied d K / d T have been used CAPE-OPEN supplied d K / d x and d K / d y have been used Relative perturbation of pressure: 0.001 Relative perturbation of temperature: 0.001 Perturbation of composition: 0.001 5"C= not all ports are connected Feed1{split}_stage12 TopProduct BottomProduct @ @0@@ @ @ @(@ @(@$@,@@@@@@@@$@@(@@(@ @(@ @ @ @,@$@@@$@@(@ @,@ @ @,@ @$@0@,@4@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@$@4@,@0@@ 4@,@0@ 4@,@0@4@,@0@ 4@,@0@ 4@,@0@ ,@0@  ,@0@@=@message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 409.74 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.1e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 420.49 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 423.45 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 424.76 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.3e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 408.28 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.1e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 420.15 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 423.31 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 424.68 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.3e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 408.24 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.1e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 420.14 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 423.31 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 424.68 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.3e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 408.24 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.1e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 420.14 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 423.31 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 424.68 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.3e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 408.24 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.1e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 420.14 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 423.31 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 424.68 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.2e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.3e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 408.24 K, range = [131.65 - 400.10] K) message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 420.14 K, range = [131.65 - 400.10] K) message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 423.31 K, range = [131.65 - 400.10] K) message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 424.68 K, range = [131.65 - 400.10] K) message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 400.10] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 317.29 K, range = [131.65 - 248.31] K)  (last message repeated 1 time) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 317.35 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 317.42 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 317.49 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 317.59 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 317.76 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 318.17 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 319.30 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 322.69 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 322.69 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 332.16 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 332.16 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 346.17 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 346.17 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 346.17 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 346.26 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 346.26 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 346.26 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 346.55 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 346.55 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 346.55 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 348.00 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 348.00 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 348.00 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 355.14 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 355.14 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 355.14 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 378.45 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 378.45 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 378.45 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 408.24 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 408.24 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 408.24 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 420.14 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 420.14 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 420.14 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 423.31 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 423.31 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 423.31 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 424.68 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 424.68 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 424.68 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 427.89 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 427.89 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 351.00 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 351.00 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 351.00 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 349.85 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 349.85 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 349.85 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 317.29 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 400.10] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 427.89 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 427.89 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0  (last message repeated 1 time) message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.3e+002 K. Poynting factor based models should not be used at supercritical conditions message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0 message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.3e+002 K. Poynting factor based models should not be used at supercritical conditions C2ChemSep Unit OperationqeWCXcCSUOO{[ChemSep] Version=6.93 Compiled=2012-9-11 12:48 70c8de5cb5ef Name=C:\windows\profiles\harry\Temp\CS_8~JOV.sep Title=ChemSep CO Unit Operation "C2" in COFE Flowsheet User=harry Date=2012-09-11 Time=12:55:58 [Cape-Open] unitname=C2 CO_ID=CS_8_4E_1CD900C_FFBDE0 3 components Methanol 67-56-1 32.0419998169 Mw Water 7732-18-5 18.0149993896 Mw Dimethyl ether 115-10-6 46.0690002441 Mw 0 thermo exe=C:\Program Files\ChemSepL6v93\bin\co-col2.exe mode=COFE NoWarnings=FALSE 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 1 use initial guess 0 inlet reflash 0 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\chemsepl6v93\bin\ Help and Info path=c:\program files\chemsepl6v93\help\ Component data path=c:\program files\chemsepl6v93\pcd\ Property data path=c:\program files\chemsepl6v93\ipd\ Section data path=c:\program files\chemsepl6v93\ild\ Executables path=C:\Program Files\ChemSepL6v93\bin\ Temporary path=C:\windows\profiles\harry\Temp\ Scripts path=c:\program files\chemsepl6v93\bin\ [Units] Temperature=C Flow=mol/s Mass flow=kg/s Pressure=bar Heat=MW Enthalpy=kJ/kmol Entropy=J/kmol/K Fraction=_ Length=m 1/Length=1/m Area=m2 Volume=m3 Mass=kg Angle=deg Velocity=m/s Surface tension=dyn/cm Density=kg/m3 Molar density=kmol/m3 Viscosity=Pa.s Molecular weight=kg/kmol Heat capacity=J/kmol/K Thermal conductivity=J/s/m/K Diffusivity=1e-8 m2/s Interaction parameter=J/mol Time=s [Components] 3 32 1101 Library Offset, Index DT=2012-07-17,01:03:18 CHK=11108 CAS=67-56-1 CID=Methanol Name=Methanol Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd 14 1921 Library Offset, Index DT=2012-07-17,01:03:18 CHK=3189 CAS=7732-18-5 CID=Water Name=Water Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd 53 1401 Library Offset, Index DT=2012-07-17,01:03:18 CHK=40248 CAS=115-10-6 CID=Dimethyl ether Name=Dimethyl ether Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd [Operation] 2 Operation Column 1 Operation kind Simple Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 27 Stages 1 Feed stages 0 Sidestream stages F=16 S= 0 Pumparound stages P= [Properties] 350 BIP estimation temperature [Thermodynamics] * K model * * * Activity coefficient * * Wilson model * * UNIQUAC model * * Equation of State * * Cubic EOS * * Virial EOS * * Vapour pressure * 0 Henry's law * Henry's default * [Enthalpy] * Enthalpy * 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 * 12 Default Liquid Diffusion Coefficients * [Reaction data] 0 Number of reactions [Specifications] Top Bottom [Heaters/Coolers] 0 Number 0 Column duty Qcolumn 2 First stage 26 Last stage 0 Qcolumn lost to surroundings [Efficiencies] 1 Default efficiency 0 Number [Pressures] 2 Column pressure Bottom & top pressures 110000 Condenser pressure 110000 Top pressure * Pressure Drop 140000 Bottom pressure [Feeds] 1 Number 1 Feed state T & p 16 Stage Feed1{split} 427.893241919 Temperature 1030000 Pressure 0 Vapour fraction 3 componentflows 0.0283748920441 Component 1 flow 0.0701147870848 Component 2 flow 9.84995290818e-006 Component 3 flow [Condenser] 1 Type Reflux ratio 1.7 Value Qcondenser * Type * * Initialization guess [Reboiler] 7 Type Mole fraction of a component 0.001 Value Qreboiler 1 1st comp. * Type * * Initialization guess [Monitored Variables] * [Solve options] 3 Initialization Old Results 1 Method Newton's method 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 0 Trace treshold [Programs] Temporary file=SCRATCH.TMP User program= 1 Compiler Gfortran 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 0 ComboBox=ComboBox23 1 StringGrid=StringGrid7 16 2 Title McCabe-Thiele diagram Methanol - Methanol Xlabel X Methanol/(Methanol+Methanol) Ylabel Y Methanol/(Methanol+Methanol) 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 0 ComboBox=ComboBox76 1 ComboBox=ComboBox77 0 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 3404008 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 3404008 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 3404008 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 3404008 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=Edit5 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 0 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow Duties 1 339.6206950 1.100000000E+05 2.832567897E-02 4.815365425E-02 -2.700492109E+06 2 339.8802425 1.100000000E+05 7.647933322E-02 4.814745977E-02 0.000000000E+00 3 340.1765969 1.112000000E+05 7.647313875E-02 4.815266476E-02 0.000000000E+00 4 340.4748670 1.124000000E+05 7.647834373E-02 4.815090863E-02 0.000000000E+00 5 340.7857522 1.136000000E+05 7.647658760E-02 4.813901466E-02 0.000000000E+00 6 341.1184191 1.148000000E+05 7.646469363E-02 4.811106807E-02 0.000000000E+00 7 341.4872525 1.160000000E+05 7.643674704E-02 4.805775137E-02 0.000000000E+00 8 341.9150570 1.172000000E+05 7.638343034E-02 4.796454591E-02 0.000000000E+00 9 342.4379446 1.184000000E+05 7.629022488E-02 4.780913506E-02 0.000000000E+00 10 343.1129938 1.196000000E+05 7.613481403E-02 4.755796187E-02 0.000000000E+00 11 344.0301111 1.208000000E+05 7.588364084E-02 4.716246761E-02 0.000000000E+00 12 345.3296834 1.220000000E+05 7.548814658E-02 4.655754012E-02 0.000000000E+00 13 347.2250652 1.232000000E+05 7.488321909E-02 4.567129334E-02 0.000000000E+00 14 350.0101861 1.244000000E+05 7.399697231E-02 4.447586362E-02 0.000000000E+00 15 353.9385096 1.256000000E+05 7.280154259E-02 4.313949886E-02 0.000000000E+00 16 357.9600989 1.268000000E+05 5.311995258E-02 1.231997470E-01 0.000000000E+00 17 358.2294850 1.280000000E+05 5.302642069E-02 1.232513111E-01 0.000000000E+00 18 358.5256161 1.292000000E+05 5.307798480E-02 1.232864502E-01 0.000000000E+00 19 358.9030931 1.304000000E+05 5.311312391E-02 1.232759950E-01 0.000000000E+00 20 359.5150836 1.316000000E+05 5.310266875E-02 1.231435699E-01 0.000000000E+00 21 360.7697615 1.328000000E+05 5.297024360E-02 1.227294418E-01 0.000000000E+00 22 363.5778561 1.340000000E+05 5.255611552E-02 1.219133985E-01 0.000000000E+00 23 368.9731898 1.352000000E+05 5.174007220E-02 1.211801045E-01 0.000000000E+00 24 375.6129759 1.364000000E+05 5.100677824E-02 1.212223332E-01 0.000000000E+00 25 380.1383147 1.376000000E+05 5.104900691E-02 1.215836576E-01 0.000000000E+00 26 382.1670124 1.388000000E+05 5.141033130E-02 1.218126028E-01 0.000000000E+00 27 383.0037849 1.400000000E+05 5.163927650E-02 7.017332626E-02 2.084998653E+06 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.3339091E+08 -0.3339091E+08 -0.9850090E+05 -0.9850090E+05 2 0.1919175E+07 -0.3337379E+08 0.5392443E+04 -0.9842906E+05 3 0.1932819E+07 -0.3334803E+08 0.5351691E+04 -0.9829873E+05 4 0.1946630E+07 -0.3332674E+08 0.5338228E+04 -0.9815209E+05 5 0.1960848E+07 -0.3331174E+08 0.5344058E+04 -0.9798150E+05 6 0.1975778E+07 -0.3330662E+08 0.5377424E+04 -0.9777828E+05 7 0.1991905E+07 -0.3331704E+08 0.5450423E+04 -0.9753237E+05 8 0.2009989E+07 -0.3335191E+08 0.5579845E+04 -0.9723369E+05 9 0.2031226E+07 -0.3342511E+08 0.5788375E+04 -0.9687541E+05 10 0.2057483E+07 -0.3355799E+08 0.6105487E+04 -0.9646095E+05 11 0.2091649E+07 -0.3378257E+08 0.6567118E+04 -0.9601730E+05 12 0.2138115E+07 -0.3414454E+08 0.7212163E+04 -0.9561792E+05 13 0.2203246E+07 -0.3470125E+08 0.8071475E+04 -0.9541515E+05 14 0.2294968E+07 -0.3549536E+08 0.9140122E+04 -0.9565542E+05 15 0.2417325E+07 -0.3644830E+08 0.1031511E+05 -0.9653168E+05 16 0.2533460E+07 -0.3712411E+08 0.1116487E+05 -0.9750973E+05 17 0.2544777E+07 -0.3710235E+08 0.1112063E+05 -0.9745110E+05 18 0.2556776E+07 -0.3708498E+08 0.1108345E+05 -0.9740040E+05 19 0.2570866E+07 -0.3707968E+08 0.1106300E+05 -0.9737136E+05 20 0.2590960E+07 -0.3710685E+08 0.1108737E+05 -0.9740170E+05 21 0.2626988E+07 -0.3721069E+08 0.1122050E+05 -0.9758229E+05 22 0.2697577E+07 -0.3743210E+08 0.1153152E+05 -0.9804815E+05 23 0.2805309E+07 -0.3764372E+08 0.1172962E+05 -0.9869488E+05 24 0.2881013E+07 -0.3762521E+08 0.1073922E+05 -0.9906716E+05 25 0.2891453E+07 -0.3750591E+08 0.8670766E+04 -0.9917905E+05 26 0.2888844E+07 -0.3742864E+08 0.7054338E+04 -0.9921867E+05 27 0.2892012E+07 -0.3738775E+08 0.6229768E+04 -0.9921970E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.3218673E+02 0.1253836E+01 0.1107342E-04 0.4761657E+05 0.1961695E-01 2 0.3204135E+02 0.1247220E+01 0.1108758E-04 0.4738469E+05 0.1962916E-01 3 0.3203292E+02 0.1259396E+01 0.1109839E-04 0.4739438E+05 0.1966164E-01 4 0.3202407E+02 0.1271520E+01 0.1110939E-04 0.4740604E+05 0.1969510E-01 5 0.3200994E+02 0.1283356E+01 0.1112116E-04 0.4741351E+05 0.1973064E-01 6 0.3198729E+02 0.1294731E+01 0.1113423E-04 0.4741424E+05 0.1976962E-01 7 0.3195109E+02 0.1305372E+01 0.1114942E-04 0.4740428E+05 0.1981422E-01 8 0.3189336E+02 0.1314846E+01 0.1116803E-04 0.4737741E+05 0.1986786E-01 9 0.3180162E+02 0.1322466E+01 0.1119209E-04 0.4732381E+05 0.1993594E-01 10 0.3165648E+02 0.1327156E+01 0.1122480E-04 0.4722809E+05 0.2002693E-01 11 0.3142819E+02 0.1327257E+01 0.1127107E-04 0.4706643E+05 0.2015396E-01 12 0.3107229E+02 0.1320275E+01 0.1133832E-04 0.4680255E+05 0.2033706E-01 13 0.3052546E+02 0.1302648E+01 0.1143727E-04 0.4638320E+05 0.2060566E-01 14 0.2970762E+02 0.1269910E+01 0.1158141E-04 0.4573662E+05 0.2099824E-01 15 0.2855380E+02 0.1218684E+01 0.1177979E-04 0.4479120E+05 0.2154482E-01 16 0.2736633E+02 0.1165914E+01 0.1197598E-04 0.4377505E+05 0.2209707E-01 17 0.2735769E+02 0.1175691E+01 0.1198614E-04 0.4377897E+05 0.2212713E-01 18 0.2734002E+02 0.1184968E+01 0.1199763E-04 0.4377490E+05 0.2216100E-01 19 0.2729584E+02 0.1192785E+01 0.1201310E-04 0.4374714E+05 0.2220623E-01 20 0.2717599E+02 0.1196436E+01 0.1203995E-04 0.4365160E+05 0.2228401E-01 21 0.2684720E+02 0.1188590E+01 0.1209767E-04 0.4336674E+05 0.2245081E-01 22 0.2599204E+02 0.1152161E+01 0.1222761E-04 0.4258986E+05 0.2283296E-01 23 0.2412923E+02 0.1063385E+01 0.1246300E-04 0.4080061E+05 0.2357788E-01 24 0.2145009E+02 0.9368458E+00 0.1269326E-04 0.3804804E+05 0.2450728E-01 25 0.1937944E+02 0.8436907E+00 0.1277598E-04 0.3580552E+05 0.2514274E-01 26 0.1844468E+02 0.8056987E+00 0.1278670E-04 0.3476602E+05 0.2542198E-01 27 0.1812651E+02 0.7969013E+00 0.1279183E-04 0.3440958E+05 0.2553065E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.3204135E+02 0.7522985E+03 0.3371736E-03 0.1142361E+06 0.1910421E+00 0.1872110E-01 2 0.3202796E+02 0.7520798E+03 0.3364981E-03 0.1142888E+06 0.1912850E+00 0.1873099E-01 3 0.3201390E+02 0.7517535E+03 0.3355854E-03 0.1143592E+06 0.1916730E+00 0.1875090E-01 4 0.3199146E+02 0.7514535E+03 0.3347095E-03 0.1144103E+06 0.1923442E+00 0.1879852E-01 5 0.3195549E+02 0.7511870E+03 0.3338624E-03 0.1144331E+06 0.1934664E+00 0.1888969E-01 6 0.3189794E+02 0.7509739E+03 0.3330522E-03 0.1144110E+06 0.1953074E+00 0.1905002E-01 7 0.3180613E+02 0.7508490E+03 0.3322916E-03 0.1143175E+06 0.1982916E+00 0.1932003E-01 8 0.3166005E+02 0.7508740E+03 0.3315982E-03 0.1141107E+06 0.2030886E+00 0.1976331E-01 9 0.3142845E+02 0.7511642E+03 0.3309943E-03 0.1137239E+06 0.2107483E+00 0.2047896E-01 10 0.3106299E+02 0.7519436E+03 0.3305022E-03 0.1130522E+06 0.2229028E+00 0.2161948E-01 11 0.3049028E+02 0.7536697E+03 0.3301243E-03 0.1119312E+06 0.2420474E+00 0.2341445E-01 12 0.2960319E+02 0.7573090E+03 0.3297879E-03 0.1101073E+06 0.2718680E+00 0.2619423E-01 13 0.2826022E+02 0.7649202E+03 0.3291966E-03 0.1072113E+06 0.3173377E+00 0.3038277E-01 14 0.2633265E+02 0.7805486E+03 0.3274919E-03 0.1028140E+06 0.3832423E+00 0.3632894E-01 15 0.2392849E+02 0.8092081E+03 0.3228120E-03 0.9693546E+05 0.4665800E+00 0.4358147E-01 16 0.2204418E+02 0.8405165E+03 0.3152079E-03 0.9204159E+05 0.5330642E+00 0.4902907E-01 17 0.2203879E+02 0.8403733E+03 0.3142910E-03 0.9207890E+05 0.5333502E+00 0.4900376E-01 18 0.2202127E+02 0.8404661E+03 0.3133261E-03 0.9208317E+05 0.5340675E+00 0.4901299E-01 19 0.2196920E+02 0.8412311E+03 0.3121983E-03 0.9199376E+05 0.5360156E+00 0.4911957E-01 20 0.2182217E+02 0.8438781E+03 0.3105790E-03 0.9164624E+05 0.5413563E+00 0.4949141E-01 21 0.2143901E+02 0.8514605E+03 0.3075329E-03 0.9065269E+05 0.5551807E+00 0.5050961E-01 22 0.2061795E+02 0.8694798E+03 0.3006851E-03 0.8845163E+05 0.5849953E+00 0.5264766E-01 23 0.1946901E+02 0.8983781E+03 0.2868780E-03 0.8539150E+05 0.6276276E+00 0.5531911E-01 24 0.1859771E+02 0.9228256E+03 0.2699877E-03 0.8325596E+05 0.6611564E+00 0.5679959E-01 25 0.1820478E+02 0.9341587E+03 0.2590703E-03 0.8244430E+05 0.6768051E+00 0.5713715E-01 26 0.1807035E+02 0.9378872E+03 0.2543666E-03 0.8222424E+05 0.6822870E+00 0.5715026E-01 27 0.1802903E+02 0.9388794E+03 0.2524504E-03 0.8218722E+05 0.6840310E+00 0.5711110E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.989378902E+00 0.999258233E+00 0.999080708E+00 0.998458297E+00 0.997451212E+00 2 0.151631480E-03 0.394029777E-03 0.783259649E-03 0.141006714E-02 0.241722915E-02 3 0.104694663E-01 0.347737491E-03 0.136032725E-03 0.131635600E-03 0.131558717E-03 Component Mole fractions on stages: 6 to 10 1 0.995836754E+00 0.993255383E+00 0.989139638E+00 0.982599519E+00 0.972251602E+00 2 0.403165940E-02 0.661297682E-02 0.107286306E-01 0.172685993E-01 0.276162749E-01 3 0.131586815E-03 0.131640440E-03 0.131731488E-03 0.131881356E-03 0.132123066E-03 Component Mole fractions on stages: 11 to 15 1 0.955975801E+00 0.930602208E+00 0.891616418E+00 0.833308646E+00 0.751047816E+00 2 0.438916920E-01 0.692646874E-01 0.108249568E+00 0.166556005E+00 0.248815027E+00 3 0.132506469E-03 0.133104180E-03 0.134014680E-03 0.135349174E-03 0.137156921E-03 Component Mole fractions on stages: 16 to 20 1 0.666648215E+00 0.666049815E+00 0.664791045E+00 0.661640858E+00 0.653097041E+00 2 0.333342585E+00 0.333949932E+00 0.335208948E+00 0.338359142E+00 0.346902959E+00 3 0.919980626E-05 0.252913527E-06 0.697798441E-08 0.192764365E-09 0.529602878E-11 Component Mole fractions on stages: 21 to 25 1 0.629656961E+00 0.568692039E+00 0.435890162E+00 0.244890985E+00 0.972722925E-01 2 0.370343039E+00 0.431307961E+00 0.564109838E+00 0.755109015E+00 0.902727708E+00 3 0.142014579E-12 0.353557024E-14 0.731526108E-16 0.109662231E-17 0.120175512E-19 Component Mole fractions on stages: 26 to 27 1 0.306322072E-01 0.794981324E-02 2 0.969367793E+00 0.992050187E+00 3 0.111272759E-21 0.128770326E-23 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.999258233E+00 0.998976268E+00 0.997987737E+00 0.996388198E+00 0.993823507E+00 2 0.394029777E-03 0.101224785E-02 0.200774846E-02 0.360741428E-02 0.617209225E-02 3 0.347737491E-03 0.114844887E-04 0.451422838E-05 0.438748233E-05 0.440069126E-05 Component Mole fractions on stages: 6 to 10 1 0.989721169E+00 0.983175645E+00 0.972761641E+00 0.956250870E+00 0.930196643E+00 2 0.102744191E-01 0.168199390E-01 0.272339525E-01 0.437447527E-01 0.697990432E-01 3 0.441201014E-05 0.441557109E-05 0.440654204E-05 0.437708335E-05 0.431416245E-05 Component Mole fractions on stages: 11 to 15 1 0.889367545E+00 0.826126972E+00 0.730385467E+00 0.592968174E+00 0.421574858E+00 2 0.110628260E+00 0.173869043E+00 0.269610909E+00 0.407028783E+00 0.578422883E+00 3 0.419586394E-05 0.398539361E-05 0.362434606E-05 0.304288430E-05 0.225860256E-05 Component Mole fractions on stages: 16 to 20 1 0.287244186E+00 0.286860578E+00 0.285611161E+00 0.281898915E+00 0.271416981E+00 2 0.712755705E+00 0.713139419E+00 0.714388839E+00 0.718101085E+00 0.728583019E+00 3 0.108856547E-06 0.300505810E-08 0.830449540E-10 0.228133029E-11 0.610876137E-13 Component Mole fractions on stages: 21 to 25 1 0.244101313E+00 0.185567477E+00 0.103657886E+00 0.415420750E-01 0.135296575E-01 2 0.755898687E+00 0.814432523E+00 0.896342114E+00 0.958457925E+00 0.986470342E+00 3 0.151402822E-14 0.310459844E-16 0.461587069E-18 0.506298648E-20 0.471398212E-22 Component Mole fractions on stages: 26 to 27 1 0.394619210E-02 0.100000000E-02 2 0.996053808E+00 0.999000000E+00 3 0.451387157E-24 0.414937700E-24 [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 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 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 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 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 Component reaction rates on stages: 26 to 27 1 -0.000000000E+00 -0.000000000E+00 2 -0.000000000E+00 -0.000000000E+00 3 -0.000000000E+00 -0.000000000E+00 [Condenser Heat Duty] -2.700492109E+06 [Reboiler Heat Duty] 2.084998653E+06 [UA Column] 0.000000000E+00 [K-values] Component K-values on stages: 1 to 5 1 0.990113335E+00 0.100028225E+01 0.100109517E+01 0.100207760E+01 0.100365025E+01 2 0.384822389E+00 0.389262151E+00 0.390118416E+00 0.390880289E+00 0.391638531E+00 3 0.301073843E+02 0.302788831E+02 0.301342143E+02 0.300025367E+02 0.298950119E+02 Component K-values on stages: 6 to 10 1 0.100617910E+01 0.101025222E+01 0.101683660E+01 0.102755412E+01 0.104521083E+01 2 0.392397795E+00 0.393162949E+00 0.393943208E+00 0.394758188E+00 0.395654061E+00 3 0.298246854E+02 0.298127780E+02 0.298945266E+02 0.301299622E+02 0.306254268E+02 Component K-values on stages: 11 to 15 1 0.107489396E+01 0.112646390E+01 0.122074775E+01 0.140531766E+01 0.178152895E+01 2 0.396749368E+00 0.398372742E+00 0.401502921E+00 0.409199575E+00 0.430161105E+00 3 0.315802587E+02 0.333980009E+02 0.369762372E+02 0.444805524E+02 0.607264524E+02 Component K-values on stages: 16 to 20 1 0.232084145E+01 0.232185900E+01 0.232760878E+01 0.234708551E+01 0.240624974E+01 2 0.467681397E+00 0.468281410E+00 0.469224784E+00 0.471185949E+00 0.476133741E+00 3 0.845131183E+02 0.841626081E+02 0.840265914E+02 0.844964734E+02 0.866956230E+02 Component K-values on stages: 21 to 25 1 0.257949027E+01 0.306461050E+01 0.420508443E+01 0.589501090E+01 0.718956059E+01 2 0.489937402E+00 0.529580964E+00 0.629346574E+00 0.787837417E+00 0.915108817E+00 3 0.937991390E+02 0.113886027E+03 0.158482696E+03 0.216645998E+03 0.255195449E+03 Component K-values on stages: 26 to 27 1 0.776247239E+01 0.794981323E+01 2 0.973208259E+00 0.993043228E+00 3 0.270173200E+03 0.274042703E+03 [Molecular weights] 1 32.042 2 18.015 3 46.069 [Feed stream 1] 16 Stage Number 9.8499529081808E-02 Flow rate 4.2789324191900E+02 Temperature [K] 1.0300000000000E+06 Pressure [Pa] -2.9989648982953E+07 Enthalpy [J/kmol] -7.8631427014148E+04 Entropy [J/kmol/K] 1.6409973020491E-11 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.8807134722983E-01 Mole fraction of component 1 7.1182865277017E-01 Mole fraction of component 2 9.9999999999992E-05 Mole fraction of component 3 1.6163746147635E-12 Flow rate 5.9525089745511E-01 Mole fraction of component 1 4.0302600890927E-01 Mole fraction of component 2 1.7230936356134E-03 Mole fraction of component 3 9.8499529080192E-02 Flow rate 2.8807134722479E-01 Mole fraction of component 1 7.1182865277524E-01 Mole fraction of component 2 9.9999999973357E-05 Mole fraction of component 3 2.6412923652896E+01 Molar mass 7.6468679463926E+00 Density 1.4569177586008E-05 Viscosity 3.1346091299732E-02 Thermal conductivity 4.5947448864479E+04 Heat capacity 2.2058581700333E+01 Molar mass 7.6672714894700E+02 Density 1.7549797037882E-04 Viscosity 5.3631302310863E-01 Thermal conductivity 1.1508853521723E+05 Heat capacity 3.6865854537706E-02 Surface tension [Reflashed Feed stream 1] 16 Stage Number 9.8499529081808E-02 Flow rate 3.6063968662507E+02 Temperature [K] 1.2680000000000E+05 Pressure [Pa] -2.9989648982953E+07 Enthalpy [J/kmol] -8.6468578413113E+04 Entropy [J/kmol/K] 1.8624771092092E-01 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.8807134722983E-01 Mole fraction of component 1 7.1182865277017E-01 Mole fraction of component 2 9.9999999999992E-05 Mole fraction of component 3 1.8345311818275E-02 Flow rate 6.0390952559912E-01 Mole fraction of component 1 3.9557488253793E-01 Mole fraction of component 2 5.1559186295369E-04 Mole fraction of component 3 8.0154217263533E-02 Flow rate 2.1578382370189E-01 Mole fraction of component 1 7.8421129496529E-01 Mole fraction of component 2 4.8813328192430E-06 Mole fraction of component 3 2.6500502977809E+01 Molar mass 1.1206375497844E+00 Density 1.2104356965513E-05 Viscosity 2.2470328492085E-02 Thermal conductivity 4.3003584911542E+04 Heat capacity 2.1041936117823E+01 Molar mass 8.6122627785083E+02 Density 3.0917648379839E-04 Viscosity 5.6898608573026E-01 Thermal conductivity 8.9326676240279E+04 Heat capacity 5.1794781291900E-02 Surface tension [Top product] 1 Stage Number 2.8325678970000E-02 Flow rate 3.3962069500000E+02 Temperature [K] 1.1000000000000E+05 Pressure [Pa] -3.3390914426456E+07 Enthalpy [J/kmol] -9.8500901977803E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9925823300000E-01 Mole fraction of component 1 3.9402977700000E-04 Mole fraction of component 2 3.4773749100000E-04 Mole fraction of component 3 2.8325678970000E-02 Flow rate 9.9925823300000E-01 Mole fraction of component 1 3.9402977700000E-04 Mole fraction of component 2 3.4773749100000E-04 Mole fraction of component 3 3.2041350483566E+01 Molar mass 7.5229846789584E+02 Density 3.3717356845364E-04 Viscosity 1.9104210836045E-01 Thermal conductivity 1.1423609831175E+05 Heat capacity 1.8721096193558E-02 Surface tension [Bottom product] 27 Stage Number 7.0173326260000E-02 Flow rate 3.8300378490000E+02 Temperature [K] 1.4000000000000E+05 Pressure [Pa] -3.7387752885108E+07 Enthalpy [J/kmol] -9.9219704456767E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.0000000000000E-03 Mole fraction of component 1 9.9900000000000E-01 Mole fraction of component 2 4.1493770000000E-25 Mole fraction of component 3 7.0173326260000E-02 Flow rate 1.0000000000000E-03 Mole fraction of component 1 9.9900000000000E-01 Mole fraction of component 2 4.1493770000000E-25 Mole fraction of component 3 1.8029026390076E+01 Molar mass 9.3887943487719E+02 Density 2.5245040824169E-04 Viscosity 6.8403097865108E-01 Thermal conductivity 8.2187218623274E+04 Heat capacity 5.7111099233074E-02 Surface tension [End of Results] GUIArguments /kpldUseCOSEThermo:UseCOSEDiffusionCoefficients8UsePerturbedDerivativesOnly"UsePerturbed_ddX"SuppressWarnings@RelativePerturbationTemperatureMbP?:RelativePerturbationPressureMbP?0PerturbationCompositionMbP?InletReflash<none>OutletFlash AutoDUseOnlyKValuesAndEnthalpyFromCOSE*RestartDataAvailable,OmitStageFromPortNameWilsonEstimate"LogPropertyCallsEnergyPorts UseInitialGuess(Temperature profile4Temperature at each stage\]9u@(y>u@3aEWBu@2#Gu@)pLu@m Qu@OGWu@^u@[g2gu@j:qu@U{u@bFu@|ݙu@e)u@o"v@\_v@Þvcv@|mhhv@snv@L M=xv@CoPv@ >v@мw/w@;ѿyw@y6w@l1w@[w@"Pressure profile.Pressure at each stage@@&@q@@@R@@@3@~@@@_@@@@@@@A6A[AAAAAA(Vapour Flow profile4Vapour Flow at each stage%m_S<@T=eS@nGS@/&/S@wFiS@YS@0[۩S@hS@y` S@yˠS@pMOR@E0'=R@/\R@dR@JyL3R@,ZJ@oaJ@gJ@>"zJ@?$J@90|J@Y.GJ@֓I@ހI@0EI@9mI@LI@(Liquid Flow profile4Liquid Flow at each stageREH@4H@ѹӄH@`DWPH@.};H@#z7H@edH@ex=vG@_ּG@RhKkG@˔G@͂y]GG@LF@ʠ^@&=@Y8ō<@/];@3d[;@e W;@@ٔ+K;@Ll> -;@+e:@R\U9@~7!8@A&9s5@S"a3@o/iq2@b 2@.Vapour Density profile:Vapour Density at each stageahV?n?Uik|&?[[%X?M?a7?g?3l ?&(? Vapour Viscosity at each stageoA8>Hd@>+XgF>pNL>R>c>Y>Xڝa>[k>~#x>ߝD>1">6>E\kV>޸I>a}:>r(>8#>~-)>!W{1>j ?>;^>uC륤>EW#>;^>R >>j>:Vapour Heat capacity profileFVapour Heat capacity at each stageG@=G@&9 {G@odG@HKG@XG@6qrG@yNG@(rG@E 2G@:ǀG@ѳYfG@镲 1G@.lIF@/L FeF@a4E@VHIE@V/E@HĔHE@l gE@IVE@PKE@lsczfD@.s,&C@#GA@| bA@@m4A@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stagej:w??6$S."?*ؐ*?ZD4?j|>?B?-J?Lă=X?$BIj??V\=?c<Ӕ??o?SK?]1e?C?>ю~?d_?Ex:?豘і?tZX?\-a?: $?to?Q ? [28?.$?4Liquid Moleweight profile@Liquid Moleweight at each stageEJ@@Oz1@@ y@@JR?@?@.Ue?@S"^?@k ?@1m?@ ?@u}>@5Fj=@%ǝB<@(U:@H7@%#gaO 6@ni5$ 6@bbq6@H}5@y5@bp5@.14@9 x3@}ƅ2@Jvl42@ F%u2@Vn2@.Liquid Density profile:Liquid Density at each stageSc@ı.n@J +~@㥛Ġ{@"~y@Lw@ov@Ev@HPy@ $(~@ q[@x@Liquid Viscosity at each stagerǕ6?U 6?oiQ05?U-[~5?PH5?nN5?%5?KlK5?!ܓ)5?#5?"v5?>5?&:5?m gv5?'5?Ƀ7O4?i^4?6WWC\@Aǘ[@ކ[@EioZ@ktY@֭;X@uiW@镲 W@CRW@ÙV@~W[V@HGũV@V@VYU@cE aT@8gDioT@ YT@JiT@:Liquid Thermal cond. profileFLiquid Thermal cond. at each stageh_It?됛|?ZC?I?;oʁ?cY7?\'a?_?,?6?kyh?( 5 If?IlBO?g< ?x=\r?c5?Jp4?Ih˹?0 '?]yrR?6ڻP ? :H?$z?Pqw1(?'H+c?K?g?0Surface tension profile<Surface tension at each stages+?u7.?\o3?4sR?? V W? v3ف?Dȓ?]qH Outlet flash: Auto Flash used for TopProduct: PVF Flash used for BottomProduct: PVF CAPE-OPEN supplied d H / d T have been used CAPE-OPEN supplied d H / d x have been used CAPE-OPEN supplied d K / d T have been used CAPE-OPEN supplied d K / d x and d K / d y have been used Relative perturbation of pressure: 0.001 Relative perturbation of temperature: 0.001 Perturbation of composition: 0.001 J-XH not all ports are connected Feed1{split}_stage16 TopProduct BottomProduct @ @0@@ @ @ @(@ @(@$@,@@@@@@@@$@@(@@(@ @(@ @ @ @,@$@@@$@@(@ @,@ @ @,@ @$@0@,@4@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@$@4@,@0@@ 4@,@0@ 4@,@0@4@,@0@ 4@,@0@ 4@,@0@ ,@0@  ,@0@@&@message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 400.10] K) amessage: TEA warning: temperature above TC for determining COSTALD liquid density; using TR=1.0 message: TEA warning: Using Pcrit rather than Psat for Poynting factor of supercritical compound Dimethyl ether at 4.3e+002 K. Poynting factor based models should not be used at supercritical conditions #(last 3 messages repeated 1 time) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 339.62 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 339.62 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 339.62 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 339.88 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 339.88 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 339.88 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 340.18 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 340.18 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 340.18 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 340.47 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 340.47 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 340.47 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 340.79 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 340.79 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 340.79 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 341.12 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 341.12 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 341.12 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 341.49 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 341.49 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 341.49 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 341.92 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 341.92 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 341.92 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 342.44 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 342.44 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 342.44 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 343.11 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 343.11 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 343.11 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 344.03 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 344.03 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 344.03 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 345.33 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 345.33 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 345.33 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 347.23 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 347.23 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 347.23 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 350.01 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 350.01 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 350.01 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 353.94 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 353.94 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 353.94 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 357.96 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 357.96 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 357.96 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 358.23 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 358.23 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 358.23 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 358.53 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 358.53 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 358.53 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 358.90 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 358.90 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 358.90 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 359.52 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 359.52 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 359.52 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 360.77 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 360.77 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 360.77 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 363.58 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 363.58 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 363.58 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 368.97 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 368.97 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 368.97 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 375.61 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 375.61 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 375.61 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 380.14 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 380.14 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 380.14 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 382.17 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 382.17 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 382.17 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 383.00 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 383.00 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 383.00 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for vapor pressure correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 400.10] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 427.89 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 427.89 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 427.89 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 360.64 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 360.64 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 360.64 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 339.62 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 339.62 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 339.62 K, range = [120.03 - 320.03] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 383.00 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Dimethyl ether (T = 383.00 K, range = [131.65 - 248.31] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Dimethyl ether (T = 383.00 K, range = [120.03 - 320.03] K) MS Sans/C6?/C6?h㈵>/C6?*http://www.chemsep.com/Copyright (c) 2012 ChemSep.org4@S@<@@-http://pubs.acs.org/doi/abs/10.1021/ie101583j(Dehydration of Methanol to DiMethylEther3@&@YA@@ VLE Validation@W@(@@-http://pubs.acs.org/doi/pdf/10.1021/je000296o/DME-Methanol = J.Chem.Eng.Data 46 p. 640 (2001)@X@ F@@BM֋68$x-ԲL g-]xhH"Fj;F-Fj$D"3/s_0{{>D?AAE}=Oޜ'=] R{/]>)zno{_hKKkng i˳K6IGǢ~r{IKsAc{{ڪ]]S2m 9=ٵ1ݦő(([ntF>C)y4-EFz}swA/|Efw!Y U^cgay߽;<-g3-6܍sQ|{z~zX?fc'kNh_¿  )ɰޕݸ4M3܏,˳ɥ~uQY, n{ Em[mΕooZn4I[֦LP㳲Kp/! <+d# 5j6fQ9]uk>޷mvU.&sw)qr^Ve$=fsq;]?%Mϲ7|p RK`ͱo}4o4I!nӲ67U3]<㏻Jݫ骏r]}c|,cmK=A!6iVMJY 35 2l}S7~K$!ٱ66Sl[_nm#)yX(WΉnޱ|etǷֿy߻|p=ܱ2EDS߿j{[uӾ]#܍bŸ5n빒./׍}&ءa~}lǟ/|oXoNIz|/1gagkA.鵙hEZʴiz!ۊ<4Ico V?Ӭ!E&>tMc-uwѵmI`emƾ]m.ټ=3s&%S<_W7I۳a_kmS]4+5M:|]4M?;tz?1'jYZgF>8E}Iz쟮 {=ѫ~K5mtC5ڍe$x=s^{jiz.7ڔq紺F^ΛY4)1^t=Q9܊rRuY/4 [_L|>,~a=h@֞mj"k YNwtG־;ݑN^x|i:\':Y4#=ޘ4} !=;~./PEwꢻn?@]tu]_vEwꢻn?@]t,}qݹGW{,L3G,dg|>/1=3l_;c)`ΏV^YG(?Ô@g/+Wh^#b\ki6fϞ. 5~c;g%4/1s .g>] Џ!7ǀ-1*1X&uu.c?:  c̼g1=/Sq}j(ti~ &#Gx)13㏙9n <'cGrNй33Lz: ?v^]c4LW^*>=z3dZuF{󠯎>2>&I|򪖆  d1/٬Lhyh$ z&WG` LRf*`n<6 @W&EAr>^1Y}Lރ>J*LSGoLDz/# T- %uZN Z0},@~@3nUЕGJ5/_fB#ASwԃڃys7cc\mKC'CZ 1̖Gʾ8+:>W[i$q2C3A]d㻦cK|?}4UV4. uE.pr^}y}OSguZ ^@.l(p 6>WkŴFB'ED>8t|[ʳ?yR!Kˠӧi9b}|G'i3>sًcW=C#FB1d=CC$}LV1`@}#TcH0"Iu>}#)#4LX.Q[̃ :9F_:˘e*w ?IB'*{ymz inq35sǟ @iޓ\?B yOݍ.I3>LWG3UzN*9m{}nO/t=/8x>jd6m#虼~u14Ӧyp{|sygj.z>t򗧏>ܿt AoH#:uF--x~f<(g  Du롑m^N3>7x>(1G /o7-/r4-=9t4ٴm13t^#u:sNQ+f@#v}gMܜVk̈́_)+Ho-'۴2C#@#GS6,+7ۮmDl?KAȢӻ*a#P&ˡyewU<'1t2]z]%1F$OʎC#/F=t<#d3JhKyۆJF3]_ȱmQmjQcerӻje?4h/jL}yo Rǿ>x=#?>]|F5/W.t=Bu'H1]Ǟh$И_HYRq$>Wq .s 4h/h,}H"'s^4%h$ИkL}#qw=»F߬m|.Y`}Ѐ5BSHY1f {Oc?x=iot zI]=@K֘OMeJ/Ӊ'u)hAMY#_y??F;>aaP|L'>WTi J秦2<\nl͈lbpiOi '_]tMXnxricE^葦:Fln+W&ZRՋc!d}?_ZoFFot\~pθJ >2vwkט{X:@T!uWh$P#WQU5ll^6]u_9j tl$+OFAK>gyP*?eZR}hEw%)"D*˖zο9rV; ߴAK+%?-ɖkV#Q%MDZ5L_v-\۠aCJQZ ]nwZ39g: }DQנ#u>7|(Od+.{}.{DRrF_}fx;y W<˦Sc=:H/u!>TFQ]y.;G?$YSp~sMh$虡5/])ϕ#7/5u=2هpיsxe{!}:- C|: z`y2}i'/>X:Y{ĝcy#>=>f _fhoÇ>dc KBkCІق y(S#ealxye1 _ij)|FYY/sAψMFW]!~8gx EEZ8>^h9<]Nu/5S:ƶ a~0>NA[t){vI!q1lo!Z! Ne-U 2i wam)8{񱵽mcƴF>jLu&B'A U?&d1X)8x^~$H![_iT3l>~tȏ"5=Y3w'dZQcC1@*LB kϘ3sN$ckto_) ]nwZ3-LGR1- g: w}a[Ntza[?c#\LJ>">4{c[! s8t| :!ҕ:6-[x`@''ؿ/,#/>Wx.{q| >h䤑5ٗJFBF:9YTDoH@#'qzFN #f}p퐵`dS_Sz?#¬F~)MV}h`dڐտN*EJy0?_!o9ğJIP}c^|sq$B yOݍ.I3D?TGyW$BXC?&tR9TG>>Μ &J%A9Z5( | 1? trTTo3;njY PAps~IH@s@'ٗşs{ğ? trP}K^13t^#u:sNQ# ]069]!җ3D4t\k&?~h ]oN8t:)v 읮c-z@.^>0A}`@';{&[f r ڢ4ي6>:#?tG~MVv s>w)QK' N~>b(p|T U Mi:)K9ǘ1=ݏ yxm5| >c:YGҕ\e># >*cM З\\A\DNN@;r~~<\nl͈lbp!>#P< {2RNjhLiz&*uZoul:wF/kl;О<ͫ@M4H LEwd?mt & -=ʾa13L42\7W<˦~$hcgL}dΏV& 0QI>+w7ĘA&Y6٧Y1ƘA~tr}dǀ-1jcg!ȡ[3?ȬoGt~K},GW1ƘA~&עWPs2!}Ċ9- -kcgad6_>?]nr#2cf1fr130UB뜗c E5WCʓmg?o'j1wv{2:Y5] BVU?Xo}~@KZ˘>@K:K9n?zl[w}~YDs;.=yJE%sHǥIyE 0G ϮϢF zsˊ zO:dkZۏ= bGX<: }Cگ[i 蠏5mP8&'s[,Jtr},u .Rbw}eX}B"Ӊ;DQyo>o͉'s:0_lkw]8)|gSyPeoȞkqή!N޻|8NњƂDiqh9{pۛgWgxsˍ=.p+֚-i0].V׺dӤsލ{[Z*MXk8uӖ)|P#y(-׳umZzQ\]cs%1Φ0 ioȧHp hn8Bʺ^z_s:xoUif[L*`!!˻I;B#Frݜ;޶t#2WXٺm23[?8Iݍ.kYax?)~K4I'[M?Iu_KosEug-ػ};,:z}g$Y+?}4:\WW7skk\>:}{u;}GYsҹ88c#(z_Ϧȇ+J}E>mO;N__٬6ߑGqfi>$|'`x>^V&6Lu%?@)EM+Γ6W<%פnթu9Rc+|.]'%\]*Ӛ?]̈́u%7McPHǜg.}QVj{#s_lڼt,|On~וSd_Y(l<Ymy-ZGԽqڗ̹WVʻ\eR-L-}c2~i?-U?o-cibs]f7̆l=-}pr^kPp~7:9kc˷JTUפ\_cQݪ?V? ._{Zg{e1kˆzY\yc%]cw駏3 7]qWǤUm/>{@ieOQy1,JR"2VF=g/s"?yֲח}6|~帄1~dt.*geT7K*)I?=&k||}l,Ύ>>N1&w*}ΞJ34k.sU_\/^Xo~Ghwf&/8Sg;nu5-C?dr?q{Ntg>gWvH^+ZWּk~f}ZkIJ+ʶu#[o g-=V{֡n:YxIgV<`{6>^϶\([dg mrȺ6q߱^Y3<hq|pk;E}̮)^\A{k.+3u7ecsR7<}m#ͱ9s_c)5g_y㵙kq1}I)%#vw~Gx2XvZn{Gi'UUՒ֝)veM'k_]B:,M&^gg;.S_m&>7NgIvaL}Lwy8}CV"7{ql5_nc_8 >d$L)hEw}~/P.R"t?KY4i}5 C_])roїşicC3H!=׆l616T?CzmƟicc3:\'"g/«W?$F3"egZ$F3*e1f4&@/DHdd`UUUUU@@Y@88`@-http://pubs.acs.org/doi/pdf/10.1021/je700174h-DME-Water = J.Chem.Eng.Data 52 p. 1814 (2007)`@YE@@BM6Gx/̻_8׵1mTݬFYF۱DhD ~~ƒ πFo_D?? 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