FSD100MbP?h㈵>d 'dfffffr@!added material template default initializing document added property activity &added property activity.Dtemperature &added property activity.DmolFraction #added property activity.Dpressure $added property activityCoefficient 1added property activityCoefficient.Dtemperature 1added property activityCoefficient.DmolFraction .added property activityCoefficient.Dpressure $added property bubblePointPressure 'added property bubblePointTemperature &added property compressibilityFactor 3added property compressibilityFactor.Dtemperature 3added property compressibilityFactor.DmolFraction 0added property compressibilityFactor.Dpressure added property density %added property density.Dtemperature %added property density.DmolFraction "added property density.Dpressure !added property dewPointPressure $added property dewPointTemperature added property enthalpy &added property enthalpy.Dtemperature &added property enthalpy.DmolFraction #added property enthalpy.Dpressure added property entropy %added property entropy.Dtemperature %added property entropy.DmolFraction "added property entropy.Dpressure added property excessEnthalpy ,added property excessEnthalpy.Dtemperature ,added property excessEnthalpy.DmolFraction )added property excessEnthalpy.Dpressure added property fugacity &added property fugacity.Dtemperature &added property fugacity.DmolFraction #added property fugacity.Dpressure $added property fugacityCoefficient 1added property fugacityCoefficient.Dtemperature 1added property fugacityCoefficient.DmolFraction .added property fugacityCoefficient.Dpressure  added property gibbsFreeEnergy -added property gibbsFreeEnergy.Dtemperature -added property gibbsFreeEnergy.DmolFraction *added property gibbsFreeEnergy.Dpressure added property heatCapacity *added property heatCapacity.Dtemperature *added property heatCapacity.DmolFraction 'added property heatCapacity.Dpressure #added property heatOfVaporization 0added property heatOfVaporization.Dtemperature 0added property heatOfVaporization.DmolFraction -added property heatOfVaporization.Dpressure !added property idealGasEnthalpy .added property idealGasEnthalpy.Dtemperature .added property idealGasEnthalpy.DmolFraction 'added property logFugacityCoefficient 4added property logFugacityCoefficient.Dtemperature 4added property logFugacityCoefficient.DmolFraction 1added property logFugacityCoefficient.Dpressure added property surfaceTension ,added property surfaceTension.Dtemperature ,added property surfaceTension.DmolFraction )added property surfaceTension.Dpressure $added property thermalConductivity 1added property thermalConductivity.Dtemperature 1added property thermalConductivity.DmolFraction .added property thermalConductivity.Dpressure added property vaporPressure +added property vaporPressure.Dtemperature added property viscosity 'added property viscosity.Dtemperature 'added property viscosity.DmolFraction $added property viscosity.Dpressure added property volume $added property volume.Dtemperature $added property volume.DmolFraction !added property volume.Dpressure %inserted unit operation ChemSepUO_1 %inserted unit operation ChemSepUO_2 Gwarning: no route found for stream ; using most direct route inserted stream 1 Gconnected stream 1 to unit ChemSepUO_1 as INLET at port Feed1_stage13 Gwarning: no route found for stream ; using most direct route !(last message repeated 4 times) inserted stream 2 Gconnected stream 2 to unit ChemSepUO_1 as INLET at port Feed2_stage26 inserted stream 3 Econnected stream 3 to unit ChemSepUO_1 as OUTLET at port TopProduct inserted stream 4 Hconnected stream 4 to unit ChemSepUO_1 as OUTLET at port BottomProduct Gconnected stream 4 to unit ChemSepUO_2 as INLET at port Feed1_stage21 inserted stream 5 Econnected stream 5 to unit ChemSepUO_2 as OUTLET at port TopProduct inserted stream 6 Hconnected stream 6 to unit ChemSepUO_2 as OUTLET at port BottomProduct !inserted unit operation Mixer_3 =connected stream 1 to unit Mixer_3 as OUTLET at port Outlet =connected stream 6 to unit Mixer_3 as INLET at port Inlet 2 inserted stream 7 =connected stream 7 to unit Mixer_3 as INLET at port Inlet 1 Saved MCH_Tol_Extraction.fsd  (last message repeated 1 time) solving ChemSepUO_1 :error: calculate failed for unit ChemSepUO_1: no results solving ChemSepUO_1 solving ChemSepUO_2 Restoring flowsheet from file Loaded MCH_Tol_Extraction.fsd Starting solve )solving Mixer_3 ChemSepUO_2 ChemSepUO_1 0Found recycle: Mixer_3 ChemSepUO_2 ChemSepUO_1 Cutting stream 6 converged in 14 iterations Solve finished Restoring flowsheet from file Loaded MCH_Tol_Extraction.fsd Starting solve )solving Mixer_3 ChemSepUO_2 ChemSepUO_1 0Found recycle: Mixer_3 ChemSepUO_2 ChemSepUO_1 Cutting stream 6 converged in 1 evaluation Solve finished Starting solve )solving Mixer_3 ChemSepUO_2 ChemSepUO_1 0Found recycle: Mixer_3 ChemSepUO_2 ChemSepUO_1 Cutting stream 6 converged in 1 evaluation Solve finished =INLET stream 6 disconnected from unit Mixer_3, port Inlet 2 )inserted unit operation HeaterCooler_10 Cconnected stream 6 to unit HeaterCooler_10 as INLET at port Inlet inserted stream 8 MbP?MbP?MbP?2C:\Program Files\COCO\data\DefaultComponentLib.pcdMPhenolC6H5OHC6H6O108-95-2 c1ccccc1(O)@TbWA@O??p|@̠s@s@Tg@`;W@Ķ?`I?d=`&@୊9?[̠s@z@i@h} A)@?ЯjY@p@/?`k@RVw %@`f2t@`f@h=w~@ K@> @`r@o|@e`|> #g?z@Ef@`f~@e@=܉A?V?@.4?Ef@`f~@j2Û@v^0 ?D@Ef@d@`H@%@@`?g|>@3Cf@@@ @̮E)@@)7>tUb@p@;k?u#9L@3@@f@@hv$|@¿좗>@g@zw@er\^>@??5/@h 8Ef@@@fVq<`GU>Ef@}@`Xo> a?@ g@`@ 8zw@@@f? c? 8 8 8Ef@`f~@j~@0_п͟? 8b@p@ 8 8 8 8 8 8 8;5@@ ݄F 8 8`fh@@3@ n?k^< ? 8 8g@zw@ x#4@@33333ξ =DQOI?Zb#>@a@v@v@ ?w@>W? 8 8 8f?@? 84?f??`[@ H?"@s@yS&y?4?Z?lMethylcyclohexane (C6H11)CH3C7H14108-87-2 C1CCCCC1(C)@|JAO?K7?aw@`Rb@`Rb@2#? X@`h?@?`=@ ?EoA@q@zAAYAY~A@33%@[C> 8 8 8`Rb@`c@&?@?@`? 8`Rb@ @i'W@̥@5^%`| >@`Rb@ @eaA@?6Y?ׁ`E ?`Rb@ @j@3@ W"v?|(@`Rb@d@@ d @`p"?`Rb@t@`=@$ d+@ X*<0}>i@p@ ?Ho@`E@@q@P@h` D@޿Q>@o@Gaw@e>? \kp@j@ 8Gaw@@fP?z4o ?@D{`a>`fq@Gaw@{?2?z.@Y@ 8Gaw@@f`R'?`? 8 8 8`Rb@ @jp@Kտ@^ ? 8i@p@ 8 8 8 8 8 8 84@@nrF 8 8 \e@ @ @? ⣿`? 8 8o@Gaw@ K7Ac@YU7i?">7G< @G@?5@?5@"?@!H@`"l? 8 8 8KY?`Ӽ? 8@Ď?ื?Eט?za@`h?@@جt@ F?rm?activityactivityactivityCoefficientactivityCoefficientbubblePointPressurebubblePointPressurebubblePointTemperaturebubblePointTemperaturecompressibilityFactorcompressibilityFactordensitydensitydensity/volume (pure)density/volume (pure)dewPointPressuredewPointPressuredewPointTemperaturedewPointTemperature enthalpyenthalpyentropyentropy excessEnthalpyexcessEnthalpyfugacityfugacityfugacityCoefficientfugacityCoefficientgibbsFreeEnergy gibbsEnergyGG heatCapacityheatCapacityCp78 heatOfVaporizationheatOfVaporizationidealGasEnthalpyidealGasEnthalpy logFugacityCoefficientlogFugacityCoefficientsurfaceTensionsurfaceTensionsurfaceTension (pure)surfaceTension (pure)thermalConductivitythermalConductivity04thermalConductivity (pure)thermalConductivity (pure))1 vaporPressure vaporPressure viscosity viscosity& viscosity (pure)viscosity (pure)" volumevolumeVapor Vapor phaseLiquid Liquid phase QI&?"MethylCycloHexane/Phenol p482 1/2dimported from NRTL.IPDQI&?"MethylCycloHexane/Phenol p482 1/2dimported from NRTL.IPDO {Gz? Phenol/phenolimported from HAYDENO.IPDZ&k"MethylCycloHexane/Phenol p482 1/2dimported from NRTL.IPDD7\@"MethylCycloHexane/Phenol p482 1/2dimported from NRTL.IPD7 4!=p"MethylCycloHexane/Phenol p482 1/2dimported from UNIQUAC.IPDGz`Methyl Cyclohexane/Tolueneimported from UNIQUACP.IPDa@"MethylCycloHexane/Phenol p482 1/2dimported from UNIQUAC.IPD33333Kj@Methyl Cyclohexane/Tolueneimported from UNIQUACP.IPD7 4!=p"MethylCycloHexane/Phenol p482 1/2dimported from UNIQUAC.IPDGz`Methyl Cyclohexane/Tolueneimported from UNIQUACP.IPDa@"MethylCycloHexane/Phenol p482 1/2dimported from UNIQUAC.IPD33333Kj@Methyl Cyclohexane/Tolueneimported from UNIQUACP.IPDACHACOHACCH2CH2ACHqh??K7 *@ACOHh"lxz?(\?S㥛=@ACCH3B?`"?%C ;@CH3ͪ?A`"? rh.@CH2M O?HzG?Zd;O ,@CH F%u?v/?K7 *@Ĕ@d@= ףp=&ףp= W9@fffffn@1X?'>yʊ=>08Hj,i?";g?Eǎ?:w M?? ]$?OՆ#?Ѥ-p?STs:&o?V\?>1X?м@ @2Bottoms9&D'>'9&D'9&9'D'   defaultм@@GV#{@}*]M@f~@Ye7?Ǟ?G?)Z'O?-C6?>[q?0?T †?EY{d?6hQ9?% O>9?=|g:??Ye7?Ǟ?G?)Z'O?-C6?>[q?м@O@2TolueneP"Z"U"P"Z"P"Z"  defaultм@KI9w@G f\#@i?MbP?E/ջP?p4?Cub?