FSD100MbP?h㈵>d 7$@@@dfffffr@м@!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.pcduPhenolC6H5OHC6H6O108-95-2 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?Methylcyclohexane (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 heatOfVaporizationheatOfVaporizationOidealGasEnthalpyidealGasEnthalpy logFugacityCoefficientlogFugacityCoefficientsurfaceTensionsurfaceTensionsurfaceTension (pure)surfaceTension (pure)thermalConductivitythermalConductivity04thermalConductivity (pure)thermalConductivity (pure))1 vaporPressure vaporPressureN 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@l>F#C >*K{:> }N;>?ca?7z?%>l>G#C >,K{:> }N;>??x@м@I@fff@2Toluene & MCH feed... (defaultм@x@4@Qs??Pk??W-ʆ&???Pk??W-ʆ&??Pk??W-ʆ&?x@м@4@Qs?MCH:??:?:?  defaultм@[1uw@R`3@??˞=j= Vܠ?l?d#/?g@?l-B=>C=ZF?=7??Qܝ?c??} ̞=8j=ݠ?tܾ?a/?ŀ?м@ @dB:&>*:*:&>*:&:*>*  defaultм@bT|@|VOI@<= @^Hp?R x?Qe,?>Gk?-C6?`;[?:A*?'vu3?+L2D?aL~?TIA?MB??'6Hp?3* x?=D,?x~>Gk?D|6?Yw=;[?м@O@=TolueneJ#O#O#J#O#J#O#  defaultм@8w@ @?b[?MbP?綹P?!?Ne? l6?a;?)^|6??!yX?fn?<;iX{? `A??MbP?V綹P?g!?%?K6??;?dRecycle SolventJ6 ;8; 6J;J6J; ;  defaultм@o|@R̋]H@h@la?I`z?*l>Q >!]:>ٓEd;>?^ pD?PJHx>WP>Ũ>b> bpb>?¢a?4z?}*l>wZhQ >#\:>"mEd;>2make-up Phenol &defaultм@Pw@?1????????Pw@м@?1? Cold Solvent;';;; defaultм@Pw@R̋]H@h@la?I`z?*l>Q >!]:>ٓEd;>?¢a?4z?}*l>wZhQ >#\:>"mEd;>??r@?I@+l@21    defaultм@Pw@@2k?oB??????2Extractive DistillationChemSep Unit OperationqeWCXc'CSUO-[ChemSep] Version=6.31 Name=C:\DOCUME~1\Harry\LOCALS~1\Temp\CS354.sep Title=ChemSep CO Unit Operation "Extractive Distillation" in COFE Flowsheet User=Harry Date=2009-04-12 Time=11:02:01 [Cape-Open] unitname=Extractive Distillation CO_ID=CS354 3 components Phenol 108-95-2 94.1129989624 Mw Toluene 108-88-3 92.1405029297 Mw Methylcyclohexane 108-87-2 98.1882019043 Mw 0 thermo exe=C:\PROGRA~1\ChemSepL\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 [Paths] Device drivers path=c:\progra~1\chemsepl\bin\ Help and Info path=c:\progra~1\chemsepl\help\ Component data path=c:\progra~1\chemsepl\pcd\ Property data path=c:\progra~1\chemsepl\ipd\ Section data path=c:\progra~1\chemsepl\ild\ Executables path=C:\PROGRA~1\ChemSepL\bin\ Temporary path=WINTMPDIR Scripts path=c:\progra~1\chemsepl\bin\ [Units] Temperature=K Flow=mol/s Mass flow=kg/s Pressure=N/m2 Heat=J/s Enthalpy=J/kmol Entropy=J/kmol/K Fraction= Length=m 1/Length=1/m Area=m2 Volume=m3 Mass=kg Angle=rad Velocity=m/s Surface tension=N/m Density=kg/m3 Molar density=kmol/m3 Viscosity=N/m2.s Molecular weight=kg/kmol Heat capacity=J/kmol/K Thermal conductivity=J/s/m/K Diffusivity=m2/s Interaction parameter=J/mol Time=s [Components] 3 126 1181 Library Offset, Index DT=2009-03-26,23:59:44 CHK=780 CAS=108-95-2 CID=Phenol Name=Phenol Lib=c:\progra~1\chemsepl\pcd\chemsep1.pcd 140 502 Library Offset, Index DT=2009-03-26,23:59:44 CHK=60854 CAS=108-88-3 CID=Toluene Name=Toluene Lib=c:\progra~1\chemsepl\pcd\chemsep1.pcd 144 138 Library Offset, Index DT=2009-03-26,23:59:44 CHK=18409 CAS=108-87-2 CID=Methylcyclohexane Name=Methylcyclohexane Lib=c:\progra~1\chemsepl\pcd\chemsep1.pcd [Operation] 2 Operation Column 2 Operation kind Extractive Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 40 Stages 2 Feed stages 0 Sidestream stages F=10, 25 S= 0 Pumparound stages P= [Properties] [Thermodynamics] 4 K model DECHEMA 8 Activity coefficient UNIFAC * Wilson model * * UNIQUAC model * 3 Equation of State Cubic 5 Cubic EOS Peng-Robinson * Virial EOS * 1 Vapour pressure Antoine [Enthalpy] 3 Enthalpy Excess 1 Enthalpy reference state Vapour 298.15 Enthalpy reference temperature 1 Formation enthalpies Excluded 298.15 Exergy surroundings temperature [Physical property models] 0 No Check T range * Cubic EOS * * Virial EOS * * Vapour model * * Liquid mixture density * * Liquid component density * * Vapour mixture viscosity * * Vapour mixture viscosity pressure correction * * Vapour component viscosity * * Liquid mixture viscosity * * Liquid component viscosity * Vapour mixture Cp * Vapour component Cp * Liquid mixture Cp * Liquid component Cp * Vapour mixture conductivity * * Vapour component conductivity * * Liquid mixture conductivity * * Liquid component conductivity * Mixture surface tension * * Component surface tension * * Vignes MS D-model * * D mixture model * * Vapour Diffusion Coefficients * [Reaction data] 0 Number of reactions [Specifications] Top Bottom [Heaters/Coolers] 0 Number 0 Column duty Qcolumn 2 First stage 39 Last stage [Efficiencies] 1 Default efficiency 0 Number [Pressures] 1 Column pressure Constant pressure 101325 Condenser pressure 101325 Top pressure * Pressure Drop * Bottom pressure [Feeds] 2 Number 1 Feed state T & p 10 Stage Feed1{split} 373 Temperature 101325 Pressure 0 Vapour fraction 3 componentflows 0.0499998898851 Component 1 flow 1.09805445076e-007 Component 2 flow 3.09483547105e-010 Component 3 flow 1 Feed state T & p 25 Stage Feed2{split} 384 Temperature 101325 Pressure 1 Vapour fraction 3 componentflows 0 Component 1 flow 0.01 Component 2 flow 0.01 Component 3 flow [Condenser] 1 Type Reflux ratio 8 Value Qcondenser * Type * * Initialization guess [Reboiler] 7 Type Mole fraction of a component 0.0001 Value Qreboiler 3 1st comp. * Type * * Initialization guess [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 [Programs] Temporary file=SCRATCH.TMP User program= 8 DOS extender NT 1 Show windows Hidden [FlowSheet] [CoCo] [Settings] -1 -1 -1 0 Graph settings 1 Auto colors 1 Auto points 0.2 StringGrid5 2 8 Title Labels Stages Axis color Commands Box Labels box Import data StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 y1 x2 y2 StringGrid3 1 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage 0 Graph settings -1 -1 StringGrid7 16 2 StringGrid11 5 3 -1 -1 -1 0.95 0.95 1.2 1 0 Use old results 1 Automatic 0 Keep sep-files 1 Restore original StringGrid1 1 6 StringGrid2 4 1 StringGrid3 1 1 None -1 -1 -1 21 Binary Phase Diagram T p x -1 -1 StringGrid1 3 5 -1 -1 -1 0 21 Ternary Phase Diagram T 0 1 1 StringGrid1 3 5 0 0 -1 -1 -1 21 Binary Property Diagram 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 -1 -1 [End Settings] [End of Input] [Results] 1 Converged 0 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow 1 378.5989894 1.013250000E+05 1.937868231E-02 1.550294585E-01 2 379.2426441 1.013250000E+05 1.744081408E-01 1.543993146E-01 3 379.8031751 1.013250000E+05 1.737779969E-01 1.538718023E-01 4 380.2767119 1.013250000E+05 1.732504846E-01 1.534403142E-01 5 380.6667956 1.013250000E+05 1.728189965E-01 1.530932697E-01 6 380.9823330 1.013250000E+05 1.724719520E-01 1.528101423E-01 7 381.2421784 1.013250000E+05 1.721888246E-01 1.524923113E-01 8 381.5499767 1.013250000E+05 1.718709936E-01 1.512364440E-01 9 382.8834854 1.013250000E+05 1.706151263E-01 1.426654210E-01 10 392.2148035 1.013250000E+05 1.620441033E-01 2.068279385E-01 11 392.2806002 1.013250000E+05 1.762066208E-01 2.067871466E-01 12 392.3314718 1.013250000E+05 1.761658289E-01 2.067557156E-01 13 392.3707137 1.013250000E+05 1.761343979E-01 2.067315337E-01 14 392.4009309 1.013250000E+05 1.761102160E-01 2.067129508E-01 15 392.4241672 1.013250000E+05 1.760916331E-01 2.066986837E-01 16 392.4420163 1.013250000E+05 1.760773660E-01 2.066877393E-01 17 392.4557139 1.013250000E+05 1.760664216E-01 2.066793574E-01 18 392.4662095 1.013250000E+05 1.760580397E-01 2.066729843E-01 19 392.4742011 1.013250000E+05 1.760516666E-01 2.066683481E-01 20 392.4800604 1.013250000E+05 1.760470304E-01 2.066659783E-01 21 392.4832820 1.013250000E+05 1.760446606E-01 2.066698043E-01 22 392.4796977 1.013250000E+05 1.760484866E-01 2.066996851E-01 23 392.4480376 1.013250000E+05 1.760783674E-01 2.068519510E-01 24 392.2850050 1.013250000E+05 1.762306333E-01 2.075462989E-01 25 392.6123580 1.013250000E+05 1.569249812E-01 2.073513499E-01 26 392.8913345 1.013250000E+05 1.567300322E-01 2.071884814E-01 27 393.1261524 1.013250000E+05 1.565671637E-01 2.070536283E-01 28 393.3217666 1.013250000E+05 1.564323106E-01 2.069427657E-01 29 393.4833687 1.013250000E+05 1.563214480E-01 2.068519945E-01 30 393.6161641 1.013250000E+05 1.562306768E-01 2.067770548E-01 31 393.7258994 1.013250000E+05 1.561557371E-01 2.067102367E-01 32 393.8226949 1.013250000E+05 1.560889190E-01 2.066239802E-01 33 393.9417104 1.013250000E+05 1.560026626E-01 2.063860788E-01 34 394.2503475 1.013250000E+05 1.557647611E-01 2.053490085E-01 35 395.5688845 1.013250000E+05 1.547276908E-01 2.009218769E-01 36 401.2015691 1.013250000E+05 1.503005592E-01 1.888348666E-01 37 416.9891358 1.013250000E+05 1.382135489E-01 1.760976696E-01 38 437.1895634 1.013250000E+05 1.254763519E-01 1.739481373E-01 39 448.9646354 1.013250000E+05 1.233268196E-01 1.757348295E-01 40 453.2969690 1.013250000E+05 1.251135118E-01 5.062131769E-02 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.2036916E+08 -0.2036916E+08 0.3899315E+05 -0.4443826E+05 2 0.1134889E+08 -0.2060724E+08 0.3877077E+05 -0.4502685E+05 3 0.1125238E+08 -0.2081420E+08 0.3843639E+05 -0.4565769E+05 4 0.1116557E+08 -0.2098882E+08 0.3804538E+05 -0.4627712E+05 5 0.1109038E+08 -0.2113252E+08 0.3764327E+05 -0.4684846E+05 6 0.1102737E+08 -0.2124869E+08 0.3726268E+05 -0.4734969E+05 7 0.1097716E+08 -0.2134429E+08 0.3692767E+05 -0.4775985E+05 8 0.1095193E+08 -0.2145703E+08 0.3669693E+05 -0.4798769E+05 9 0.1108972E+08 -0.2192738E+08 0.3705247E+05 -0.4764368E+05 10 0.1239712E+08 -0.2445685E+08 0.4124815E+05 -0.4719249E+05 11 0.1238041E+08 -0.2447519E+08 0.4113398E+05 -0.4728622E+05 12 0.1236741E+08 -0.2448937E+08 0.4104378E+05 -0.4735973E+05 13 0.1235734E+08 -0.2450030E+08 0.4097303E+05 -0.4741707E+05 14 0.1234956E+08 -0.2450873E+08 0.4091785E+05 -0.4746161E+05 15 0.1234356E+08 -0.2451520E+08 0.4087499E+05 -0.4749608E+05 16 0.1233895E+08 -0.2452018E+08 0.4084181E+05 -0.4752270E+05 17 0.1233540E+08 -0.2452400E+08 0.4081619E+05 -0.4754321E+05 18 0.1233267E+08 -0.2452692E+08 0.4079645E+05 -0.4755900E+05 19 0.1233057E+08 -0.2452915E+08 0.4078123E+05 -0.4757112E+05 20 0.1232892E+08 -0.2453081E+08 0.4076942E+05 -0.4758043E+05 21 0.1232747E+08 -0.2453182E+08 0.4075974E+05 -0.4758756E+05 22 0.1232549E+08 -0.2453134E+08 0.4074947E+05 -0.4759294E+05 23 0.1231979E+08 -0.2452501E+08 0.4072796E+05 -0.4759670E+05 24 0.1229538E+08 -0.2449133E+08 0.4064605E+05 -0.4759791E+05 25 0.1220897E+08 -0.2458312E+08 0.3998289E+05 -0.4811887E+05 26 0.1213319E+08 -0.2466134E+08 0.3934812E+05 -0.4860049E+05 27 0.1206787E+08 -0.2472718E+08 0.3875555E+05 -0.4903744E+05 28 0.1201238E+08 -0.2478204E+08 0.3821375E+05 -0.4942766E+05 29 0.1196581E+08 -0.2482737E+08 0.3772687E+05 -0.4977155E+05 30 0.1192715E+08 -0.2486459E+08 0.3729568E+05 -0.5007127E+05 31 0.1189550E+08 -0.2489523E+08 0.3691891E+05 -0.5032998E+05 32 0.1187066E+08 -0.2492163E+08 0.3659592E+05 -0.5055110E+05 33 0.1185603E+08 -0.2495095E+08 0.3633710E+05 -0.5073626E+05 34 0.1187334E+08 -0.2501577E+08 0.3621436E+05 -0.5087651E+05 35 0.1203414E+08 -0.2526402E+08 0.3660492E+05 -0.5091533E+05 36 0.1279359E+08 -0.2610720E+08 0.3905143E+05 -0.5067257E+05 37 0.1496979E+08 -0.2710994E+08 0.4620913E+05 -0.4962134E+05 38 0.1773226E+08 -0.2657263E+08 0.5395930E+05 -0.4746854E+05 39 0.1927171E+08 -0.2572046E+08 0.5550418E+05 -0.4622549E+05 40 0.1981399E+08 -0.2534320E+08 0.5436570E+05 -0.4597645E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.9565887E+02 0.3193554E+01 0.8530813E-05 0.1589831E+06 0.1969720E-01 2 0.9525972E+02 0.3173754E+01 0.8581812E-05 0.1563129E+06 0.1960921E-01 3 0.9490409E+02 0.3156303E+01 0.8627261E-05 0.1539183E+06 0.1952918E-01 4 0.9459774E+02 0.3141410E+01 0.8666431E-05 0.1518442E+06 0.1945906E-01 5 0.9434130E+02 0.3129036E+01 0.8699241E-05 0.1501003E+06 0.1939956E-01 6 0.9413168E+02 0.3118976E+01 0.8726098E-05 0.1486700E+06 0.1935047E-01 7 0.9396362E+02 0.3110865E+01 0.8747867E-05 0.1475229E+06 0.1931161E-01 8 0.9383118E+02 0.3103566E+01 0.8767504E-05 0.1466492E+06 0.1928999E-01 9 0.9373106E+02 0.3088320E+01 0.8808469E-05 0.1463211E+06 0.1937012E-01 10 0.9368666E+02 0.3006911E+01 0.9037800E-05 0.1486259E+06 0.2015202E-01 11 0.9364358E+02 0.3004931E+01 0.9043556E-05 0.1483171E+06 0.2014123E-01 12 0.9361020E+02 0.3003399E+01 0.9048017E-05 0.1480776E+06 0.2013285E-01 13 0.9358442E+02 0.3002216E+01 0.9051464E-05 0.1478926E+06 0.2012637E-01 14 0.9356453E+02 0.3001304E+01 0.9054122E-05 0.1477498E+06 0.2012137E-01 15 0.9354923E+02 0.3000603E+01 0.9056168E-05 0.1476399E+06 0.2011752E-01 16 0.9353746E+02 0.3000064E+01 0.9057741E-05 0.1475554E+06 0.2011455E-01 17 0.9352842E+02 0.2999650E+01 0.9058949E-05 0.1474905E+06 0.2011227E-01 18 0.9352149E+02 0.2999332E+01 0.9059876E-05 0.1474407E+06 0.2011053E-01 19 0.9351617E+02 0.2999089E+01 0.9060586E-05 0.1474024E+06 0.2010918E-01 20 0.9351209E+02 0.2998905E+01 0.9061123E-05 0.1473731E+06 0.2010812E-01 21 0.9350896E+02 0.2998775E+01 0.9061505E-05 0.1473502E+06 0.2010721E-01 22 0.9350652E+02 0.2998723E+01 0.9061651E-05 0.1473308E+06 0.2010599E-01 23 0.9350450E+02 0.2998919E+01 0.9061067E-05 0.1473074E+06 0.2010260E-01 24 0.9350218E+02 0.3000193E+01 0.9057276E-05 0.1472480E+06 0.2008819E-01 25 0.9328417E+02 0.2990241E+01 0.9086410E-05 0.1456801E+06 0.2003295E-01 26 0.9309629E+02 0.2981706E+01 0.9111542E-05 0.1443251E+06 0.1998493E-01 27 0.9293665E+02 0.2974485E+01 0.9132916E-05 0.1431711E+06 0.1994384E-01 28 0.9280262E+02 0.2968444E+01 0.9150877E-05 0.1422003E+06 0.1990914E-01 29 0.9269121E+02 0.2963436E+01 0.9165818E-05 0.1413920E+06 0.1988016E-01 30 0.9259936E+02 0.2959315E+01 0.9178151E-05 0.1407248E+06 0.1985620E-01 31 0.9252416E+02 0.2955935E+01 0.9188290E-05 0.1401783E+06 0.1983664E-01 32 0.9246298E+02 0.2953126E+01 0.9196739E-05 0.1397351E+06 0.1982132E-01 33 0.9241371E+02 0.2950532E+01 0.9204580E-05 0.1393871E+06 0.1981230E-01 34 0.9237564E+02 0.2946776E+01 0.9216079E-05 0.1391661E+06 0.1982285E-01 35 0.9235424E+02 0.2935451E+01 0.9251403E-05 0.1392896E+06 0.1992070E-01 36 0.9238466E+02 0.2892003E+01 0.9392723E-05 0.1406379E+06 0.2037045E-01 37 0.9261139E+02 0.2782004E+01 0.9801370E-05 0.1443604E+06 0.2150762E-01 38 0.9319278E+02 0.2663573E+01 0.1037866E-04 0.1477148E+06 0.2240603E-01 39 0.9374686E+02 0.2606641E+01 0.1075579E-04 0.1484798E+06 0.2242157E-01 40 0.9400315E+02 0.2588110E+01 0.1090379E-04 0.1484639E+06 0.2229063E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.9525972E+02 0.7512387E+03 0.2727452E-03 0.2028054E+06 0.1025101E+00 0.1658580E-01 2 0.9485946E+02 0.7551905E+03 0.2695453E-03 0.2004117E+06 0.1037426E+00 0.1679406E-01 3 0.9451437E+02 0.7586601E+03 0.2668279E-03 0.1983416E+06 0.1048030E+00 0.1697253E-01 4 0.9422531E+02 0.7616122E+03 0.2645810E-03 0.1966030E+06 0.1056897E+00 0.1712125E-01 5 0.9398889E+02 0.7640589E+03 0.2627637E-03 0.1951781E+06 0.1064139E+00 0.1724238E-01 6 0.9379925E+02 0.7660487E+03 0.2613258E-03 0.1940340E+06 0.1069950E+00 0.1733948E-01 7 0.9364964E+02 0.7677017E+03 0.2602778E-03 0.1931400E+06 0.1074628E+00 0.1741895E-01 8 0.9353518E+02 0.7697442E+03 0.2603409E-03 0.1925642E+06 0.1079281E+00 0.1751348E-01 9 0.9347298E+02 0.7790166E+03 0.2694593E-03 0.1933938E+06 0.1093134E+00 0.1791759E-01 10 0.9360564E+02 0.8374240E+03 0.3362229E-03 0.2022741E+06 0.1169563E+00 0.2019316E-01 11 0.9357720E+02 0.8378217E+03 0.3359398E-03 0.2021015E+06 0.1170461E+00 0.2020693E-01 12 0.9355522E+02 0.8381294E+03 0.3357213E-03 0.2019681E+06 0.1171154E+00 0.2021756E-01 13 0.9353828E+02 0.8383668E+03 0.3355530E-03 0.2018653E+06 0.1171689E+00 0.2022575E-01 14 0.9352524E+02 0.8385497E+03 0.3354235E-03 0.2017861E+06 0.1172100E+00 0.2023206E-01 15 0.9351521E+02 0.8386904E+03 0.3353240E-03 0.2017252E+06 0.1172417E+00 0.2023690E-01 16 0.9350752E+02 0.8387985E+03 0.3352476E-03 0.2016784E+06 0.1172659E+00 0.2024062E-01 17 0.9350161E+02 0.8388815E+03 0.3351890E-03 0.2016425E+06 0.1172846E+00 0.2024347E-01 18 0.9349708E+02 0.8389450E+03 0.3351439E-03 0.2016150E+06 0.1172988E+00 0.2024565E-01 19 0.9349360E+02 0.8389935E+03 0.3351090E-03 0.2015938E+06 0.1173098E+00 0.2024732E-01 20 0.9349093E+02 0.8390291E+03 0.3350806E-03 0.2015773E+06 0.1173179E+00 0.2024854E-01 21 0.9348886E+02 0.8390493E+03 0.3350508E-03 0.2015636E+06 0.1173233E+00 0.2024923E-01 22 0.9348714E+02 0.8390308E+03 0.3349894E-03 0.2015476E+06 0.1173232E+00 0.2024857E-01 23 0.9348517E+02 0.8388541E+03 0.3347583E-03 0.2015093E+06 0.1173028E+00 0.2024240E-01 24 0.9348056E+02 0.8379367E+03 0.3336942E-03 0.2013545E+06 0.1171896E+00 0.2021032E-01 25 0.9333874E+02 0.8399272E+03 0.3322965E-03 0.2004918E+06 0.1176360E+00 0.2027862E-01 26 0.9321829E+02 0.8416292E+03 0.3311154E-03 0.1997580E+06 0.1180147E+00 0.2033639E-01 27 0.9311722E+02 0.8430658E+03 0.3301284E-03 0.1991414E+06 0.1183322E+00 0.2038470E-01 28 0.9303322E+02 0.8442655E+03 0.3293112E-03 0.1986285E+06 0.1185958E+00 0.2042472E-01 29 0.9296400E+02 0.8452585E+03 0.3286401E-03 0.1982055E+06 0.1188130E+00 0.2045764E-01 30 0.9290734E+02 0.8460758E+03 0.3280937E-03 0.1978592E+06 0.1189909E+00 0.2048459E-01 31 0.9286127E+02 0.8467512E+03 0.3276592E-03 0.1975786E+06 0.1191366E+00 0.2050677E-01 32 0.9282424E+02 0.8473430E+03 0.3273572E-03 0.1973588E+06 0.1192597E+00 0.2052616E-01 33 0.9279598E+02 0.8480486E+03 0.3273743E-03 0.1972226E+06 0.1193857E+00 0.2054939E-01 34 0.9278198E+02 0.8497955E+03 0.3287412E-03 0.1973283E+06 0.1196246E+00 0.2060721E-01 35 0.9281416E+02 0.8570049E+03 0.3364550E-03 0.1984745E+06 0.1204919E+00 0.2084259E-01 36 0.9300760E+02 0.8853550E+03 0.3671343E-03 0.2034717E+06 0.1237997E+00 0.2170029E-01 37 0.9345052E+02 0.9479903E+03 0.4226123E-03 0.2144785E+06 0.1311970E+00 0.2314677E-01 38 0.9384654E+02 0.1003555E+04 0.4452942E-03 0.2241343E+06 0.1384724E+00 0.2373920E-01 39 0.9402799E+02 0.1028411E+04 0.4433787E-03 0.2283542E+06 0.1422450E+00 0.2372505E-01 40 0.9408939E+02 0.1036715E+04 0.4408155E-03 0.2297202E+06 0.1436091E+00 0.2367889E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.875886534E-11 0.123253995E-09 0.151234774E-08 0.179552861E-07 0.208660623E-06 2 0.418229760E+00 0.484230247E+00 0.543034772E+00 0.593690829E+00 0.636093686E+00 3 0.581770240E+00 0.515769752E+00 0.456965226E+00 0.406309153E+00 0.363906105E+00 Component Mole fractions on stages: 6 to 10 1 0.238386059E-05 0.268633520E-04 0.299304892E-03 0.328818988E-02 0.339046133E-01 2 0.670753132E+00 0.698525496E+00 0.720241331E+00 0.734782826E+00 0.721493583E+00 3 0.329244485E+00 0.301447641E+00 0.279459365E+00 0.261928984E+00 0.244601803E+00 Component Mole fractions on stages: 11 to 15 1 0.340080200E-01 0.340881380E-01 0.341500402E-01 0.341977660E-01 0.342345009E-01 2 0.728546666E+00 0.734011572E+00 0.738234137E+00 0.741489776E+00 0.743995751E+00 3 0.237445314E+00 0.231900290E+00 0.227615823E+00 0.224312458E+00 0.221769748E+00 Component Mole fractions on stages: 16 to 20 1 0.342627383E-01 0.342844144E-01 0.343010006E-01 0.343134913E-01 0.343219663E-01 2 0.745922230E+00 0.747401776E+00 0.748537260E+00 0.749408360E+00 0.750077168E+00 3 0.219815032E+00 0.218313809E+00 0.217161740E+00 0.216278148E+00 0.215600866E+00 Component Mole fractions on stages: 21 to 25 1 0.343232070E-01 0.342990801E-01 0.341609068E-01 0.334834987E-01 0.339923656E-01 2 0.750594432E+00 0.751013199E+00 0.751441179E+00 0.752281137E+00 0.787986969E+00 3 0.215082361E+00 0.214687721E+00 0.214397915E+00 0.214235364E+00 0.178020665E+00 Component Mole fractions on stages: 26 to 30 1 0.344307137E-01 0.348030549E-01 0.351156338E-01 0.353756453E-01 0.355911825E-01 2 0.818757979E+00 0.844903519E+00 0.866855041E+00 0.885102214E+00 0.900144514E+00 3 0.146811307E+00 0.120293427E+00 0.980293252E-01 0.795221403E-01 0.642643034E-01 Component Mole fractions on stages: 31 to 35 1 0.357740697E-01 0.359569448E-01 0.362845776E-01 0.374945833E-01 0.434240986E-01 2 0.912455861E+00 0.922448671E+00 0.930375257E+00 0.935853375E+00 0.935397646E+00 3 0.517700692E-01 0.415943846E-01 0.333401652E-01 0.266520422E-01 0.211782554E-01 Component Mole fractions on stages: 36 to 40 1 0.734263165E-01 0.203706089E+00 0.515696998E+00 0.808278092E+00 0.942692401E+00 2 0.910149581E+00 0.784871670E+00 0.478504605E+00 0.189731962E+00 0.567799867E-01 3 0.164241026E-01 0.114222413E-01 0.579839687E-02 0.198994583E-02 0.527612169E-03 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.123254162E-09 0.168669402E-08 0.202010757E-07 0.234997766E-06 0.268559618E-05 2 0.484230247E+00 0.550415338E+00 0.607476343E+00 0.655273218E+00 0.694363364E+00 3 0.515769752E+00 0.449584661E+00 0.392523637E+00 0.344726547E+00 0.305633950E+00 Component Mole fractions on stages: 6 to 10 1 0.302700237E-04 0.337340463E-03 0.370952208E-02 0.385099811E-01 0.270719475E+00 2 0.725701437E+00 0.750233556E+00 0.766887381E+00 0.753721791E+00 0.575314389E+00 3 0.274268292E+00 0.249429103E+00 0.229403097E+00 0.207768228E+00 0.153966136E+00 Component Mole fractions on stages: 11 to 15 1 0.270834424E+00 0.270923148E+00 0.270991501E+00 0.271044081E+00 0.271084481E+00 2 0.579939817E+00 0.583513582E+00 0.586268894E+00 0.588389694E+00 0.590020034E+00 3 0.149225760E+00 0.145563270E+00 0.142739606E+00 0.140566226E+00 0.138895485E+00 Component Mole fractions on stages: 16 to 20 1 0.271115485E+00 0.271139219E+00 0.271157162E+00 0.271169695E+00 0.271173467E+00 2 0.591272127E+00 0.592233047E+00 0.592970263E+00 0.593536466E+00 0.593975293E+00 3 0.137612388E+00 0.136627734E+00 0.135872575E+00 0.135293840E+00 0.134851240E+00 Component Mole fractions on stages: 21 to 25 1 0.271148531E+00 0.270996587E+00 0.270245122E+00 0.266611181E+00 0.267161219E+00 2 0.594334913E+00 0.594722139E+00 0.595553117E+00 0.598763668E+00 0.621844553E+00 3 0.134516557E+00 0.134281273E+00 0.134201761E+00 0.134625150E+00 0.110994228E+00 Component Mole fractions on stages: 26 to 30 1 0.267625535E+00 0.268013330E+00 0.268334505E+00 0.268599523E+00 0.268822084E+00 2 0.641447293E+00 0.657899507E+00 0.671571206E+00 0.682838616E+00 0.692057253E+00 3 0.909271723E-01 0.740871633E-01 0.600942885E-01 0.485618607E-01 0.391206628E-01 Component Mole fractions on stages: 31 to 35 1 0.269035507E+00 0.269380172E+00 0.270562083E+00 0.276206949E+00 0.303779409E+00 2 0.699531678E+00 0.705423253E+00 0.709298423E+00 0.707810872E+00 0.683909269E+00 3 0.314328152E-01 0.251965753E-01 0.201394936E-01 0.159821794E-01 0.123113221E-01 Component Mole fractions on stages: 36 to 40 1 0.413879362E+00 0.651386761E+00 0.860499465E+00 0.955664110E+00 0.987724439E+00 2 0.577733571E+00 0.344452913E+00 0.138060590E+00 0.439314535E-01 0.121755613E-01 3 0.838706682E-02 0.416032659E-02 0.143994541E-02 0.404436294E-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 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 30 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 31 to 35 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 36 to 40 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 [Condenser Heat Duty] -5.531886853E+06 [Reboiler Heat Duty] 5.716071563E+06 [K-values] Component K-values on stages: 1 to 5 1 0.710634816E-01 0.730743256E-01 0.748647266E-01 0.764061993E-01 0.776962021E-01 2 0.863700198E+00 0.879754278E+00 0.893919210E+00 0.906020287E+00 0.916081867E+00 3 0.112796502E+01 0.114721386E+01 0.116417250E+01 0.117864190E+01 0.119065995E+01 Component K-values on stages: 6 to 10 1 0.787531789E-01 0.796327598E-01 0.806855668E-01 0.853853933E-01 0.125238915E+00 2 0.924282491E+00 0.931077382E+00 0.939174835E+00 0.974872739E+00 0.125408576E+01 3 0.120044677E+01 0.120855039E+01 0.121820223E+01 0.126067872E+01 0.158867274E+01 Component K-values on stages: 11 to 15 1 0.125567568E+00 0.125822168E+00 0.126018861E+00 0.126170495E+00 0.126287203E+00 2 0.125624530E+01 0.125791686E+01 0.125920741E+01 0.126020184E+01 0.126096693E+01 3 0.159118181E+01 0.159312367E+01 0.159462275E+01 0.159577777E+01 0.159666635E+01 Component K-values on stages: 16 to 20 1 0.126376914E+00 0.126445796E+00 0.126498597E+00 0.126538813E+00 0.126568306E+00 2 0.126155487E+01 0.126200620E+01 0.126235210E+01 0.126261553E+01 0.126280870E+01 3 0.159734916E+01 0.159787330E+01 0.159827500E+01 0.159858091E+01 0.159880521E+01 Component K-values on stages: 21 to 25 1 0.126584521E+00 0.126566465E+00 0.126407117E+00 0.125589251E+00 0.127235404E+00 2 0.126291492E+01 0.126279677E+01 0.126175341E+01 0.125639075E+01 0.126717677E+01 3 0.159892854E+01 0.159879122E+01 0.159757900E+01 0.159134726E+01 0.160387318E+01 Component K-values on stages: 26 to 30 1 0.128652573E+00 0.129855687E+00 0.130865144E+00 0.131704051E+00 0.132396796E+00 2 0.127642285E+01 0.128424404E+01 0.129078649E+01 0.129620996E+01 0.130067926E+01 3 0.161460324E+01 0.162367435E+01 0.163125860E+01 0.163754311E+01 0.164272021E+01 Component K-values on stages: 31 to 35 1 0.132971555E+00 0.133480295E+00 0.134108139E+00 0.135748153E+00 0.142946155E+00 2 0.130438104E+01 0.130765277E+01 0.131168381E+01 0.132217999E+01 0.136772184E+01 3 0.164700708E+01 0.165079517E+01 0.165546194E+01 0.166761000E+01 0.172022593E+01 Component K-values on stages: 36 to 40 1 0.177409949E+00 0.312726787E+00 0.599299615E+00 0.845776338E+00 0.954408300E+00 2 0.157537942E+01 0.227860366E+01 0.346590296E+01 0.431881821E+01 0.466343893E+01 3 0.195826538E+01 0.274551554E+01 0.402681713E+01 0.492029490E+01 0.527612169E+01 [Molecular weights] 1 94.113 2 92.141 3 98.188 [Feed stream 1] 10 Stage Number 5.0000000000029E-02 Flow rate 3.7300000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -4.2054189500954E+07 Enthalpy [J/kmol] -8.5739300072761E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9999779770143E-01 Mole fraction of component 1 2.1961089015187E-06 Mole fraction of component 2 6.1896709420965E-09 Mole fraction of component 3 5.0000000000029E-02 Flow rate 9.9999779770143E-01 Mole fraction of component 1 2.1961089015187E-06 Mole fraction of component 2 6.1896709420965E-09 Mole fraction of component 3 9.4112994655810E+01 Molar mass 1.1184016785816E+03 Density 1.1149003841730E-03 Viscosity 1.4884135995272E-01 Thermal conductivity 2.1570061514853E+05 Heat capacity 3.2491866295125E-02 Surface tension [Feed stream 2] 25 Stage Number 2.0000000000000E-02 Flow rate 3.8400000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] 1.2044584296216E+07 Enthalpy [J/kmol] 4.0596962627597E+04 Entropy [J/kmol/K] 1.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 0.0000000000000E+00 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 5.0000000000000E-01 Mole fraction of component 3 2.0000000000000E-02 Flow rate 0.0000000000000E+00 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 5.0000000000000E-01 Mole fraction of component 3 9.5164352416992E+01 Molar mass 3.1272844887241E+00 Density 8.6958338767964E-06 Viscosity 2.0032063277787E-02 Thermal conductivity 1.5745502083969E+05 Heat capacity [Top product] 1 Stage Number 1.9378682310000E-02 Flow rate 3.7859898940000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.0369159530816E+07 Enthalpy [J/kmol] -4.4438258509426E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.2325416200000E-10 Mole fraction of component 1 4.8423024700000E-01 Mole fraction of component 2 5.1576975200000E-01 Mole fraction of component 3 1.9378682310000E-02 Flow rate 1.2325416200000E-10 Mole fraction of component 1 4.8423024700000E-01 Mole fraction of component 2 5.1576975200000E-01 Mole fraction of component 3 9.5259723049452E+01 Molar mass 7.5123871748569E+02 Density 2.7274524493388E-04 Viscosity 1.0251010821798E-01 Thermal conductivity 2.0280541745063E+05 Heat capacity 1.6585799614394E-02 Surface tension [Bottom product] 40 Stage Number 5.0621317690000E-02 Flow rate 4.5329696900000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.5343196479721E+07 Enthalpy [J/kmol] -4.5976445922282E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.8772443900000E-01 Mole fraction of component 1 1.2175561300000E-02 Mole fraction of component 2 1.0000000000000E-04 Mole fraction of component 3 5.0621317690000E-02 Flow rate 9.8772443900000E-01 Mole fraction of component 1 1.2175561300000E-02 Mole fraction of component 2 1.0000000000000E-04 Mole fraction of component 3 9.4089390264570E+01 Molar mass 1.0367153649572E+03 Density 4.4081548026508E-04 Viscosity 1.4360906066350E-01 Thermal conductivity 2.2972015142158E+05 Heat capacity 2.3678887343152E-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(iuw@w@b7"ټw@uimw@1w@΢w@x@*Ralx@9+&x@%F9y@؄z@LsS{@y%o|@bT|@"Pressure profile.Pressure at each stage(м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@(Vapour Flow profile4Vapour Flow at each stage(R`3@:K}e@vIWc@aS.b@dFa@|^_@Fl^@r-CG_@(Liquid Flow profile4Liquid Flow at each stage(R`c@zi/Lc@|;c@ .c@"c@fsc@pc@b@J" Ka@.x~i@ N0i@wb{.i@\hi@52~i@7[i@5i@vKi@^i@ci@KOi@ gm oi@ci@mY.Ci@G{i@~>%B>i@% i@{TRi@L)"+i@;Ci@e&i@hPBi@@ Si@uZi@ְ+i@i@(:g@: f@$We@Z'e@|VOI@4Vapour Moleweight profile@Vapour Moleweight at each stage(1*W@@W@MܹW@E_AW@וW@cbqmW@aq8}W@E 2uW@{nW@+@I0e@FD1y@K⬈@]ʾ@4`_@O@xW@h?@7@jin@K@{@xx"@*PA@l\N@IMf@s@2Vapour Viscosity profile>Vapour Viscosity at each stage(M>0BS>!>v4,>%<^>>eL>+yX>c>5y>!>hO8>H>kSw>b >h@>A֠q>bYx|>>C>w*u]>j,C>Ԛ>G>ِ>.刖>gEd:≯>j2'>aN0> o8>w{?>X8D>.vI>/4׫M>"o@S>~%f>>p >59+>&xx>/ډ|>:Vapour Heat capacity profileFVapour Heat capacity at each stage(S!uc@c]Fc@V}b=c@鷯b@>yX5b@> ףpb@ǘpb@?Tb@ׁsFJb@ o_b@1%b@n{b@ -|b@Nё\wb@ztb@Y8qb@V-ob@6nb@"ulb@hDiokb@a4kb@jb@KY8ib@-gb@O@a5b@}8g b@ ya@qha@Ca@ŏ1a@3a@Eiowa@ cla@{Pea@~8gDia@Bia@Oe b@?vb@ݓZb@D؎b@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stage(J+?so?ָu?]>i?ozݓ??Г?M5lƓ?&P?sՓ?d+?ך矔?M?/?!gH?鯙?M蘔?ᗗO?ڗ?)9?N"9?t?&?Bƕ?W?^?]( v?3:r(l?c?v0(v[?}/U?@`P?yD L?;I?OpL?ܿ f?T8۔?&? 1U8?_?fmZӖ?4Liquid Moleweight profile@Liquid Moleweight at each stage(@W@dW@&pW@]zkW@UHIW@x&sW@iW@J^c@bW@`ME^W@IFfW@DdW@swcW@-sbW@D;aW@$]3`W@8*5{`W@.V``W@ߡ(_W@St$_W@ek_W@t{I_W@$@M-_W@x _W@~^W@6vUW@žvMW@PGW@dF BW@V-=W@:W@4 7W@!Y4W@IV2W@ 2W@m24W@ܵ|@W@iQ\W@`-vW@]ʁW@ՐW@.Liquid Density profile:Liquid Density at each stage(qy@/$@@G@̇@-x@ZӼc@Ӽ@w-! @H.!X@Zd+@sג.@ 1@b42@e4@Dio5@Sc6@d;O 7@(\7@ 7@ǘ;8@ed8@?8@|a26@Nё\~/@fj?@%uM@&†X@vb@!rhj@K=p@ F%uv@9vz@ec@/]@ Ȋ@p= ת@ h"쟍@= ףp\@/ݤ@(2@2Liquid Viscosity profile>Liquid Viscosity at each stage(vѶ1??81?@|1?V1?q81?Q 1?M1?T1?<ƨ1?\6?.Ut"6?j x6?0<)5?zx5?&5?Mbz5?ˉ5?75?225?Q175?~:85?Q{05?2XO5?"{u5?R5? o15?u5?厎5? M{5?i&5?=Y5y5?w$t5?*|mt5?F\5? /8 6?.}8?#B;?c.=?=(=?92'i@R';i@W/'9i@a47i@hs5i@(\4i@Hz3i@h3i@b=y2i@ 2i@Eio1i@J{/L0i@MbX+i@ZӼi@K7Ah@JYh@'1h@jth@%~h@%䃲h@9#J{h@ h@hoh@w/h@0*oi@Zd;Oj@J{/Ll@=Ul@ l@:Liquid Thermal cond. profileFLiquid Thermal cond. at each stage({>?3?΅^Ժ?8(z?V=?9d?]?Z -???՟?)\F?/?|y?9:S?oU#?S]?+MK??C?O X??i?kn;#?Քd?66?PK?eqZK\?,V]j?0v?x?;͇?]-? ?ؾ?3.NV?*4?Rv?5?"9qa?0Surface tension profile<Surface tension at each stage(eO2?pEIv2?5?a?G=D;? !҈?[p?SRE֑?)J[ ?UJX?4*6?m ?) |鳔?4%?ar?^??t#nF?_F?4?%]? z6?ZXÇ ?"_wl?Kĝ?&Ô?EӔ?Zߔ?F7?k?Y|? ?\G?8 ?d t?ߧW?qtϙ8?ӡpɳ?kfO?Db'aK?PhG??3.<& not all ports are connectedFeed2{split}_stage25Feed1{split}_stage10 TopProduct BottomProduct @ @0@@$@,@@$@0@,@4@@@@@@@$@@@(@@(@ @(@ @ @ @ffffff,@ɿ#@@ ɿ#@@ɿ#@@ ɿ#@@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@#@3333334@ffffff,@/@ 3333334@ffffff,@/@3333334@ffffff,@/@ 3333334@ffffff,@/@ 334@ffffff,@/@ 334@ffffff,@/@ ffffff,@/@  ffffff,@/@? @@ @?(@@(@@@@RecoveryChemSep Unit OperationqeWCXcmCSUOQX[ChemSep] Version=6.31 Name=C:\DOCUME~1\Harry\LOCALS~1\Temp\CS355.sep Title=ChemSep CO Unit Operation "Recovery" in COFE Flowsheet User=Harry Date=2009-04-12 Time=11:02:12 [Cape-Open] unitname=Recovery CO_ID=CS355 3 components Phenol 108-95-2 94.1129989624 Mw Toluene 108-88-3 92.1405029297 Mw Methylcyclohexane 108-87-2 98.1882019043 Mw 0 thermo exe=C:\PROGRA~1\ChemSepL\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 [Paths] Device drivers path=c:\progra~1\chemsepl\bin\ Help and Info path=c:\progra~1\chemsepl\help\ Component data path=c:\progra~1\chemsepl\pcd\ Property data path=c:\progra~1\chemsepl\ipd\ Section data path=c:\progra~1\chemsepl\ild\ Executables path=C:\PROGRA~1\ChemSepL\bin\ Temporary path=WINTMPDIR Scripts path=c:\progra~1\chemsepl\bin\ [Units] Temperature=K Flow=mol/s Mass flow=kg/s Pressure=N/m2 Heat=J/s Enthalpy=J/kmol Entropy=J/kmol/K Fraction= Length=m 1/Length=1/m Area=m2 Volume=m3 Mass=kg Angle=rad Velocity=m/s Surface tension=N/m Density=kg/m3 Molar density=kmol/m3 Viscosity=N/m2.s Molecular weight=kg/kmol Heat capacity=J/kmol/K Thermal conductivity=J/s/m/K Diffusivity=m2/s Interaction parameter=J/mol Time=s [Components] 3 126 1181 Library Offset, Index DT=2009-03-26,23:59:44 CHK=780 CAS=108-95-2 CID=Phenol Name=Phenol Lib=c:\progra~1\chemsepl\pcd\chemsep1.pcd 140 502 Library Offset, Index DT=2009-03-26,23:59:44 CHK=60854 CAS=108-88-3 CID=Toluene Name=Toluene Lib=c:\progra~1\chemsepl\pcd\chemsep1.pcd 144 138 Library Offset, Index DT=2009-03-26,23:59:44 CHK=18409 CAS=108-87-2 CID=Methylcyclohexane Name=Methylcyclohexane Lib=c:\progra~1\chemsepl\pcd\chemsep1.pcd [Operation] 2 Operation Column 2 Operation kind Extractive Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 20 Stages 1 Feed stages 0 Sidestream stages F=12 S= 0 Pumparound stages P= [Properties] [Thermodynamics] 4 K model DECHEMA 8 Activity coefficient UNIFAC * Wilson model * * UNIQUAC model * 3 Equation of State Cubic 5 Cubic EOS Peng-Robinson * Virial EOS * 1 Vapour pressure Antoine [Enthalpy] 3 Enthalpy Excess 1 Enthalpy reference state Vapour 298.15 Enthalpy reference temperature 1 Formation enthalpies Excluded 298.15 Exergy surroundings temperature [Physical property models] 0 No Check T range * Cubic EOS * * Virial EOS * * Vapour model * * Liquid mixture density * * Liquid component density * * Vapour mixture viscosity * * Vapour mixture viscosity pressure correction * * Vapour component viscosity * * Liquid mixture viscosity * * Liquid component viscosity * Vapour mixture Cp * Vapour component Cp * Liquid mixture Cp * Liquid component Cp * Vapour mixture conductivity * * Vapour component conductivity * * Liquid mixture conductivity * * Liquid component conductivity * Mixture surface tension * * Component surface tension * * Vignes MS D-model * * D mixture model * * Vapour Diffusion Coefficients * [Reaction data] 0 Number of reactions [Specifications] Top Bottom [Heaters/Coolers] 0 Number 0 Column duty Qcolumn 2 First stage 19 Last stage [Efficiencies] 1 Default efficiency 0 Number [Pressures] 1 Column pressure Constant pressure 101325 Condenser pressure 101325 Top pressure * Pressure Drop * Bottom pressure [Feeds] 1 Number 1 Feed state T & p 12 Stage Feed1{split} 453.296968961 Temperature 101325 Pressure 0 Vapour fraction 3 componentflows 0.0499999126168 Component 1 flow 0.000616342956621 Component 2 flow 5.062131769e-006 Component 3 flow [Condenser] 7 Type Mole fraction of a component 0.001 Value Qcondenser 1 1st comp. * Type * * Initialization guess [Reboiler] 1 Type Boilup ratio 1 Value Qreboiler * Type * * Initialization guess [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 [Programs] Temporary file=SCRATCH.TMP User program= 8 DOS extender NT 1 Show windows Hidden [FlowSheet] [CoCo] [Settings] -1 -1 -1 0 Graph settings 1 Auto colors 1 Auto points 0.2 StringGrid5 2 8 Title Labels Stages Axis color Commands Box Labels box Import data StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 y1 x2 y2 StringGrid3 1 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage 0 Graph settings -1 -1 StringGrid7 16 2 StringGrid11 5 3 -1 -1 -1 0.95 0.95 1.2 1 0 Use old results 1 Automatic 0 Keep sep-files 1 Restore original StringGrid1 1 6 StringGrid2 4 1 StringGrid3 1 1 None -1 -1 -1 21 Binary Phase Diagram T p x -1 -1 StringGrid1 3 5 -1 -1 -1 0 21 Ternary Phase Diagram T 0 1 1 StringGrid1 3 5 0 0 -1 -1 -1 21 Binary Property Diagram 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 -1 -1 [End Settings] [End of Input] [Results] 1 Converged 0 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow 1 383.7474994 1.013250000E+05 6.219168920E-04 6.823199353E-02 2 384.1022355 1.013250000E+05 6.885391042E-02 6.705474796E-02 3 387.4721656 1.013250000E+05 6.767666485E-02 6.047340686E-02 4 406.1080553 1.013250000E+05 6.109532375E-02 5.040817128E-02 5 435.9568409 1.013250000E+05 5.103008818E-02 4.832086825E-02 6 449.9916293 1.013250000E+05 4.894278514E-02 4.891445647E-02 7 453.5569241 1.013250000E+05 4.953637336E-02 4.914925993E-02 8 454.3332321 1.013250000E+05 4.977117683E-02 4.920410368E-02 9 454.4970677 1.013250000E+05 4.982602057E-02 4.921584046E-02 10 454.5314234 1.013250000E+05 4.983775735E-02 4.921830869E-02 11 454.5386182 1.013250000E+05 4.984022558E-02 4.921882589E-02 12 454.5401246 1.013250000E+05 4.984074279E-02 9.993104702E-02 13 454.8077942 1.013250000E+05 4.993164622E-02 9.997044396E-02 14 454.9199331 1.013250000E+05 4.997104316E-02 9.998704609E-02 15 454.9667220 1.013250000E+05 4.998764529E-02 9.999398985E-02 16 454.9862121 1.013250000E+05 4.999458904E-02 9.999688511E-02 17 454.9943256 1.013250000E+05 4.999748431E-02 9.999809084E-02 18 454.9977024 1.013250000E+05 4.999869004E-02 9.999859272E-02 19 454.9991078 1.013250000E+05 4.999919192E-02 9.999880160E-02 20 454.9996926 1.013250000E+05 4.999940080E-02 4.999940080E-02 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.2226426E+08 -0.2226426E+08 0.3049553E+05 -0.5413966E+05 2 0.1042513E+08 -0.2238545E+08 0.3056495E+05 -0.5388833E+05 3 0.1087369E+08 -0.2342936E+08 0.3209587E+05 -0.5249172E+05 4 0.1342316E+08 -0.2661696E+08 0.4077054E+05 -0.5064097E+05 5 0.1754324E+08 -0.2664893E+08 0.5337671E+05 -0.4766732E+05 6 0.1939501E+08 -0.2563490E+08 0.5532071E+05 -0.4615637E+05 7 0.1984458E+08 -0.2531994E+08 0.5421176E+05 -0.4597534E+05 8 0.1994104E+08 -0.2524894E+08 0.5369610E+05 -0.4598214E+05 9 0.1996134E+08 -0.2523384E+08 0.5355848E+05 -0.4598893E+05 10 0.1996560E+08 -0.2523068E+08 0.5352773E+05 -0.4599072E+05 11 0.1996649E+08 -0.2523001E+08 0.5352120E+05 -0.4599111E+05 12 0.1996668E+08 -0.2522987E+08 0.5351983E+05 -0.4599119E+05 13 0.1999942E+08 -0.2520519E+08 0.5324287E+05 -0.4601233E+05 14 0.2001314E+08 -0.2519482E+08 0.5309819E+05 -0.4602692E+05 15 0.2001887E+08 -0.2519048E+08 0.5302600E+05 -0.4603542E+05 16 0.2002126E+08 -0.2518867E+08 0.5299102E+05 -0.4603998E+05 17 0.2002226E+08 -0.2518792E+08 0.5297441E+05 -0.4604230E+05 18 0.2002268E+08 -0.2518761E+08 0.5296664E+05 -0.4604344E+05 19 0.2002285E+08 -0.2518748E+08 0.5296304E+05 -0.4604400E+05 20 0.2002292E+08 -0.2518742E+08 0.5296137E+05 -0.4604426E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.9220411E+02 0.3028649E+01 0.8974769E-05 0.1353221E+06 0.1888037E-01 2 0.9219170E+02 0.3025177E+01 0.8984528E-05 0.1353236E+06 0.1890622E-01 3 0.9220022E+02 0.2996829E+01 0.9065525E-05 0.1362472E+06 0.1919612E-01 4 0.9237596E+02 0.2854200E+01 0.9523136E-05 0.1413725E+06 0.2072536E-01 5 0.9312057E+02 0.2669337E+01 0.1034390E-04 0.1473640E+06 0.2236794E-01 6 0.9379865E+02 0.2601952E+01 0.1079113E-04 0.1484374E+06 0.2239543E-01 7 0.9401825E+02 0.2587005E+01 0.1091300E-04 0.1484456E+06 0.2227947E-01 8 0.9406900E+02 0.2583873E+01 0.1094001E-04 0.1484312E+06 0.2224634E-01 9 0.9407985E+02 0.2583218E+01 0.1094573E-04 0.1484275E+06 0.2223897E-01 10 0.9408214E+02 0.2583081E+01 0.1094693E-04 0.1484267E+06 0.2223741E-01 11 0.9408262E+02 0.2583053E+01 0.1094718E-04 0.1484265E+06 0.2223709E-01 12 0.9408272E+02 0.2583047E+01 0.1094724E-04 0.1484265E+06 0.2223702E-01 13 0.9410026E+02 0.2581973E+01 0.1095664E-04 0.1484168E+06 0.2222451E-01 14 0.9410767E+02 0.2581525E+01 0.1096059E-04 0.1484128E+06 0.2221917E-01 15 0.9411078E+02 0.2581339E+01 0.1096223E-04 0.1484111E+06 0.2221692E-01 16 0.9411208E+02 0.2581261E+01 0.1096292E-04 0.1484105E+06 0.2221599E-01 17 0.9411262E+02 0.2581229E+01 0.1096320E-04 0.1484102E+06 0.2221560E-01 18 0.9411284E+02 0.2581216E+01 0.1096332E-04 0.1484101E+06 0.2221543E-01 19 0.9411294E+02 0.2581210E+01 0.1096337E-04 0.1484100E+06 0.2221537E-01 20 0.9411298E+02 0.2581208E+01 0.1096339E-04 0.1484100E+06 0.2221534E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.9219170E+02 0.7838971E+03 0.2497700E-03 0.1842869E+06 0.1119205E+00 0.1815768E-01 2 0.9220030E+02 0.7863950E+03 0.2524629E-03 0.1846838E+06 0.1122401E+00 0.1825998E-01 3 0.9237785E+02 0.8091937E+03 0.2791394E-03 0.1890286E+06 0.1149769E+00 0.1915845E-01 4 0.9313203E+02 0.9073422E+03 0.3882850E-03 0.2070993E+06 0.1263929E+00 0.2228372E-01 5 0.9381933E+02 0.1000772E+04 0.4448636E-03 0.2235921E+06 0.1380771E+00 0.2372999E-01 6 0.9404147E+02 0.1030430E+04 0.4428313E-03 0.2286764E+06 0.1425709E+00 0.2371602E-01 7 0.9409275E+02 0.1037206E+04 0.4406313E-03 0.2297974E+06 0.1436913E+00 0.2367561E-01 8 0.9410372E+02 0.1038652E+04 0.4400776E-03 0.2300336E+06 0.1439354E+00 0.2366529E-01 9 0.9410603E+02 0.1038956E+04 0.4399575E-03 0.2300831E+06 0.1439869E+00 0.2366305E-01 10 0.9410651E+02 0.1039020E+04 0.4399322E-03 0.2300935E+06 0.1439977E+00 0.2366257E-01 11 0.9410661E+02 0.1039033E+04 0.4399269E-03 0.2300956E+06 0.1439999E+00 0.2366247E-01 12 0.9410663E+02 0.1039036E+04 0.4399258E-03 0.2300961E+06 0.1440004E+00 0.2366245E-01 13 0.9411033E+02 0.1039533E+04 0.4397258E-03 0.2301762E+06 0.1440847E+00 0.2365874E-01 14 0.9411189E+02 0.1039740E+04 0.4396412E-03 0.2302097E+06 0.1441200E+00 0.2365717E-01 15 0.9411254E+02 0.1039827E+04 0.4396057E-03 0.2302237E+06 0.1441347E+00 0.2365651E-01 16 0.9411281E+02 0.1039863E+04 0.4395910E-03 0.2302295E+06 0.1441409E+00 0.2365623E-01 17 0.9411292E+02 0.1039878E+04 0.4395848E-03 0.2302319E+06 0.1441434E+00 0.2365612E-01 18 0.9411297E+02 0.1039884E+04 0.4395822E-03 0.2302329E+06 0.1441445E+00 0.2365607E-01 19 0.9411299E+02 0.1039887E+04 0.4395812E-03 0.2302334E+06 0.1441449E+00 0.2365605E-01 20 0.9411299E+02 0.1039888E+04 0.4395807E-03 0.2302335E+06 0.1441451E+00 0.2365604E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.885499177E-04 0.100000000E-02 0.110330159E-01 0.105655089E+00 0.490360376E+00 2 0.989422281E+00 0.990860935E+00 0.982690855E+00 0.889872078E+00 0.507517018E+00 3 0.104891689E-01 0.813906545E-02 0.627612864E-02 0.447283308E-02 0.212260656E-02 Component Mole fractions on stages: 6 to 10 1 0.838687015E+00 0.951265074E+00 0.977249405E+00 0.982802683E+00 0.983970282E+00 2 0.160677613E+00 0.485073465E-01 0.226064738E-01 0.170691907E-01 0.159046215E-01 3 0.635371689E-03 0.227579217E-03 0.144121363E-03 0.128125961E-03 0.125096144E-03 Component Mole fractions on stages: 11 to 15 1 0.984214940E+00 0.984266170E+00 0.993400353E+00 0.997246619E+00 0.998854882E+00 2 0.156605376E-01 0.156094166E-01 0.655337909E-02 0.273625762E-02 0.113879642E-02 3 0.124522277E-03 0.124413304E-03 0.462678636E-04 0.171235044E-04 0.632121041E-05 Component Mole fractions on stages: 16 to 20 1 0.999525418E+00 0.999804663E+00 0.999920903E+00 0.999969282E+00 0.999989417E+00 2 0.472253988E-03 0.194484352E-03 0.787887939E-04 0.306101098E-04 0.105490347E-04 3 0.232771732E-05 0.852958378E-06 0.308588769E-06 0.107686247E-06 0.335478801E-07 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.100000000E-02 0.111260697E-01 0.106731377E+00 0.496397918E+00 0.849468521E+00 2 0.990860935E+00 0.982615080E+00 0.888833494E+00 0.501553704E+00 0.149992685E+00 3 0.813906545E-02 0.625885034E-02 0.443512904E-02 0.204837777E-02 0.538794908E-03 Component Mole fractions on stages: 6 to 10 1 0.963347104E+00 0.989602510E+00 0.995212211E+00 0.996391605E+00 0.996638731E+00 2 0.365259067E-01 0.103545334E-01 0.476091787E-02 0.358456775E-02 0.333801744E-02 3 0.126989590E-03 0.429562429E-04 0.268714273E-04 0.238274701E-04 0.232514309E-04 Component Mole fractions on stages: 11 to 15 1 0.996690478E+00 0.996701312E+00 0.998622598E+00 0.999426407E+00 0.999761619E+00 2 0.328638001E-02 0.327556672E-02 0.136883911E-02 0.570429463E-03 0.237213752E-03 3 0.231421447E-04 0.231213437E-04 0.856241931E-05 0.316332885E-05 0.116689768E-05 Component Mole fractions on stages: 16 to 20 1 0.999901232E+00 0.999959350E+00 0.999983540E+00 0.999993608E+00 0.999997798E+00 2 0.983384009E-04 0.404921924E-04 0.164030928E-04 0.637258494E-05 0.219613522E-05 3 0.429565947E-06 0.157388182E-06 0.569378902E-07 0.198688126E-07 0.618974512E-08 [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 [Condenser Heat Duty] -2.250792071E+06 [Reboiler Heat Duty] 2.260495511E+06 [K-values] Component K-values on stages: 1 to 5 1 0.885499176E-01 0.898789979E-01 0.103371813E+00 0.212843538E+00 0.577255501E+00 2 0.998548077E+00 0.100839174E+01 0.110559611E+01 0.177423090E+01 0.338361180E+01 3 0.128874364E+01 0.130040902E+01 0.141509494E+01 0.218359774E+01 0.393954458E+01 Component K-values on stages: 6 to 10 1 0.870596914E+00 0.961259762E+00 0.981950777E+00 0.986361867E+00 0.987288826E+00 2 0.439900409E+01 0.468464823E+01 0.474834358E+01 0.476185470E+01 0.476469096E+01 3 0.500333681E+01 0.529793113E+01 0.536336835E+01 0.537723731E+01 0.538014817E+01 Component K-values on stages: 11 to 15 1 0.987483037E+00 0.987523704E+00 0.994770552E+00 0.997818962E+00 0.999093047E+00 2 0.476528506E+01 0.476540946E+01 0.478754520E+01 0.479683783E+01 0.480071839E+01 3 0.538075788E+01 0.538088554E+01 0.540359704E+01 0.541312813E+01 0.541710772E+01 Component K-values on stages: 16 to 20 1 0.999624149E+00 0.999845305E+00 0.999937361E+00 0.999975676E+00 0.999991619E+00 2 0.480233544E+01 0.480300869E+01 0.480328891E+01 0.480340554E+01 0.480345407E+01 3 0.541876593E+01 0.541945631E+01 0.541974365E+01 0.541986325E+01 0.541991301E+01 [Molecular weights] 1 94.113 2 92.141 3 98.188 [Feed stream 1] 12 Stage Number 5.0621317705190E-02 Flow rate 4.5329696896100E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.5343196480778E+07 Enthalpy [J/kmol] -4.5976445924539E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.8772443870369E-01 Mole fraction of component 1 1.2175561296339E-02 Mole fraction of component 2 9.9999999969993E-05 Mole fraction of component 3 5.0621317705190E-02 Flow rate 9.8772443870369E-01 Mole fraction of component 1 1.2175561296339E-02 Mole fraction of component 2 9.9999999969993E-05 Mole fraction of component 3 9.4089390236343E+01 Molar mass 1.0367153649100E+03 Density 4.4081548143958E-04 Viscosity 1.4360906062163E-01 Thermal conductivity 2.2972015134525E+05 Heat capacity 2.3678887340200E-02 Surface tension [Top product] 1 Stage Number 6.2191689200000E-04 Flow rate 3.8374749940000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.2264260812673E+07 Enthalpy [J/kmol] -5.4139656822790E+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 9.9086093500000E-01 Mole fraction of component 2 8.1390654500000E-03 Mole fraction of component 3 6.2191689200000E-04 Flow rate 1.0000000000000E-03 Mole fraction of component 1 9.9086093500000E-01 Mole fraction of component 2 8.1390654500000E-03 Mole fraction of component 3 9.2191698084960E+01 Molar mass 7.8389712952042E+02 Density 2.4976998350774E-04 Viscosity 1.1192049507519E-01 Thermal conductivity 1.8428693931695E+05 Heat capacity 1.8157684120287E-02 Surface tension [Bottom product] 20 Stage Number 4.9999400800000E-02 Flow rate 4.5499969260000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.5187422641197E+07 Enthalpy [J/kmol] -4.6044259616058E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9999779800000E-01 Mole fraction of component 1 2.1961352200000E-06 Mole fraction of component 2 6.1897451200000E-09 Mole fraction of component 3 4.9999400800000E-02 Flow rate 9.9999779800000E-01 Mole fraction of component 1 2.1961352200000E-06 Mole fraction of component 2 6.1897451200000E-09 Mole fraction of component 3 9.4112994686342E+01 Molar mass 1.0398875947492E+03 Density 4.3958073093602E-04 Viscosity 1.4414510335895E-01 Thermal conductivity 2.3023354143955E+05 Heat capacity 2.3656041397271E-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 stageyLw@x@$7x@1ay@Og8O?{@T|@>)X|@.Te|@^Bg|@Dҵh|@| .h|@>LYh|@`nl|@ 0 n|@.|wo|@Vo|@6o|@@ʖo|@uXo|@o|@"Pressure profile.Pressure at each stageм@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@(Vapour Flow profile4Vapour Flow at each stage @?Ew6Q@FzNP@d3N@OكI@6.xH@H@8$ H@ H@;H@kH@벱uH@+.@H@-k$KH@L.)kH@IᓱNH@ܐH@ RBH@iUH@R̋]H@(Liquid Flow profile4Liquid Flow at each stagedQ@AnP@w4I@ 5)H@! uH@ H@K H@CmH@H@|H@ |=FX@?X@v ]+X@X@qT4X@.gX@pX@R̋]X@R̋]H@4Vapour Moleweight profile@Vapour Moleweight at each stageWc# W@*D W@Tg W@&W@=;kGW@ӼsW@I +W@#~jW@z,CW@al!AW@eIW@hHKW@5FjW@0W@BCW@IQ,W@ 8*5W@kC8W@Ah:W@Fw;W@.Vapour Density profile:Vapour Density at each stage=S:@!3@{@Af@h[Z@&5@5l/@#ū@2n@Z_&@q@O?@u=u@sF@`@*l@c[@KT@ݰmQ@xcAaP@2Vapour Viscosity profile>Vapour Viscosity at each stageEJ>1 >D>Cyر>sV>+-q> L>~_>q>Y>q8>x5A>!w"M>l>L>kM>u@>>|5:>#sm>Ro>:Vapour Heat capacity profileFVapour Heat capacity at each stageUN`@cZ`@Hra@Ra@Skb@H.b@ cZBb@!Ac̍b@Hzb@&†b@S㥍b@S㥍b@!lVb@>yX5b@W/'b@B`"b@7[ b@ b@Qb@Qb@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stageFھ.`U?(*]&\?ջp%?_]9?g ?,? mЖ?Wǖ? cŖ?<}RgŖ? ;QŖ?Y&MŖ?~z–?m A?zEC?8ɿ?ح?,DE?mby>?8;?4Liquid Moleweight profile@Liquid Moleweight at each stage*D W@X W@2ı.W@-sHW@motW@pqW@-W@;5YW@F 2ɆW@QцW@Mۿ҆W@pӆW@"qW@4)W@z3W@Z*oG8W@:W@wۅ:W@h:;W@h:;W@.Liquid Density profile:Liquid Density at each stageB-@\(@镲I@ZӼZ@V-F@Q@4@S㥛:@;@Gz<@!<@/$<@!>@)\>@+N?@ˡEs?@n?@K7?@5^I?@d;O?@2Liquid Viscosity profile>Liquid Viscosity at each stageCEq^0?!柋0?.K2?d`Wr9?(k'=??~y=?p|nd??yd?zKޥyl?ǵF)n?Bn?eJn?2Nn?N-^q?߉Y/r?\s? 5s?cwzJs?Ss?MWs?w0Xs?0Surface tension profile<Surface tension at each stage-G헒?-Գ?E?k"і?fL?E*)I?L¦Jk>?f;?[~g ;?A(1;?c+{:?@#:?B*9?͕9?e&i9?_ɸV9?AWO9?K9?uiJ9?cI9?4>L6 not all ports are connectedFeed1{split}_stage12 TopProduct BottomProduct @ @0@@$@,@@$@0@,@4@@@@@@@$@@@(@@(@ @(@ @ @ @ffffff,@ɿ#@@ ɿ#@@ɿ#@@ ɿ#@@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@#@3333334@ffffff,@/@ 3333334@ffffff,@/@3333334@ffffff,@/@ 3333334@ffffff,@/@ 334@ffffff,@/@ 334@ffffff,@/@ ffffff,@/@  ffffff,@/@? @@ @?(@@(@@=@CoolerMHeaterCooler - heat or cool stream specifying heat duty or outlet temperaturez,wKJEKBpCOUSCOUS0001TypeOperation type Temperature Heat duty Heat duty Temperature Energy inletOutlet temperatureOutlet temperature?Pw@r@ _B Heat duty Heat duty@?@^Yy)@x@xD Pressure drop Pressure drop? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.01.01.01.159 = $not all material ports are connectedInletOutlet HmUd n?TTHmUd n?TTHmUd n?TTHmUd n?TT@@ ɿ@????@@@@@ɿ@@@MixerMakeUpMixer - mixer for de/!TLCc0COUSCOUS0001Thermo Version*Thermodynamics CAPE-OPEN Interface version1.01.01.01.1 Outlet flowTarget flow at recycle outlet?I@ _B Nett flowResulting nett make up flow?7OQC? _B Flow basisBasis for target and nett flowmol/smol/smol/skg/sTarget compound&Compound for outlet flow specification Total flow Total flow Total flowPhenolTolueneMethylcyclohexane6$ $not all material ports are connectedMake up excess flow Recycle inletRecycle outletMake up surplus flow 0?@@?@@@ @ @MS Sans -C6?-C6?h㈵>-C6?vG m