FSD100MbP?h㈵>dk 7*dfffffr@м@Harry Kooijmanwww.ChemSep.org"Extractive azeotropic distillationdDx temperaturepressure compositionflowMCH-Tol Extractionڐ@'t+5010MCH-Tol Extraction:0yE>MbP?MbP?MbP?%c:\werk\CO\COCO\bin\data\ChemSep1.pcd{Phenol(C6H5)OHC6H6O108-95-2 c1ccccc1(O)0@TbWA@O??p|@s@s@Tg@`;W@~?`I?@w= @୊9?[@@3gs@@eTnA9]?Mb?@<2?s@@j@͈@6`?r D@̠s@d`+@@᠃Qx/@ɂ )>̠s@z@i@h} A)@?ЯjY@p@`?`f@W @`f2t@@@hŋ@`fa@)m&@@37r@@3[@e`|> #g?zI@@@d 8 8 8 8 8 8 8@ w5@5@xV 8 8z@`@ @ i 8 8@37r@@3[@ i @p@@z?`I?`&@Ķ? 8 8 ?D?|:??@z?zDX@~?N @@eq@('`G-(??H?|Toluene (C6H5)CH3C7H8108-88-3 c1ccccc1(C)~@pWOA X9?@`?w@Ef@Ef@U?  W@ [?@`?=@V9@x?ADA"AxAxPYA 8@ #@`:? 8 8 8IW@Ef@U??~@.4? 8@3cd@`fn@i X@n&@i>@Ef@@3@eA@?෯?S@+0?Ef@ρ@j2Û@v^0 ?D@Ef@d@`H@%@@`?g|>@3Cf@@@ @̮E)@@)7>tUb@p@S:?dk`F@=o@@h@c @t6@.}@Ef@zw@e Z>_?=s@`f@ 8Ef@@@f +'7uqZ[`>Ef@}@`Xo> a?@ g@`@ 8zw@@@f43@mV 7|ϾEf@ρ@OV܂@ٿ \? 8i@p@ 8 8 8 8 8 8 8 /4@`f@N 8 85v@t@ N@]"? 8 8Ef@zw@ x#4@@33333ξ =DQOI?Zb#>@a@v@v@ ?w@>W? 8 8f?@?4?f?E?`[@ [?"@-s@K\y?4?Z?Methylcyclohexane (C6H11)CH3C7H14108-87-2 C1CCCCC1(C) @L{JAO?&?paw@`Rb@`Rb@ #?@X@m?z?`=^@ ?EoAt]zAAYA 8ٷ&@@(} 8 8 8PM@`Rb@? ? @&? 8`Rb@@iPZ@`f )`{>@`Rb@@e@.A?`t?@zŧ?`Rb@@j@3@ W"v?|(@`Rb@d@@ d @`p"?`Rb@t@`=@$ d+@ X*<0}>i@p@Q?n@}@q@@hn&@3@@?Aa@`Rb@@|@er>@?=fs@@37@ 8`Rb@@@fP?z4o ?@D{`a>`fq@Gaw@?l?@3)@X@ 8Gaw@@@fW}B@| F,H?ܾ`Rb@@@)c@?Yr>I@@@d 8 8 8 8 8 8 8`4@@3!@LE 8 8=u@@@ @ũ ? 8 8`Rb@@|@ K7Ac@YU7i?">7G< @G@?5@?5@"?@!H@`"l? 8 8KY?`Ӽ?@Ď?ื?@Gr?za@m?@[@ Cft@ F?rm?activityactivityDactivityCoefficientactivityCoefficientDbubblePointPressurebubblePointPressurebubblePointTemperaturebubblePointTemperaturecompressibilityFactorcompressibilityFactordensitydensitydensity/volume (pure)density/volume (pure)dewPointPressuredewPointPressuredewPointTemperaturedewPointTemperature enthalpyenthalpyentropyentropy excessEnthalpyexcessEnthalpyfugacityfugacityfugacityCoefficientfugacityCoefficientgibbsFreeEnergy gibbsEnergyGG heatCapacityheatCapacityCpKK 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@&?_NS%?INs?Br?w{hv? 1?`>f?\S?['=KCt?Ks?3?5(BQ??on>&?_NS%?INs?Br?w{hv? 1?м@ @2Bottoms9&D'>'9&D'9&9'D'   defaultм@FlMz@ppiM@n@n2Y?O?=*A?5?-C6?dq?! DN??)6P??R#+?\ _5Q?&r8R??n2Y?O?=*A?5?-C6?dq?м@O@2TolueneP"Z"U"P"Z"P"Z"  defaultм@Ǭ1w@T #@21c?tMbP?H`!ջP?eb?h a?UƸC?0E?!3?4?5.?b.?kP?9"[zQ??tMbP?J`!ջP?eb?h a?UƸC?0E?2Recycle SolventP3 8;8 3P8P3P8 8  defaultм@޺^o|@ ɼI@H Ì@w`^?R g?J*?Hz)?7W0="2=B?I3? :^?ܘ]?&jct >tю >?w`^?R g?J*?Hz)?7W0="2=2Phenol  &defaultм@Pw@Zd;O?r9~Q????????Pw@м@Zd;O?r9~Q?2 Cold Solvent8.888 defaultм@Pw@ ɼI@H Ì@w`^?R g?J*?Hz)?7W0="2=?w`^?R g?J*?Hz)?7W0="2=??r@?zGI@Á@2Extractive DistillationChemSep Unit OperationqeWCXc9CSUO#[ChemSep] Version=6.82 Compiled=2011-5-25 00:06 Name=C:\Users\jasper\AppData\Local\Temp\CS_3_4~2.sep Title=ChemSep CO Unit Operation "Extractive Distillation" in COFE Flowsheet User=jasper Date=2011-05-25 Time=09:33:32 [Cape-Open] unitname=Extractive Distillation CO_ID=CS_3_4B4_1CC1AAE_C53EC40 3 components Phenol 108-95-2 94.1129989624 Mw Toluene 108-88-3 92.1409988403 Mw Methylcyclohexane 108-87-2 98.18800354 Mw 0 thermo exe=C:\Program Files (x86)\ChemSepL6v70\bin\co-col2.exe mode=COFE NoWarnings=TRUE WilsonEstimate=TRUE Status= 0 only K-values and ethalpies 0 use only perturbed derivative 0 use only perturbed mole derivative 0.001 relative T perturbation 0.001 relative P perturbation 0.001 X perturbation 0 write all values to log 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 (x86)\chemsepl6v70\bin\ Help and Info path=c:\program files (x86)\chemsepl6v70\help\ Component data path=c:\program files (x86)\chemsepl6v70\pcd\ Property data path=c:\program files (x86)\chemsepl6v70\ipd\ Section data path=c:\program files (x86)\chemsepl6v70\ild\ Executables path=C:\Program Files (x86)\ChemSepL6v70\bin\ Temporary path=WINTMPDIR Scripts path=c:\program files (x86)\chemsepl6v70\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=2010-09-20,09:33:26 CHK=11034 CAS=108-95-2 CID=Phenol Name=Phenol Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 140 502 Library Offset, Index DT=2010-09-20,09:33:26 CHK=62500 CAS=108-88-3 CID=Toluene Name=Toluene Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 144 138 Library Offset, Index DT=2010-09-20,09:33:26 CHK=31662 CAS=108-87-2 CID=Methylcyclohexane Name=Methylcyclohexane Lib=c:\program files (x86)\chemsepl6v70\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] 350 BIP estimation temperature [Thermodynamics] 4 K model DECHEMA 8 * Activity coefficient UNIFAC * Wilson model * * UNIQUAC model * 3 Equation of State Cubic 5 Cubic EOS Peng-Robinson 76 * Virial EOS * 1 Vapour pressure Antoine 0 Henry's law * Henry's default * [Enthalpy] 3 Enthalpy Excess 1 Enthalpy reference state Vapour 298.15 Enthalpy reference temperature 1 Formation enthalpies Excluded 298.15 Exergy surroundings temperature [Physical property models] 0 No Check T range * Cubic EOS * * Virial EOS * * Vapour model * * Liquid mixture density * * Liquid component density * * Vapour mixture viscosity * * Vapour mixture viscosity pressure correction * * Vapour component viscosity * * Liquid mixture viscosity * * Liquid component viscosity * Vapour mixture Cp * Vapour component Cp * Liquid mixture Cp * Liquid component Cp * Vapour mixture conductivity * * Vapour component conductivity * * Liquid mixture conductivity * * Liquid component conductivity * Mixture surface tension * * Component surface tension * * Vignes MS D-model * * D mixture model * * Vapour Diffusion Coefficients * [Reaction data] 0 Number of reactions [Specifications] Top Bottom [Heaters/Coolers] 0 Number 0 Column duty Qcolumn 2 First stage 39 Last stage 0 Qcolumn lost to surroundings [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 0.0500221303285 Component 1 flow 9.96101157274e-006 Component 2 flow 1.56395868378e-012 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] 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 1 StringGrid=StringGrid7 16 2 Title McCabe-Thiele diagram Methylcyclohexane - Toluene Xlabel X Methylcyclohexane/(Methylcyclohexane+Toluene) Ylabel Y Methylcyclohexane/(Methylcyclohexane+Toluene) X interval 0.2 Y interval 0.2 X min 0 X max 1 Y min 0 Y max 1 X tics 0 Y tics 0 Axis color Black Grid Off y Fractions Vertical Commands set label "ChemSep" at 1,0.02 right Stage numbers On StringGrid=StringGrid11 5 3 CheckBox=CheckBox45 0 Lumped ComboBox=ComboBox75 -1 ComboBox=ComboBox76 -1 ComboBox=ComboBox77 -1 Edit=Edit55 0.95 Edit=Edit56 0.95 Edit=Edit57 1.2 Edit=Edit1 1 CheckBox=CheckBox2 0 Use old results CheckBox=CheckBox3 1 Automatic CheckBox=CheckBox1 0 Keep sep-files CheckBox=CheckBox4 1 Restore original StringGrid=StringGrid1 1 6 Name Variable Units Value Start/Valuelist End StringGrid=StringGrid2 4 1 Name Variable Units Current Value StringGrid=StringGrid3 1 1 None ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Title ComboBox=ComboBox4 0 ComboBox=ComboBox15 0 Edit=Edit17 Plot font CheckBox=CheckBox2 1 Color=Edit18 1635136 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 1635136 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 1635136 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 1635136 SpinEdit=SpinEdit3 1 ComboBox=ComboBox14 0 RadioButton=RadioButton3 TRUE DrawSetColors=BVLEcolors 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 ComboBox=ComboBox7 -1 ComboBox=ComboBox11 -1 ComboBox=ComboBox6 -1 Memo=Memo1 Memo1, ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox4 0 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Ternary Phase Diagram Edit=Edit4 10, 25 Edit=Edit6 Edit=Edit7 chemsep1.pcd Edit=Edit8 Edit=Edit5 StringGrid=StringGrid1 4 7 Identifier L# File Loc. CAS SMILES Name Phenol 1181 c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 126 108-95-2 c1ccccc1(O) Phenol Toluene 502 c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 140 108-88-3 c1ccccc1(C) Toluene Methylcyclohexane 138 c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 144 108-87-2 C1CCCCC1(C) Methylcyclohexane 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 1 374.0902135 1.013250000E+05 1.004465451E-02 8.035723606E-02 -2.775077226E+06 2 374.0937530 1.013250000E+05 9.040189057E-02 8.035079916E-02 0.000000000E+00 3 374.1002991 1.013250000E+05 9.039545367E-02 8.033840915E-02 0.000000000E+00 4 374.1125432 1.013250000E+05 9.038306366E-02 8.031461093E-02 0.000000000E+00 5 374.1358324 1.013250000E+05 9.035926544E-02 8.026808875E-02 0.000000000E+00 6 374.1814638 1.013250000E+05 9.031274326E-02 8.017301999E-02 0.000000000E+00 7 374.2761025 1.013250000E+05 9.021767450E-02 7.995932877E-02 0.000000000E+00 8 374.4966889 1.013250000E+05 9.000398328E-02 7.936157371E-02 0.000000000E+00 9 375.1712966 1.013250000E+05 8.940622822E-02 7.613200525E-02 0.000000000E+00 10 379.9351003 1.013250000E+05 8.617665976E-02 1.338772108E-01 0.000000000E+00 11 379.9437754 1.013250000E+05 9.388960316E-02 1.338616575E-01 0.000000000E+00 12 379.9552880 1.013250000E+05 9.387404984E-02 1.338412415E-01 0.000000000E+00 13 379.9706425 1.013250000E+05 9.385363383E-02 1.338143928E-01 0.000000000E+00 14 379.9912500 1.013250000E+05 9.382678515E-02 1.337790018E-01 0.000000000E+00 15 380.0191257 1.013250000E+05 9.379139408E-02 1.337322133E-01 0.000000000E+00 16 380.0572009 1.013250000E+05 9.374460560E-02 1.336701342E-01 0.000000000E+00 17 380.1098240 1.013250000E+05 9.368252649E-02 1.335874164E-01 0.000000000E+00 18 380.1835738 1.013250000E+05 9.359980869E-02 1.334766784E-01 0.000000000E+00 19 380.2885862 1.013250000E+05 9.348907071E-02 1.333277638E-01 0.000000000E+00 20 380.4406750 1.013250000E+05 9.334015613E-02 1.331270489E-01 0.000000000E+00 21 380.6644649 1.013250000E+05 9.313944119E-02 1.328581549E-01 0.000000000E+00 22 380.9964315 1.013250000E+05 9.287054719E-02 1.325134347E-01 0.000000000E+00 23 381.4748444 1.013250000E+05 9.252582702E-02 1.321939945E-01 0.000000000E+00 24 381.9958171 1.013250000E+05 9.220638677E-02 1.323186275E-01 0.000000000E+00 25 382.3112544 1.013250000E+05 7.233101985E-02 1.321303022E-01 0.000000000E+00 26 382.8111020 1.013250000E+05 7.214269456E-02 1.318680585E-01 0.000000000E+00 27 383.5869055 1.013250000E+05 7.188045079E-02 1.315437288E-01 0.000000000E+00 28 384.7312747 1.013250000E+05 7.155612108E-02 1.312254183E-01 0.000000000E+00 29 386.2656044 1.013250000E+05 7.123781064E-02 1.310376158E-01 0.000000000E+00 30 388.0491187 1.013250000E+05 7.105000815E-02 1.310764914E-01 0.000000000E+00 31 389.7945288 1.013250000E+05 7.108888367E-02 1.313119590E-01 0.000000000E+00 32 391.2357530 1.013250000E+05 7.132435136E-02 1.316192500E-01 0.000000000E+00 33 392.2692820 1.013250000E+05 7.163164229E-02 1.318910189E-01 0.000000000E+00 34 392.9388289 1.013250000E+05 7.190341120E-02 1.320864133E-01 0.000000000E+00 35 393.3461684 1.013250000E+05 7.209880560E-02 1.322067503E-01 0.000000000E+00 36 393.5953565 1.013250000E+05 7.221914258E-02 1.322413966E-01 0.000000000E+00 37 393.8264773 1.013250000E+05 7.225378889E-02 1.319883436E-01 0.000000000E+00 38 394.6073400 1.013250000E+05 7.200073592E-02 1.300135790E-01 0.000000000E+00 39 399.4908229 1.013250000E+05 7.002597135E-02 1.217033257E-01 0.000000000E+00 40 420.8721736 1.013250000E+05 6.171571798E-02 5.998760768E-02 2.690140545E+06 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.1900229E+08 -0.1900229E+08 -0.4700628E+05 -0.4700628E+05 2 0.1169482E+08 -0.1900386E+08 0.3451906E+05 -0.4699996E+05 3 0.1169562E+08 -0.1900709E+08 0.3452958E+05 -0.4698798E+05 4 0.1169695E+08 -0.1901347E+08 0.3454984E+05 -0.4696710E+05 5 0.1169937E+08 -0.1902597E+08 0.3458701E+05 -0.4693235E+05 6 0.1170408E+08 -0.1905117E+08 0.3465448E+05 -0.4687639E+05 7 0.1171407E+08 -0.1910558E+08 0.3477939E+05 -0.4679013E+05 8 0.1173878E+08 -0.1924279E+08 0.3502653E+05 -0.4667545E+05 9 0.1182320E+08 -0.1975162E+08 0.3561530E+05 -0.4672602E+05 10 0.1253791E+08 -0.2627240E+08 0.3841527E+05 -0.5492470E+05 11 0.1253478E+08 -0.2627975E+08 0.3848104E+05 -0.5487537E+05 12 0.1253072E+08 -0.2628936E+08 0.3856055E+05 -0.5481681E+05 13 0.1252545E+08 -0.2630192E+08 0.3865652E+05 -0.5474762E+05 14 0.1251865E+08 -0.2631834E+08 0.3877198E+05 -0.5466644E+05 15 0.1250988E+08 -0.2633981E+08 0.3891033E+05 -0.5457207E+05 16 0.1249864E+08 -0.2636789E+08 0.3907520E+05 -0.5446380E+05 17 0.1248430E+08 -0.2640464E+08 0.3927032E+05 -0.5434177E+05 18 0.1246619E+08 -0.2645269E+08 0.3949927E+05 -0.5420766E+05 19 0.1244362E+08 -0.2651541E+08 0.3976494E+05 -0.5406566E+05 20 0.1241609E+08 -0.2659688E+08 0.4006870E+05 -0.5392397E+05 21 0.1238354E+08 -0.2670148E+08 0.4040896E+05 -0.5379630E+05 22 0.1234676E+08 -0.2683149E+08 0.4077815E+05 -0.5370132E+05 23 0.1230605E+08 -0.2697173E+08 0.4115217E+05 -0.5364182E+05 24 0.1224059E+08 -0.2696838E+08 0.4141758E+05 -0.5341611E+05 25 0.1222841E+08 -0.2703233E+08 0.4152888E+05 -0.5345970E+05 26 0.1221361E+08 -0.2711897E+08 0.4166204E+05 -0.5354141E+05 27 0.1219786E+08 -0.2722386E+08 0.4178615E+05 -0.5368186E+05 28 0.1218324E+08 -0.2732720E+08 0.4182394E+05 -0.5389295E+05 29 0.1216897E+08 -0.2739443E+08 0.4164189E+05 -0.5416068E+05 30 0.1214936E+08 -0.2739866E+08 0.4110255E+05 -0.5444812E+05 31 0.1211994E+08 -0.2734695E+08 0.4019023E+05 -0.5472299E+05 32 0.1208468E+08 -0.2727260E+08 0.3907248E+05 -0.5497033E+05 33 0.1205213E+08 -0.2720499E+08 0.3798704E+05 -0.5518223E+05 34 0.1202751E+08 -0.2715576E+08 0.3709300E+05 -0.5535294E+05 35 0.1201139E+08 -0.2712462E+08 0.3643462E+05 -0.5548214E+05 36 0.1200312E+08 -0.2711048E+08 0.3598876E+05 -0.5557738E+05 37 0.1201024E+08 -0.2713577E+08 0.3573862E+05 -0.5566504E+05 38 0.1210138E+08 -0.2738242E+08 0.3588310E+05 -0.5587834E+05 39 0.1274993E+08 -0.2866188E+08 0.3801933E+05 -0.5670031E+05 40 0.1563082E+08 -0.2938561E+08 0.4744652E+05 -0.5495088E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.9815776E+02 0.3324384E+01 0.8213343E-05 0.1720375E+06 0.2018347E-01 2 0.9815784E+02 0.3324354E+01 0.8213455E-05 0.1720382E+06 0.2018361E-01 3 0.9815757E+02 0.3324282E+01 0.8213698E-05 0.1720365E+06 0.2018371E-01 4 0.9815667E+02 0.3324134E+01 0.8214187E-05 0.1720307E+06 0.2018375E-01 5 0.9815463E+02 0.3323841E+01 0.8215139E-05 0.1720178E+06 0.2018373E-01 6 0.9815045E+02 0.3323260E+01 0.8217008E-05 0.1719916E+06 0.2018370E-01 7 0.9814194E+02 0.3322060E+01 0.8220812E-05 0.1719406E+06 0.2018403E-01 8 0.9812396E+02 0.3319323E+01 0.8229264E-05 0.1718436E+06 0.2018690E-01 9 0.9808133E+02 0.3311363E+01 0.8252564E-05 0.1716846E+06 0.2020858E-01 10 0.9794485E+02 0.3261188E+01 0.8383592E-05 0.1723638E+06 0.2053069E-01 11 0.9793388E+02 0.3260725E+01 0.8384719E-05 0.1722936E+06 0.2052752E-01 12 0.9791954E+02 0.3260119E+01 0.8386196E-05 0.1722019E+06 0.2052339E-01 13 0.9790079E+02 0.3259323E+01 0.8388134E-05 0.1720821E+06 0.2051803E-01 14 0.9787627E+02 0.3258278E+01 0.8390683E-05 0.1719257E+06 0.2051105E-01 15 0.9784417E+02 0.3256902E+01 0.8394041E-05 0.1717211E+06 0.2050200E-01 16 0.9780210E+02 0.3255084E+01 0.8398481E-05 0.1714537E+06 0.2049028E-01 17 0.9774693E+02 0.3252676E+01 0.8404370E-05 0.1711039E+06 0.2047513E-01 18 0.9767450E+02 0.3249471E+01 0.8412219E-05 0.1706464E+06 0.2045565E-01 19 0.9757932E+02 0.3245187E+01 0.8422734E-05 0.1700480E+06 0.2043075E-01 20 0.9745425E+02 0.3239430E+01 0.8436904E-05 0.1692665E+06 0.2039924E-01 21 0.9729014E+02 0.3231660E+01 0.8456105E-05 0.1682493E+06 0.2035998E-01 22 0.9707589E+02 0.3221164E+01 0.8482178E-05 0.1669341E+06 0.2031212E-01 23 0.9679958E+02 0.3207199E+01 0.8517102E-05 0.1652527E+06 0.2025463E-01 24 0.9645361E+02 0.3190488E+01 0.8559126E-05 0.1631140E+06 0.2017602E-01 25 0.9631056E+02 0.3182685E+01 0.8578959E-05 0.1622623E+06 0.2015188E-01 26 0.9609693E+02 0.3170799E+01 0.8609342E-05 0.1609969E+06 0.2011812E-01 27 0.9578795E+02 0.3153202E+01 0.8654722E-05 0.1591765E+06 0.2007345E-01 28 0.9536413E+02 0.3128494E+01 0.8719251E-05 0.1566885E+06 0.2001814E-01 29 0.9482933E+02 0.3096784E+01 0.8803492E-05 0.1535451E+06 0.1995436E-01 30 0.9423044E+02 0.3061078E+01 0.8900325E-05 0.1499974E+06 0.1988597E-01 31 0.9365205E+02 0.3026779E+01 0.8995376E-05 0.1465269E+06 0.1981915E-01 32 0.9317333E+02 0.2998701E+01 0.9074715E-05 0.1436148E+06 0.1976148E-01 33 0.9282726E+02 0.2978628E+01 0.9132299E-05 0.1414853E+06 0.1971791E-01 34 0.9260137E+02 0.2965636E+01 0.9169959E-05 0.1400839E+06 0.1968851E-01 35 0.9246371E+02 0.2957751E+01 0.9192971E-05 0.1392258E+06 0.1967032E-01 36 0.9238345E+02 0.2953068E+01 0.9206711E-05 0.1387268E+06 0.1966053E-01 37 0.9233876E+02 0.2949715E+01 0.9216710E-05 0.1384690E+06 0.1966205E-01 38 0.9232118E+02 0.2942825E+01 0.9238137E-05 0.1385193E+06 0.1971481E-01 39 0.9236603E+02 0.2905479E+01 0.9358597E-05 0.1398596E+06 0.2009416E-01 40 0.9274225E+02 0.2759376E+01 0.9905444E-05 0.1454229E+06 0.2156308E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.9815784E+02 0.7249924E+03 0.2985904E-03 0.2307542E+06 0.9352586E-01 0.1505409E-01 2 0.9815753E+02 0.7250365E+03 0.2986532E-03 0.2307512E+06 0.9353373E-01 0.1505661E-01 3 0.9815652E+02 0.7251231E+03 0.2987672E-03 0.2307427E+06 0.9354990E-01 0.1506160E-01 4 0.9815423E+02 0.7252896E+03 0.2989786E-03 0.2307244E+06 0.9358156E-01 0.1507124E-01 5 0.9814952E+02 0.7256106E+03 0.2993795E-03 0.2306880E+06 0.9364311E-01 0.1508985E-01 6 0.9813995E+02 0.7262449E+03 0.3001657E-03 0.2306179E+06 0.9376510E-01 0.1512663E-01 7 0.9811970E+02 0.7275720E+03 0.3018059E-03 0.2304827E+06 0.9402029E-01 0.1520344E-01 8 0.9807165E+02 0.7307239E+03 0.3057055E-03 0.2302158E+06 0.9462445E-01 0.1538514E-01 9 0.9791675E+02 0.7410595E+03 0.3186000E-03 0.2296020E+06 0.9658238E-01 0.1597391E-01 10 0.9648900E+02 0.8503045E+03 0.4643517E-03 0.2205033E+06 0.1152282E+00 0.2156007E-01 11 0.9647877E+02 0.8504471E+03 0.4641901E-03 0.2204347E+06 0.1152619E+00 0.2156622E-01 12 0.9646541E+02 0.8506337E+03 0.4639784E-03 0.2203451E+06 0.1153058E+00 0.2157427E-01 13 0.9644793E+02 0.8508782E+03 0.4637007E-03 0.2202281E+06 0.1153634E+00 0.2158478E-01 14 0.9642504E+02 0.8511990E+03 0.4633361E-03 0.2200751E+06 0.1154387E+00 0.2159853E-01 15 0.9639506E+02 0.8516204E+03 0.4628563E-03 0.2198751E+06 0.1155374E+00 0.2161652E-01 16 0.9635574E+02 0.8521752E+03 0.4622236E-03 0.2196136E+06 0.1156670E+00 0.2164007E-01 17 0.9630413E+02 0.8529069E+03 0.4613867E-03 0.2192715E+06 0.1158373E+00 0.2167090E-01 18 0.9623633E+02 0.8538742E+03 0.4602761E-03 0.2188242E+06 0.1160612E+00 0.2171128E-01 19 0.9614727E+02 0.8551555E+03 0.4587970E-03 0.2182404E+06 0.1163557E+00 0.2176406E-01 20 0.9603048E+02 0.8568535E+03 0.4568194E-03 0.2174812E+06 0.1167425E+00 0.2183279E-01 21 0.9587816E+02 0.8590957E+03 0.4541641E-03 0.2165021E+06 0.1172476E+00 0.2192136E-01 22 0.9568212E+02 0.8620021E+03 0.4505632E-03 0.2152617E+06 0.1178947E+00 0.2203221E-01 23 0.9543810E+02 0.8654162E+03 0.4453752E-03 0.2137562E+06 0.1186636E+00 0.2215439E-01 24 0.9516601E+02 0.8666315E+03 0.4349853E-03 0.2121848E+06 0.1191646E+00 0.2216900E-01 25 0.9504774E+02 0.8683920E+03 0.4323268E-03 0.2114862E+06 0.1195432E+00 0.2222619E-01 26 0.9487723E+02 0.8709393E+03 0.4282999E-03 0.2104968E+06 0.1200852E+00 0.2230504E-01 27 0.9464444E+02 0.8744059E+03 0.4223541E-03 0.2091833E+06 0.1208136E+00 0.2240395E-01 28 0.9435237E+02 0.8786728E+03 0.4139941E-03 0.2076042E+06 0.1216994E+00 0.2250954E-01 29 0.9402696E+02 0.8832145E+03 0.4032342E-03 0.2059503E+06 0.1226342E+00 0.2259580E-01 30 0.9371333E+02 0.8872624E+03 0.3911377E-03 0.2044808E+06 0.1234668E+00 0.2263941E-01 31 0.9345320E+02 0.8902837E+03 0.3796212E-03 0.2033709E+06 0.1240939E+00 0.2263970E-01 32 0.9326420E+02 0.8922401E+03 0.3703191E-03 0.2026354E+06 0.1245069E+00 0.2261613E-01 33 0.9314015E+02 0.8933974E+03 0.3637566E-03 0.2021884E+06 0.1247562E+00 0.2258853E-01 34 0.9306421E+02 0.8940532E+03 0.3595549E-03 0.2019299E+06 0.1248998E+00 0.2256660E-01 35 0.9301982E+02 0.8944318E+03 0.3570411E-03 0.2017846E+06 0.1249823E+00 0.2255240E-01 36 0.9299524E+02 0.8947496E+03 0.3556919E-03 0.2017084E+06 0.1250408E+00 0.2254748E-01 37 0.9298691E+02 0.8957197E+03 0.3557079E-03 0.2017020E+06 0.1251651E+00 0.2257230E-01 38 0.9302118E+02 0.9018584E+03 0.3611029E-03 0.2019558E+06 0.1258789E+00 0.2277935E-01 39 0.9325669E+02 0.9366116E+03 0.3885500E-03 0.2036920E+06 0.1298238E+00 0.2387423E-01 40 0.9378595E+02 0.1010703E+04 0.3565100E-03 0.2112245E+06 0.1384073E+00 0.2515091E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.816392844E-04 0.169712984E-03 0.332919877E-03 0.636671160E-03 0.120663345E-02 2 0.494698959E-02 0.487309625E-02 0.480861957E-02 0.475276211E-02 0.470511559E-02 3 0.994971371E+00 0.994957191E+00 0.994858461E+00 0.994610567E+00 0.994088251E+00 Component Mole fractions on stages: 6 to 10 1 0.229274017E-02 0.442450346E-02 0.886102920E-02 0.193153368E-01 0.527499401E-01 2 0.466587748E-02 0.463630666E-02 0.461971993E-02 0.462374800E-02 0.466285441E-02 3 0.993041382E+00 0.990939190E+00 0.986519251E+00 0.976060915E+00 0.942587206E+00 Component Mole fractions on stages: 11 to 15 1 0.527133190E-01 0.526660425E-01 0.526052222E-01 0.525273543E-01 0.524283323E-01 2 0.650232483E-02 0.890548965E-02 0.120465120E-01 0.161542316E-01 0.215297703E-01 3 0.940784356E+00 0.938428468E+00 0.935348266E+00 0.931318414E+00 0.926041897E+00 Component Mole fractions on stages: 16 to 20 1 0.523036262E-01 0.521488084E-01 0.519607765E-01 0.517403173E-01 0.514971051E-01 2 0.285698986E-01 0.377978400E-01 0.499031453E-01 0.657911524E-01 0.866383559E-01 3 0.919126475E+00 0.910053352E+00 0.898136078E+00 0.882468530E+00 0.861864539E+00 Component Mole fractions on stages: 21 to 25 1 0.512584794E-01 0.510794509E-01 0.510051429E-01 0.504773982E-01 0.506805776E-01 2 0.113937981E+00 0.149490278E+00 0.195233344E+00 0.252803238E+00 0.276321349E+00 3 0.834803540E+00 0.799430271E+00 0.753761513E+00 0.696719364E+00 0.672998073E+00 Component Mole fractions on stages: 26 to 30 1 0.510934026E-01 0.519016748E-01 0.533614232E-01 0.556740431E-01 0.587437586E-01 2 0.311371985E+00 0.361923765E+00 0.431027514E+00 0.517909795E+00 0.614880044E+00 3 0.637534612E+00 0.586174560E+00 0.515611063E+00 0.426416162E+00 0.326376197E+00 Component Mole fractions on stages: 31 to 35 1 0.620715538E-01 0.650339892E-01 0.672712227E-01 0.687702449E-01 0.697066178E-01 2 0.708287192E+00 0.785456077E+00 0.841178124E+00 0.877525092E+00 0.899658676E+00 3 0.229641254E+00 0.149509934E+00 0.915506529E-01 0.537046627E-01 0.306347060E-01 Component Mole fractions on stages: 36 to 40 1 0.703293675E-01 0.712132343E-01 0.755769711E-01 0.105949231E+00 0.301675144E+00 2 0.912511347E+00 0.919306485E+00 0.919272741E+00 0.891388138E+00 0.697274533E+00 3 0.171592853E-01 0.948028093E-02 0.515028791E-02 0.266263072E-02 0.105032280E-02 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.169712984E-03 0.353322373E-03 0.695054610E-03 0.133631730E-02 0.255841330E-02 2 0.487309625E-02 0.480055934E-02 0.473771681E-02 0.468410686E-02 0.463994636E-02 3 0.994957191E+00 0.994846118E+00 0.994567229E+00 0.993979576E+00 0.992801640E+00 Component Mole fractions on stages: 6 to 10 1 0.495757432E-02 0.995285013E-02 0.217385647E-01 0.596872355E-01 0.410598858E+00 2 0.460663995E-02 0.458789028E-02 0.459218843E-02 0.463511566E-02 0.426892878E-02 3 0.990435786E+00 0.985459260E+00 0.973669247E+00 0.935677649E+00 0.585132213E+00 Component Mole fractions on stages: 11 to 15 1 0.410607287E+00 0.410619238E+00 0.410636471E+00 0.410661785E+00 0.410699702E+00 2 0.595395257E-02 0.815608470E-02 0.110355184E-01 0.148029117E-01 0.197355999E-01 3 0.583438761E+00 0.581224677E+00 0.578328010E+00 0.574535303E+00 0.569564698E+00 Component Mole fractions on stages: 16 to 20 1 0.410757644E+00 0.410847949E+00 0.410991284E+00 0.411222266E+00 0.411597672E+00 2 0.261988869E-01 0.346734487E-01 0.457890124E-01 0.603613907E-01 0.794213614E-01 3 0.563043469E+00 0.554478602E+00 0.543219703E+00 0.528416343E+00 0.508980966E+00 Component Mole fractions on stages: 21 to 25 1 0.412201825E+00 0.413089363E+00 0.413596216E+00 0.405735581E+00 0.406467042E+00 2 0.104203280E+00 0.136024987E+00 0.176037382E+00 0.226329559E+00 0.245395833E+00 3 0.483594895E+00 0.450885650E+00 0.410366402E+00 0.367934861E+00 0.348137125E+00 Component Mole fractions on stages: 26 to 30 1 0.407614351E+00 0.409285447E+00 0.411404246E+00 0.413578509E+00 0.415278089E+00 2 0.272820085E+00 0.310190907E+00 0.357063228E+00 0.409411018E+00 0.460131003E+00 3 0.319565564E+00 0.280523647E+00 0.231532526E+00 0.177010472E+00 0.124590909E+00 Component Mole fractions on stages: 31 to 35 1 0.416253819E+00 0.416651405E+00 0.416748714E+00 0.416745067E+00 0.416769369E+00 2 0.502491603E+00 0.533478060E+00 0.553927476E+00 0.566487693E+00 0.573811840E+00 3 0.812545781E-01 0.498705349E-01 0.293238102E-01 0.167672392E-01 0.941879011E-02 Component Mole fractions on stages: 36 to 40 1 0.417161530E+00 0.420205249E+00 0.441798430E+00 0.563983729E+00 0.833848844E+00 2 0.577613291E+00 0.576939777E+00 0.556721324E+00 0.435434362E+00 0.166051156E+00 3 0.522517908E-02 0.285497394E-02 0.148024587E-02 0.581908394E-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] -2.775077226E+06 [Reboiler Heat Duty] 2.690140545E+06 [K-values] Component K-values on stages: 1 to 5 1 0.481043249E+00 0.480334668E+00 0.478983773E+00 0.476437117E+00 0.471633515E+00 2 0.101516340E+01 0.101510997E+01 0.101496547E+01 0.101465694E+01 0.101404513E+01 3 0.100001425E+01 0.100011165E+01 0.100029282E+01 0.100063481E+01 0.100129594E+01 Component K-values on stages: 6 to 10 1 0.462472175E+00 0.444546378E+00 0.407617952E+00 0.323609172E+00 0.128470742E+00 2 0.101285904E+01 0.101055296E+01 0.100599517E+01 0.997547387E+00 0.109227733E+01 3 0.100263076E+01 0.100556079E+01 0.101319750E+01 0.104315938E+01 0.161089611E+01 Component K-values on stages: 11 to 15 1 0.128378918E+00 0.128260046E+00 0.128106551E+00 0.127909039E+00 0.127656125E+00 2 0.109210217E+01 0.109188289E+01 0.109161266E+01 0.109128742E+01 0.109091034E+01 3 0.161248176E+01 0.161457093E+01 0.161733177E+01 0.162099424E+01 0.162587657E+01 Component K-values on stages: 16 to 20 1 0.127334517E+00 0.126929704E+00 0.126427928E+00 0.125820807E+00 0.125115152E+00 2 0.109050046E+01 0.109010904E+01 0.108984978E+01 0.108995421E+01 0.109086969E+01 3 0.163242543E+01 0.164127768E+01 0.165335696E+01 0.167002505E+01 0.169331389E+01 Component K-values on stages: 21 to 25 1 0.124352869E+00 0.123652302E+00 0.123321106E+00 0.124409592E+00 0.124685577E+00 2 0.109342029E+01 0.109899130E+01 0.110904480E+01 0.111696961E+01 0.112602299E+01 3 0.172624556E+01 0.177302221E+01 0.183680123E+01 0.189359432E+01 0.193314078E+01 Component K-values on stages: 26 to 30 1 0.125347408E+00 0.126810458E+00 0.129705573E+00 0.134615416E+00 0.141456437E+00 2 0.114130887E+01 0.116677748E+01 0.120714619E+01 0.126501186E+01 0.133631518E+01 3 0.199500411E+01 0.208957272E+01 0.222694872E+01 0.240898833E+01 0.261958277E+01 Component K-values on stages: 31 to 35 1 0.149119482E+00 0.156087292E+00 0.161419149E+00 0.165017538E+00 0.167254656E+00 2 0.140955031E+01 0.147233061E+01 0.151857086E+01 0.154906294E+01 0.156786356E+01 3 0.282619465E+01 0.299796131E+01 0.312205857E+01 0.320295204E+01 0.325250969E+01 Component K-values on stages: 36 to 40 1 0.168590252E+00 0.169472501E+00 0.171066636E+00 0.187858666E+00 0.361786368E+00 2 0.157979631E+01 0.159341845E+01 0.165122603E+01 0.204712401E+01 0.419915495E+01 3 0.328396119E+01 0.332061908E+01 0.347934625E+01 0.457568710E+01 0.105032280E+02 [Molecular weights] 1 94.113 2 92.141 3 98.188 [Feed stream 1] 10 Stage Number 5.0032091341637E-02 Flow rate 3.7300000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -4.2171881423486E+07 Enthalpy [J/kmol] -8.6075579473399E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9980090752016E-01 Mole fraction of component 1 1.9909244857911E-04 Mole fraction of component 2 3.1259110739560E-11 Mole fraction of component 3 5.0032091341637E-02 Flow rate 9.9980090752016E-01 Mole fraction of component 1 1.9909244857911E-04 Mole fraction of component 2 3.1259110739560E-11 Mole fraction of component 3 9.4112606352197E+01 Molar mass 1.1182644720425E+03 Density 1.0724134353447E-03 Viscosity 1.4883455896794E-01 Thermal conductivity 1.8870000102335E+05 Heat capacity 3.2492083914772E-02 Surface tension [Feed stream 2] 25 Stage Number 2.0000000000000E-02 Flow rate 3.8400000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] 1.2062363941554E+07 Enthalpy [J/kmol] 4.0032098867236E+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 9.5164501190186E+01 Molar mass 3.1275560157045E+00 Density 8.6940984685969E-06 Viscosity 2.0028537772932E-02 Thermal conductivity 1.5602017494965E+05 Heat capacity [Reflashed Feed stream 1] 10 Stage Number 5.0032091341637E-02 Flow rate 3.7300000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -4.2171881423486E+07 Enthalpy [J/kmol] -8.6075579473399E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9980090752016E-01 Mole fraction of component 1 1.9909244857911E-04 Mole fraction of component 2 3.1259110739560E-11 Mole fraction of component 3 5.0032091341637E-02 Flow rate 9.9980090752016E-01 Mole fraction of component 1 1.9909244857911E-04 Mole fraction of component 2 3.1259110739560E-11 Mole fraction of component 3 9.4112606352197E+01 Molar mass 1.1182644720425E+03 Density 1.0724134353446E-03 Viscosity 1.4883455896794E-01 Thermal conductivity 1.8870000102335E+05 Heat capacity 3.2492083914772E-02 Surface tension [Reflashed Feed stream 2] 25 Stage Number 2.0000000000000E-02 Flow rate 3.8400000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] 1.2062363941554E+07 Enthalpy [J/kmol] 4.0032098867236E+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 9.5164501190186E+01 Molar mass 3.1275560157045E+00 Density 8.6940984685969E-06 Viscosity 2.0028537772933E-02 Thermal conductivity 1.5602017494965E+05 Heat capacity [Top product] 1 Stage Number 1.0044654510000E-02 Flow rate 3.7409021350000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -1.9002290665687E+07 Enthalpy [J/kmol] -4.7006275278906E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.6971298400000E-04 Mole fraction of component 1 4.8730962500000E-03 Mole fraction of component 2 9.9495719100000E-01 Mole fraction of component 3 1.0044654510000E-02 Flow rate 1.6971298400000E-04 Mole fraction of component 1 4.8730962500000E-03 Mole fraction of component 2 9.9495719100000E-01 Mole fraction of component 3 9.8157844345903E+01 Molar mass 7.2499244349965E+02 Density 2.9859041477393E-04 Viscosity 9.3525855543168E-02 Thermal conductivity 2.3075419913355E+05 Heat capacity 1.5054086683863E-02 Surface tension [Bottom product] 40 Stage Number 5.9987607680000E-02 Flow rate 4.2087217360000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.9385612607831E+07 Enthalpy [J/kmol] -5.4950881093394E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 8.3384884400000E-01 Mole fraction of component 1 1.6605115600000E-01 Mole fraction of component 2 1.0000000000000E-04 Mole fraction of component 3 5.9987607680000E-02 Flow rate 8.3384884400000E-01 Mole fraction of component 1 1.6605115600000E-01 Mole fraction of component 2 1.0000000000000E-04 Mole fraction of component 3 9.3785953562958E+01 Molar mass 1.0107034198553E+03 Density 3.5651001021197E-04 Viscosity 1.3840725753212E-01 Thermal conductivity 2.1122453918206E+05 Heat capacity 2.5150913307413E-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(qaw@nN%aw@:Ӛaw@26aw@;^,bw@Fbw@}tjdw@\pgw@rw@o+w@O;w@.Hw@nw@(ܿw@6VNw@Ԭ}Kw@w@pw@;1 w@: w@pmw@E(bw@ qw@Tw@w@;Fw@{cw@FM x@:f?$x@0@x@c\x@sx@lvNx@sqx@N牕x@`x@/B@9x@%x@ ix@NlMz@"Pressure profile.Pressure at each stage(м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@(Vapour Flow profile4Vapour Flow at each stage(H#$@"9V@OV@pV@x4V@oNV@aV@,UCAV@/祤YV@dNU@BxW@wnwW@vW@aC tW@FZ3rW@?oW@ MkW@CcfW@j8R@G R@Q@-N@(Liquid Flow profile4Liquid Flow at each stage(T@Q~sT@~T@"T@;k](T@o T@PeS@$S@%rS@V6b`@Mۿ`@8QKs`@!C}`@.`@H&Jn`@Gq`@Jdz̲`@V@`@: }`@`@Cv`@5n`@S#35`@gL22`@o+`@y"{`@9fq`@pMp6g`@ &4a`@rb`@,pi`@A`s`@s:|`@.Â`@β`@\`@`@2:=o@`@Im^@ppiM@Duties profile*Duties at each stage(h,E\E.DA4Vapour Moleweight profile@Vapour Moleweight at each stage(|'fX@ X@+5{X@됛X@>:uX@k X@X@ǀX@4X@ h"lx|X@ݘ{X@ILzX@yX@xX@됛vX@=UsX@|oX@I +kX@z1eX@Pn]X@\RX@aDX@IQ,3X@<X@ 7X@4X@8mW@_MW@"W@-iW@V/iW@ZKW@~R4W@겘|&W@5lW@iqW@YLl>W@F6W@ mW@/$/W@.Vapour Density profile:Vapour Density at each stage(zV @AF @sE)! @^, ӗ @@9 @V @Oz1 @7 @yq} @w @.! @0E @  @5Z @H7¢" @zi @nߣz @AgҦ @<$ @CsFZ @Tގp @k @zW @\> @£#v @] @Ot]9 @۽' @a56@l dv}@6@'+V@_:@ظ]@5[y@@E*-@Bf@!k>@9j3@2Vapour Viscosity profile>Vapour Viscosity at each stage(;4D9>Cڨ9>D9>C9>dVx:>x;> G̃=>ݗn B>vN>s^><(>OyN>w[X>/^> w5> (|p>K@>cF>~> A>8ֻ>1.>╕>+oQ%>@%>5^>c,w&>I>5Vv>ZS>PC[>(U>5 &>2~;>9DPpG>ЉN>).T>^_>@[>f>:Vapour Heat capacity profileFVapour Heat capacity at each stage(33333e@48e@I +e@~e@;Nёe@V/e@+e~e@\mze@ZB>ue@?e@a+ee@!ue@ -e@=U}e@N@we@@ܵne@&Sce@M OTe@K7Ae@J +(e@\Ce@2%d@`vOd@Scd@7dHd@=,Ԛd@Sc@y&1c@!uq1c@gb@ec]Pb@ qa@ݓa@M Oa@9ga@sAWa@^I Oa@Pa@ׁ{a@Oe-b@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stage(xG?u#?r ?~ ? 1 ?x+- ?S?^;߫?]؎?uH?E*?׆ic?*:P?gC?zy?Hig?n?RoS?Tl?T,҉?% ?ٔ?3 sL̔?35?@?/6Ʊ?-ؙ?Rm"?ʁ?/Psnn?7k2\?VxK?a@HyZW@ۅ:W@6oW@]P2mW@:]W@PW@47HW@BDW@DAW@?W@)?W@[[AW@umPW@:MrW@.Liquid Density profile:Liquid Density at each stage(gDio@oJ@Q@_Q@@⬆@S!@jt@LՆ@"y(@-o@U0*@;N@Ǻ@;O@sF@Af@TA@Nё\@9v>@Ɗ@ё\؊@:M@d`T @d;O @B`"#@鷯7@H?S@eau@K@+e@oEҋ@(~@q -@-!l@MSt@H.@s@.@qD@v@2Liquid Viscosity profile>Liquid Viscosity at each stage(3?3?leZ{3? 'O3?%^)3?wh3?zaxv3?4?84? ]n>?,rLk>?X? Dh>?7uWc>?ȴe}]>?b֫pU>?>J>??<>?&*>?9IV>?b(=?P=?r52=?'0=?KBׁ]7?:Liquid Heat capacity profileFLiquid Heat capacity at each stage( h"l@+ l@W2l@H.l@tl@Y8l@8EGrl@Bfl@%Cl@uk@Hrk@0' k@_Lk@}8gk@Y|k@lwsk@ hk@_Zk@>W[Gk@ڊe/k@K4k@_j@W2j@j@jMoj@Oj@k+%j@=Ui@qhi@V}bi@Biki@|a2UTi@ o_Fi@=i@"uq9i@z66i@X9v6i@>i@/$vi@w/gj@:Liquid Thermal cond. profileFLiquid Thermal cond. at each stage(O?Bl?3H ?j ?f?UV? ߵ?&N9?Gxs?вf?́? P?'t?hX1d?wۓ?s9>Z?F-(g?ʢU/?4|ɽ?£#?OԈO?)X.?9ټ`?F;?Kub?xλV罾?zܣ?\'?_vd?9K$,?y"*Ŀ?W'߿?%?Fn?90 ?4UAV?wߌh?`?n?dT?0Surface tension profile<Surface tension at each stage(Ԏ?qOՎ?Ig؎?Hݎ?W*bm?0?َ,"?u'>?v0(v[?t2?dt?W?R?y?5"?݋(?{{0? 7V{;?GuWQI?*U[?"r?!i?)# 򣯖?"gx?v\v–? X!ז?r4?R ?xZ#?3.?p].?,ʮ(?wur!?z??/į?×.i1?MxS?aDt|r?8(? 1 Converged 0 Iterations 6ChemSep (TM) - COL2 6.81 Copyright (c) 1988-2011 Harry Kooijman and Ross Taylor 2100 6 LITE free license Checking data file C:\Users\jasper\AppData\Local\Temp\CS_3_4~2.SEP Cape Open unit name: Extractive Distillation Cape-Open unit id: CS_3_4B4_1CC1AAE_C53EC40 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 108-95-2 Phenol 108-88-3 Toluene 108-87-2 Methylcyclohexane Determining feed conditions Possible trivial solution Run level: Initialization Reading initial temperature profiles Reading initial composition profiles Init 47 milliseconds Run level: Complete model Iteration Error 0 -0.5973 Run level: Report Convergence obtained in 0 iterations Time 109 milliseconds FixMem driver done run time: 0.3 seconds Using: C:\Program Files (x86)\ChemSepL6v70\bin\co-col2.exe Using CAPE-OPEN version 1.0 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: 0.0013-;&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,@/@? @@ @?(@@(@@@@message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.09 K, range = [383.78 - 1000.00] K)  (last message repeated 1 time) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.10 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.11 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.14 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.18 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.28 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.50 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 375.17 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 379.94 K, range = [383.78 - 1000.00] K)  (last message repeated 1 time) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 379.96 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 379.97 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 379.99 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.02 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.06 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.11 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.18 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.29 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.44 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.66 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 381.00 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 381.47 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 382.00 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 382.31 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 382.81 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 383.59 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.09 K, range = [273.15 - 374.08] K)  (last message repeated 1 time) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.10 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.11 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.14 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.18 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.28 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.50 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 375.17 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 379.94 K, range = [273.15 - 374.08] K)  (last message repeated 1 time) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 379.96 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 379.97 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 379.99 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.02 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.06 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.11 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.18 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.29 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.44 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.66 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 381.00 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 381.47 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 382.00 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 382.31 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 382.81 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 383.59 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 384.73 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 384.73 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 386.27 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 386.27 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 388.05 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 388.05 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 389.79 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 389.79 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 391.24 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 391.24 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 392.27 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 392.27 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 392.94 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 392.94 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 393.35 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 393.35 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 393.60 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 393.60 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 393.83 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 393.83 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 394.61 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 394.61 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 399.49 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 399.49 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 420.87 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 420.87 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.09 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.09 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 420.87 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 420.87 K, range = [273.15 - 374.08] K) RecoveryChemSep Unit OperationqeWCXc_CSUOh[ChemSep] Version=6.82 Compiled=2011-5-25 00:06 Name=C:\Users\jasper\AppData\Local\Temp\CS_4_4~1.sep Title=ChemSep CO Unit Operation "Recovery" in COFE Flowsheet User=jasper Date=2011-05-25 Time=09:33:44 [Cape-Open] unitname=Recovery CO_ID=CS_4_4B4_1CC1AAE_C565D40 3 components Phenol 108-95-2 94.1129989624 Mw Toluene 108-88-3 92.1409988403 Mw Methylcyclohexane 108-87-2 98.18800354 Mw 0 thermo exe=C:\Program Files (x86)\ChemSepL6v70\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 (x86)\chemsepl6v70\bin\ Help and Info path=c:\program files (x86)\chemsepl6v70\help\ Component data path=c:\program files (x86)\chemsepl6v70\pcd\ Property data path=c:\program files (x86)\chemsepl6v70\ipd\ Section data path=c:\program files (x86)\chemsepl6v70\ild\ Executables path=C:\Program Files (x86)\ChemSepL6v70\bin\ Temporary path=WINTMPDIR Scripts path=c:\program files (x86)\chemsepl6v70\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=2010-09-20,09:33:26 CHK=11034 CAS=108-95-2 CID=Phenol Name=Phenol Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 140 502 Library Offset, Index DT=2010-09-20,09:33:26 CHK=62500 CAS=108-88-3 CID=Toluene Name=Toluene Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 144 138 Library Offset, Index DT=2010-09-20,09:33:26 CHK=31662 CAS=108-87-2 CID=Methylcyclohexane Name=Methylcyclohexane Lib=c:\program files (x86)\chemsepl6v70\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] 350 BIP estimation temperature [Thermodynamics] 4 K model DECHEMA 8 * Activity coefficient UNIFAC * Wilson model * * UNIQUAC model * 3 Equation of State Cubic 5 Cubic EOS Peng-Robinson 76 * Virial EOS * 1 Vapour pressure Antoine 0 Henry's law * Henry's default * [Enthalpy] 3 Enthalpy Excess 1 Enthalpy reference state Vapour 298.15 Enthalpy reference temperature 1 Formation enthalpies Excluded 298.15 Exergy surroundings temperature [Physical property models] 0 No Check T range * Cubic EOS * * Virial EOS * * Vapour model * * Liquid mixture density * * Liquid component density * * Vapour mixture viscosity * * Vapour mixture viscosity pressure correction * * Vapour component viscosity * * Liquid mixture viscosity * * Liquid component viscosity * Vapour mixture Cp * Vapour component Cp * Liquid mixture Cp * Liquid component Cp * Vapour mixture conductivity * * Vapour component conductivity * * Liquid mixture conductivity * * Liquid component conductivity * Mixture surface tension * * Component surface tension * * Vignes MS D-model * * D mixture model * * Vapour Diffusion Coefficients * [Reaction data] 0 Number of reactions [Specifications] Top Bottom [Heaters/Coolers] 0 Number 0 Column duty Qcolumn 2 First stage 19 Last stage 0 Qcolumn lost to surroundings [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} 420.872173574 Temperature 101325 Pressure 0 Vapour fraction 3 componentflows 0.0500205973183 Component 1 flow 0.00996101160094 Component 2 flow 5.998760768e-006 Component 3 flow [Condenser] 7 Type Mole fraction of a component 0.001 Value Qcondenser 1 1st comp. * Type * * Initialization guess [Reboiler] 8 Type Component recovery 0.001 Value Qreboiler 2 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] 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 -1 ComboBox=ComboBox23 -1 StringGrid=StringGrid7 16 2 StringGrid=StringGrid11 5 3 CheckBox=CheckBox45 0 Lumped ComboBox=ComboBox75 -1 ComboBox=ComboBox76 -1 ComboBox=ComboBox77 -1 Edit=Edit55 0.95 Edit=Edit56 0.95 Edit=Edit57 1.2 Edit=Edit1 1 CheckBox=CheckBox2 0 Use old results CheckBox=CheckBox3 1 Automatic CheckBox=CheckBox1 0 Keep sep-files CheckBox=CheckBox4 1 Restore original StringGrid=StringGrid1 1 6 StringGrid=StringGrid2 4 1 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 1635136 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 1635136 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 1635136 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 1635136 SpinEdit=SpinEdit3 1 ComboBox=ComboBox14 0 RadioButton=RadioButton3 TRUE DrawSetColors=BVLEcolors 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 ComboBox=ComboBox7 -1 ComboBox=ComboBox11 -1 ComboBox=ComboBox6 -1 Memo=Memo1 Memo1, ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox4 0 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Ternary Phase Diagram Edit=Edit4 Edit=Edit6 Edit=Edit7 chemsep1.pcd Edit=Edit8 Edit=Edit5 StringGrid=StringGrid1 1 7 Identifier L# File Loc. CAS SMILES Name 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 1 383.8000963 1.013250000E+05 9.967016340E-03 1.067263306E-02 -6.791064673E+05 2 383.8655281 1.013250000E+05 2.063964940E-02 1.065846566E-02 0.000000000E+00 3 383.9728443 1.013250000E+05 2.062548200E-02 1.063238112E-02 0.000000000E+00 4 384.1689092 1.013250000E+05 2.059939746E-02 1.058079672E-02 0.000000000E+00 5 384.5595361 1.013250000E+05 2.054781306E-02 1.046499906E-02 0.000000000E+00 6 385.4558879 1.013250000E+05 2.043201540E-02 1.013986746E-02 0.000000000E+00 7 388.1073372 1.013250000E+05 2.010688380E-02 9.071125773E-03 0.000000000E+00 8 397.3942705 1.013250000E+05 1.903814211E-02 7.287960371E-03 0.000000000E+00 9 413.3436435 1.013250000E+05 1.725497671E-02 6.637989316E-03 0.000000000E+00 10 421.3326613 1.013250000E+05 1.660500566E-02 6.585389943E-03 0.000000000E+00 11 423.3682545 1.013250000E+05 1.655240628E-02 6.585032822E-03 0.000000000E+00 12 423.8039125 1.013250000E+05 1.655204916E-02 6.659354415E-02 0.000000000E+00 13 429.1667518 1.013250000E+05 1.657295280E-02 6.690483687E-02 0.000000000E+00 14 437.2499059 1.013250000E+05 1.688424553E-02 6.784263541E-02 0.000000000E+00 15 445.3881921 1.013250000E+05 1.782204407E-02 6.918984474E-02 0.000000000E+00 16 450.7663192 1.013250000E+05 1.916925340E-02 7.025736374E-02 0.000000000E+00 17 453.3674931 1.013250000E+05 2.023677240E-02 7.081925403E-02 0.000000000E+00 18 454.4292108 1.013250000E+05 2.079866268E-02 7.105681284E-02 0.000000000E+00 19 454.8315146 1.013250000E+05 2.103622150E-02 7.114805529E-02 0.000000000E+00 20 454.9795825 1.013250000E+05 2.112746395E-02 5.002059134E-02 9.569489709E+05 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.2223167E+08 -0.2223167E+08 -0.5553823E+05 -0.5553823E+05 2 0.1067133E+08 -0.2224964E+08 0.2971701E+05 -0.5545317E+05 3 0.1068465E+08 -0.2228221E+08 0.2981032E+05 -0.5531202E+05 4 0.1070954E+08 -0.2234598E+08 0.2997908E+05 -0.5509397E+05 5 0.1075953E+08 -0.2248651E+08 0.3028503E+05 -0.5476167E+05 6 0.1087517E+08 -0.2286850E+08 0.3089739E+05 -0.5429801E+05 7 0.1122200E+08 -0.2428615E+08 0.3240670E+05 -0.5419709E+05 8 0.1246027E+08 -0.2817845E+08 0.3689785E+05 -0.5644775E+05 9 0.1461373E+08 -0.2967701E+08 0.4415559E+05 -0.5622644E+05 10 0.1568969E+08 -0.2935431E+08 0.4759035E+05 -0.5485926E+05 11 0.1596224E+08 -0.2921045E+08 0.4842429E+05 -0.5443508E+05 12 0.1602045E+08 -0.2917700E+08 0.4859992E+05 -0.5434107E+05 13 0.1673184E+08 -0.2869741E+08 0.5064320E+05 -0.5310415E+05 14 0.1778582E+08 -0.2778508E+08 0.5324082E+05 -0.5102944E+05 15 0.1881279E+08 -0.2669690E+08 0.5478739E+05 -0.4879936E+05 16 0.1946563E+08 -0.2590714E+08 0.5466981E+05 -0.4732063E+05 17 0.1977233E+08 -0.2550850E+08 0.5393278E+05 -0.4663954E+05 18 0.1989564E+08 -0.2534296E+08 0.5333945E+05 -0.4638435E+05 19 0.1994206E+08 -0.2527983E+08 0.5300249E+05 -0.4629814E+05 20 0.1995910E+08 -0.2525653E+08 0.5283487E+05 -0.4627085E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.9214776E+02 0.3026685E+01 0.8974305E-05 0.1350941E+06 0.1886303E-01 2 0.9214661E+02 0.3026089E+01 0.8976247E-05 0.1350954E+06 0.1886667E-01 3 0.9214824E+02 0.3025233E+01 0.8979132E-05 0.1351204E+06 0.1887377E-01 4 0.9215231E+02 0.3023707E+01 0.8984271E-05 0.1351744E+06 0.1888727E-01 5 0.9216029E+02 0.3020664E+01 0.8994383E-05 0.1352861E+06 0.1891486E-01 6 0.9217663E+02 0.3013629E+01 0.9017198E-05 0.1355482E+06 0.1898048E-01 7 0.9221502E+02 0.2992638E+01 0.9082915E-05 0.1363454E+06 0.1918519E-01 8 0.9232550E+02 0.2920685E+01 0.9308663E-05 0.1391461E+06 0.1992510E-01 9 0.9257344E+02 0.2807649E+01 0.9707472E-05 0.1435652E+06 0.2109610E-01 10 0.9274944E+02 0.2756393E+01 0.9918261E-05 0.1454969E+06 0.2158748E-01 11 0.9280130E+02 0.2743913E+01 0.9973579E-05 0.1459515E+06 0.2169850E-01 12 0.9281280E+02 0.2741273E+01 0.9985513E-05 0.1460466E+06 0.2172141E-01 13 0.9296531E+02 0.2709622E+01 0.1013553E-04 0.1471402E+06 0.2197614E-01 14 0.9324481E+02 0.2665121E+01 0.1037342E-04 0.1485418E+06 0.2225160E-01 15 0.9359429E+02 0.2624235E+01 0.1063061E-04 0.1495839E+06 0.2236317E-01 16 0.9386820E+02 0.2599419E+01 0.1081229E-04 0.1500330E+06 0.2232442E-01 17 0.9401420E+02 0.2588058E+01 0.1090397E-04 0.1501734E+06 0.2226847E-01 18 0.9407646E+02 0.2583542E+01 0.1094216E-04 0.1502153E+06 0.2223808E-01 19 0.9410047E+02 0.2581850E+01 0.1095674E-04 0.1502289E+06 0.2222538E-01 20 0.9410936E+02 0.2581229E+01 0.1096213E-04 0.1502335E+06 0.2222054E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.9214661E+02 0.7852831E+03 0.2360513E-03 0.1953850E+06 0.1117805E+00 0.1812331E-01 2 0.9214977E+02 0.7858655E+03 0.2366143E-03 0.1953986E+06 0.1118554E+00 0.1814838E-01 3 0.9215765E+02 0.7868919E+03 0.2376638E-03 0.1954378E+06 0.1119846E+00 0.1819294E-01 4 0.9217318E+02 0.7888216E+03 0.2396620E-03 0.1955271E+06 0.1122268E+00 0.1827681E-01 5 0.9220522E+02 0.7927988E+03 0.2438135E-03 0.1957493E+06 0.1127257E+00 0.1844955E-01 6 0.9228227E+02 0.8025011E+03 0.2540842E-03 0.1963997E+06 0.1139413E+00 0.1886921E-01 7 0.9252205E+02 0.8338146E+03 0.2882314E-03 0.1985131E+06 0.1178203E+00 0.2019094E-01 8 0.9315718E+02 0.9226603E+03 0.3785511E-03 0.2029372E+06 0.1282548E+00 0.2345346E-01 9 0.9365460E+02 0.9936605E+03 0.3852716E-03 0.2084855E+06 0.1362946E+00 0.2508045E-01 10 0.9379218E+02 0.1011510E+04 0.3543746E-03 0.2113929E+06 0.1385148E+00 0.2514607E-01 11 0.9382114E+02 0.1015006E+04 0.3448243E-03 0.2121497E+06 0.1389870E+00 0.2512176E-01 12 0.9382708E+02 0.1015709E+04 0.3427184E-03 0.2123125E+06 0.1390842E+00 0.2511482E-01 13 0.9389361E+02 0.1023188E+04 0.3154401E-03 0.2143355E+06 0.1401856E+00 0.2498561E-01 14 0.9397645E+02 0.1031203E+04 0.2718662E-03 0.2174463E+06 0.1415990E+00 0.2467186E-01 15 0.9404489E+02 0.1036367E+04 0.2280888E-03 0.2206361E+06 0.1428291E+00 0.2425422E-01 16 0.9408426E+02 0.1038585E+04 0.2003795E-03 0.2227682E+06 0.1435756E+00 0.2393816E-01 17 0.9410199E+02 0.1039380E+04 0.1875004E-03 0.2238049E+06 0.1439237E+00 0.2377630E-01 18 0.9410901E+02 0.1039657E+04 0.1823554E-03 0.2242289E+06 0.1440639E+00 0.2370875E-01 19 0.9411164E+02 0.1039756E+04 0.1804236E-03 0.2243897E+06 0.1441167E+00 0.2368294E-01 20 0.9411261E+02 0.1039791E+04 0.1797151E-03 0.2244489E+06 0.1441362E+00 0.2367341E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.300556379E-03 0.100000000E-02 0.221991890E-02 0.440319704E-02 0.849141662E-02 2 0.998679260E+00 0.998398139E+00 0.997306347E+00 0.995162587E+00 0.991087203E+00 3 0.102018365E-02 0.601861074E-03 0.473733873E-03 0.434215867E-03 0.421380303E-03 Component Mole fractions on stages: 6 to 10 1 0.167922655E-01 0.362779441E-01 0.923237788E-01 0.218098838E+00 0.307375581E+00 2 0.982791828E+00 0.963311003E+00 0.907273290E+00 0.781511862E+00 0.692244212E+00 3 0.415906226E-03 0.411052573E-03 0.402931299E-03 0.389299343E-03 0.380206996E-03 Component Mole fractions on stages: 11 to 15 1 0.333684135E+00 0.339519014E+00 0.417602482E+00 0.559620195E+00 0.736936456E+00 2 0.665939250E+00 0.660105319E+00 0.582265708E+00 0.440340466E+00 0.263054326E+00 3 0.376614695E-03 0.375667031E-03 0.131810440E-03 0.393394553E-04 0.921841789E-05 Component Mole fractions on stages: 16 to 20 1 0.875856238E+00 0.949896176E+00 0.981470807E+00 0.993644931E+00 0.998154935E+00 2 0.124142056E+00 0.501035525E-01 0.185291533E-01 0.635506290E-02 0.184506461E-02 3 0.170606687E-05 0.271559973E-06 0.401930395E-07 0.571692065E-08 0.740827583E-09 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.100000000E-02 0.336069770E-02 0.759342512E-02 0.155482645E-01 0.318330476E-01 2 0.998398139E+00 0.996285384E+00 0.992129513E+00 0.984200366E+00 0.967928152E+00 3 0.601861074E-03 0.353918699E-03 0.277061742E-03 0.251369021E-03 0.238800139E-03 Component Mole fractions on stages: 6 to 10 1 0.709545170E-01 0.192666960E+00 0.515003265E+00 0.767402002E+00 0.837203026E+00 2 0.928821986E+00 0.807148686E+00 0.484898135E+00 0.232550607E+00 0.162761271E+00 3 0.223496721E-03 0.184354643E-03 0.985998652E-04 0.473908763E-04 0.357033145E-04 Component Mole fractions on stages: 11 to 15 1 0.851896804E+00 0.854910747E+00 0.888715942E+00 0.930747220E+00 0.965461633E+00 2 0.148069893E+00 0.145056450E+00 0.111274130E+00 0.692503579E-01 0.345378941E-01 3 0.333027907E-04 0.328033264E-04 0.992781115E-05 0.242167204E-05 0.472693530E-06 Component Mole fractions on stages: 16 to 20 1 0.985426429E+00 0.994417571E+00 0.997978411E+00 0.999312103E+00 0.999800862E+00 2 0.145734930E-01 0.558241715E-02 0.202158690E-02 0.687897193E-03 0.199138221E-03 3 0.782417816E-07 0.118262391E-07 0.171449243E-08 0.241971009E-09 0.312662974E-10 [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] -6.791064673E+05 [Reboiler Heat Duty] 9.569489709E+05 [K-values] Component K-values on stages: 1 to 5 1 0.300556379E+00 0.297557260E+00 0.292347507E+00 0.283195404E+00 0.266748465E+00 2 0.100028157E+01 0.100212063E+01 0.100521790E+01 0.101113820E+01 0.102392641E+01 3 0.169504841E+01 0.170056309E+01 0.170984947E+01 0.172740406E+01 0.176457310E+01 Component K-values on stages: 6 to 10 1 0.236662388E+00 0.188293540E+00 0.179268345E+00 0.284204165E+00 0.367145811E+00 2 0.105810569E+01 0.119347404E+01 0.187105950E+01 0.336060974E+01 0.425312607E+01 3 0.186090528E+01 0.222968387E+01 0.408652981E+01 0.821464734E+01 0.106490672E+02 Component K-values on stages: 11 to 15 1 0.391695490E+00 0.397139720E+00 0.469894220E+00 0.601259057E+00 0.763299577E+00 2 0.449746558E+01 0.455067884E+01 0.523271404E+01 0.635867417E+01 0.761639731E+01 3 0.113088029E+02 0.114521017E+02 0.132768883E+02 0.162447492E+02 0.195018913E+02 Component K-values on stages: 16 to 20 1 0.888809364E+00 0.955228672E+00 0.983458957E+00 0.994328927E+00 0.998353744E+00 2 0.851834599E+01 0.897524336E+01 0.916564767E+01 0.923839051E+01 0.926524601E+01 3 0.218050615E+02 0.229624964E+02 0.234431129E+02 0.236264694E+02 0.236941258E+02 [Molecular weights] 1 94.113 2 92.141 3 98.188 [Feed stream 1] 12 Stage Number 5.9987607680008E-02 Flow rate 4.2087217357400E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.9385612613117E+07 Enthalpy [J/kmol] -7.5043573215984E+03 Entropy [J/kmol/K] 5.9525210483877E-12 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 8.3384884400000E-01 Mole fraction of component 1 1.6605115600000E-01 Mole fraction of component 2 9.9999999999987E-05 Mole fraction of component 3 3.5707749735767E-13 Flow rate 3.0167514464405E-01 Mole fraction of component 1 6.9727453255296E-01 Mole fraction of component 2 1.0503228029867E-03 Mole fraction of component 3 5.9987607679651E-02 Flow rate 8.3384884400316E-01 Mole fraction of component 1 1.6605115599684E-01 Mole fraction of component 2 9.9999999994330E-05 Mole fraction of component 3 9.2742253569322E+01 Molar mass 2.7593756652924E+00 Density 9.9054437504959E-06 Viscosity 2.1563077902231E-02 Thermal conductivity 1.4542285002539E+05 Heat capacity 9.3785953562964E+01 Molar mass 1.0107034198828E+03 Density 3.5651001040006E-04 Viscosity 1.3840725753425E-01 Thermal conductivity 2.1122453917018E+05 Heat capacity 2.5150913310236E-02 Surface tension [Reflashed Feed stream 1] 12 Stage Number 5.9987607680008E-02 Flow rate 4.2087217357394E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.9385612613117E+07 Enthalpy [J/kmol] -7.5043573216589E+03 Entropy [J/kmol/K] 6.2975180625813E-12 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 8.3384884400000E-01 Mole fraction of component 1 1.6605115600000E-01 Mole fraction of component 2 9.9999999999987E-05 Mole fraction of component 3 3.7777304289589E-13 Flow rate 3.0167514464293E-01 Mole fraction of component 1 6.9727453255408E-01 Mole fraction of component 2 1.0503228029872E-03 Mole fraction of component 3 5.9987607679630E-02 Flow rate 8.3384884400335E-01 Mole fraction of component 1 1.6605115599666E-01 Mole fraction of component 2 9.9999999994002E-05 Mole fraction of component 3 9.2742253569319E+01 Molar mass 2.7593756652927E+00 Density 9.9054437504942E-06 Viscosity 2.1563077902229E-02 Thermal conductivity 1.4542285002538E+05 Heat capacity 9.3785953562965E+01 Molar mass 1.0107034198829E+03 Density 3.5651001040053E-04 Viscosity 1.3840725753427E-01 Thermal conductivity 2.1122453917015E+05 Heat capacity 2.5150913310244E-02 Surface tension [Top product] 1 Stage Number 9.9670163400000E-03 Flow rate 3.8380009630000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.2231669454426E+07 Enthalpy [J/kmol] -5.5538233085238E+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 9.9839813900000E-01 Mole fraction of component 2 6.0186107400000E-04 Mole fraction of component 3 9.9670163400000E-03 Flow rate 1.0000000000000E-03 Mole fraction of component 1 9.9839813900000E-01 Mole fraction of component 2 6.0186107400000E-04 Mole fraction of component 3 9.2146610304016E+01 Molar mass 7.8528308459748E+02 Density 2.3605127662118E-04 Viscosity 1.1178045205746E-01 Thermal conductivity 1.9538502494985E+05 Heat capacity 1.8123307569495E-02 Surface tension [Bottom product] 20 Stage Number 5.0020591340000E-02 Flow rate 4.5497958250000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.5256532253926E+07 Enthalpy [J/kmol] -4.6270850661830E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9980086200000E-01 Mole fraction of component 1 1.9913822100000E-04 Mole fraction of component 2 3.1266297400000E-11 Mole fraction of component 3 5.0020591340000E-02 Flow rate 9.9980086200000E-01 Mole fraction of component 1 1.9913822100000E-04 Mole fraction of component 2 3.1266297400000E-11 Mole fraction of component 3 9.4112606285675E+01 Molar mass 1.0397908456771E+03 Density 1.7971513265027E-04 Viscosity 1.4413615482844E-01 Thermal conductivity 2.2444893906833E+05 Heat capacity 2.3673409340847E-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 stagei"1w@N43w@I/Őw@"ڳx@& x@FRQKx@O:6Ax@qtNx@Sy@Q§RUz@^uz@Z|z@xz@=9TS{@ a6{@B,|@q@U|@q$ f|@X@Mm|@^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#@%4@<4@fr4@ z=4@M^n4@x\4@ k 3@V'FA1@L0@|zj0@S0@&0@@]0@Ozq1@0T+3@n<4@"K(u4@}E 5@C8z 5@(Liquid Flow profile4Liquid Flow at each stageE\cX%@ez6i"Q%@JuC%@S 0^)%@ҽV[$@,G$@j$"@_&@m=M@^vpW@nNW@>P@\7P@P@gj&LQ@zåxQ@}tnQ@rRҢQ@0#yQ@𭼢I@Duties profile*Duties at each stageA$)4-A4Vapour Moleweight profile@Vapour Moleweight at each stage [t W@b W@a| W@6qr W@0B W@_M W@> W@FW@=$W@0/W@:H3W@J4W@ =W@OW@fW@ȘwW@W@{W@nW@eW@.Vapour Density profile:Vapour Density at each stageY6@bHN&n5@`=[3@|}K0@!Q*@7j@"1@W]@E-ͭv@b @ҍ@1C @I-LN@w*R@&pn@L0@5W@Mn@k @c[@2Vapour Viscosity profile>Vapour Viscosity at each stage[ >eh>R>Sd>~t.>sA>3UZ >,<挅>ʨ[>҆i>B>vt>g֢xA>/>0qCK>" ~ͬ>ط9>A> d Z>_ά?>:Vapour Heat capacity profileFVapour Heat capacity at each stage`@:M `@Q`@ O`@W/'`@Zڊ`@:M a@C>٬da@`vOa@=,Ԛ/b@ r>b@H}Ab@ܵ|db@!lVb@M Ob@Vb@ $(~b@ZӼb@&Sb@xb@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stageYЃP?Q?CS?};/W?Foj^?Jsso? ^xNH?ez>g?JN7?iB?0}!8?qJ&#>?w^逖?U{"ɖ?Ĺ#^?k5w6ܖ?͖?ҦMIŖ?@–?e2?4Liquid Moleweight profile@Liquid Moleweight at each stageb W@ԕ W@ W@a W@ S" W@0W@8gDi!W@u<JW@eiW@"rW@[ɎtW@>tW@:X0yW@x $(~~W@zNz߂W@dW@8W@;W@:;%W@̒5W@.Liquid Density profile:Liquid Density at each stageC@C쎈@kw"@&S@\ Acƈ@4@@:M@d]KHՌ@X9H @Gz@5^I @&1@/$@Zd;@w1@p= W:@Q=@㥛Ġ>@/$?@l)?@2Liquid Viscosity profile>Liquid Viscosity at each stageG 4:.?K\u/?3&/?xi/?|/?UTӦ0?Go2?K(8?F ?9?IQk97?c16?4PQu6?d44? jp(1?Fc-?o̞C*?5z,x(?`'?@'??F<'?:Liquid Heat capacity profileFLiquid Heat capacity at each stageQlh@Tlh@ F%unh@ph@\Cwh@ÆWʌh@|Pkh@ڊ]i@K7j@&Slj@ÆWʄj@j@~jj@H.k@cZk@1*k@k@&Sl@ h"lx l@ec]l@:Liquid Thermal cond. profileFLiquid Thermal cond. at each stage|ԗ?4?!ا?sC庼?e0jۼ?)A+?Nx)? =j?r?\ں?uS?1Ղ?` ??cT9H?;u@m`?EOl?#ap?LZjr?:s?0Surface tension profile<Surface tension at each stage'ꎒ?0M*}?sE+?W'?UWp?g?sR? ﬔ?5Q/?k?z1俙?xƄ?E. ?"NHӕ?CrSC?&֘??N>?H{X?#GG?t3W@?>o=? 1 Converged 0 Iterations ChemSep (TM) - COL2 6.81 Copyright (c) 1988-2011 Harry Kooijman and Ross Taylor 2100 6 LITE free license Checking data file C:\Users\jasper\AppData\Local\Temp\CS_4_4~1.SEP Cape Open unit name: Recovery Cape-Open unit id: CS_4_4B4_1CC1AAE_C565D40 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 108-95-2 Phenol 108-88-3 Toluene 108-87-2 Methylcyclohexane Determining feed conditions Run level: Initialization Reading initial temperature profiles Reading initial composition profiles Init 31 milliseconds Run level: Complete model Iteration Error 0 -1.3895 Run level: Report Convergence obtained in 0 iterations Time 63 milliseconds FixMem driver done run time: 0.23 seconds Using: C:\Program Files (x86)\ChemSepL6v70\bin\co-col2.exe Using CAPE-OPEN version 1.0 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: 0.0014DR3not 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,@/@? @@ @?(@@(@@;@message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 383.80 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 383.80 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 383.87 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 383.87 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 383.97 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 383.97 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 384.17 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 384.17 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 384.56 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 384.56 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 385.46 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 385.46 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 388.11 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 388.11 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 397.39 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 397.39 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 413.34 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 413.34 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 421.33 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 421.33 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 423.37 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 423.37 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 423.80 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 423.80 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 429.17 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 429.17 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 437.25 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 437.25 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 445.39 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 445.39 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 450.77 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 450.77 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 453.37 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 453.37 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 454.43 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 454.43 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 454.83 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 454.83 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 454.98 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 454.98 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 420.87 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 420.87 K, range = [273.15 - 374.08] K) #(last 2 messages repeated 1 time) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 383.80 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 383.80 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 454.98 K, range = [178.18 - 383.78] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 454.98 K, range = [273.15 - 374.08] K) Solvent Makeup6Mixer - mix 2 or more inlet streams to a single outletk!^/E a-COUSCOUS0002Number of inletsNumber of inlet ports Pressure drop Pressure drop? _BThermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Last runD+++ specifications +++ Number of inlets: 2 Pressure drop: 0 Pa 5 $not all material ports are connectedInlet 1Inlet 2Outlet0@@@@@@@ @CoolerMHeaterCooler - heat or cool stream specifying heat duty or outlet temperaturez,wKJEKBCOUSCOUS0002TypeOperation type Temperature Heat duty Heat duty Temperature Energy inletOutlet temperatureOutlet temperature?Pw@r@ _B Heat duty Heat duty@?@RPsG)@x@xD Pressure drop Pressure drop? _BThermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Last run+++ specifications +++ Heat duty: -846115.724615978 W Pressure drop: 0 Pa +++ optional parameters +++ Outlet temperature: 373 K 66 : $not all material ports are connectedInletOutlet HmUd n?TTHmUd n?TTHmUd n?TTHmUd n?TT@@ ɿ@????@@@@@ɿ@@@MS Sans -C6?-C6?h㈵>-C6?,:P