FSD100MbP?h㈵>dkU*$@@@dfffffr@м@jl[xx temperaturepressure compositionflow e@l@E@`Y@@FLast runP2 `m@Z}@.@h@@FProfilesP  a@e@G@Q@@FLast runP C1_C2 (EOS)ڐ@'t+@-<-ethane production:0yE>MbP?MbP?MbP?%c:\werk\CO\COCO\bin\data\ChemSep1.pcdaEthyleneCH2CH2C2H474-85-1C=C pq@:SA?I ?p-e@Z@Z@`;_@ <@%?E?F=L@s?E,A A?QA AIA 8@ض@,=@ A 8 8 8IR@Z@@@)?¥q@@? 8 Y@q@i@O@ |[>@Z@q@etA_v?:`I@@dZ@q@j@3ϲ@L`;Q@@Nuu?$@Y@d@q@`Y\?zX@@3?p@@@ /&@N?bI@p@@?N_v78R@^@p@h`D! \r@ $̿@ٶ@`fY@@p@e}>߄?)xv@`f 8-e@@@fnȿ"[&ӿQl@>Y@q@)>_? y@ 8@e@ \w@fkg…m@@Ou?Z@@3q@"@&AR#? BUB@>I@@@d 8 8 8 8 8 8 84@@3y@`! 8 8-e@@3o@ ڊe@R ? 8 8`fY@@p@ N@aC@֡O.삿?5^ID>@`?@ ?@ ?]K?QJ@`d;? 8 8F??<̐?`Ɔ??D@%?`%pQ@`.h@`?@?PHydrogenH2H2 1333-74-0[H][H]JQ@@4A k??c4@`f+@`f+@4@ @@?˿b=@ y? A@@ 8Ӭ 8 8 8 8 8,@@ ?Q@@s? 8+@@ @@i*@-bXh?4?@(*@Q@@ej7AE @ @r`f+@ \O@@jb@+s`mjt=WA<`f+@@3s7@dW@`fQc@ ?+@@@%@`@ 4't?g@o@p@? $J@ j>ி`0@z@hC@tSX@ӫ@=i@+@@@e >0?s `@ 8`f+@@@fտg3`q8 S?.,+@?@ e??*@N? 8$@@fyj@? ]9>cD`f+@@ @@@I"@jH`> 8Y@@@ 8 8 8 8 8 8 8n2@Q(a@ H3? 8 8 4@#=@ jM#^SJ9 8 8+@@@ MSt?@HztbX9@@U0???@v? 8 8HͿ`r?_?@I?@Px?@z@@?B?@f(>@?@?^EthaneCH3CH3C2H674-84-0CCs@ЕRA?"?g@ V@ V@z?>@?`X?=8@`?EAp~ AEA 8@I`M9@ 8 8 8`f&7@`fV@ ??@s@ G? 8p-V@`s@iAM@@3ܥ`>@`fV@`s@efvA`ff?`[1@`QxV@Gs@j`m@@3IV@@Oۀ? \/@@3S@d`@`f?@))?p-V@ r@4@^E'@@K3?}b@p@(?@3N4`#@"[*\@@h/Xz@`?@`fV@r@e>`?g@ 8`fV@@@f鲿~[#@ё@k@gy¾`fV@r@ ? ?`f@덋 8g@@@fG!>@* `9Me?QxV@s@@@lgBO?B >I@@@d 8 8 8 8 8 8 8E4@@3@  8 8@3f@q@ @;j o? 8 8`fV@r@ NbX9/@̆(|x#?*Pz}>@?"?"?@>?+@ B? 8 8`0*??@t]??<,?zF@?)@)i@ ? B?MNitrogenN2N2 7727-37-9N#NJ̌_@IA ?~?`fVS@`O@`O@t@<@`֡??=@-?d6A``A%A 8 \B@ۮ 8 8 8`f4@@3O@@z@@r?G_@`;? 8@3O@࣐_@iBD@|@??@ gN@࣐_@e"zAY5@ 33@+@3O@࣐_@jHnA]@`-'``?@%5@`f @ 8@3O@Ȟ@f˿$@ u7?&eN@_@`?6?@^?@3@@^r@ 8I@@@f@d5X@Ֆ3?`7@3O@̌_@@@`]\AC? P`>4AI@@@d 8 8 8 8 8 8 8zt4@V@@ 8 8S@ ;\@ \@Cqd? 8 8@3O@@_@ QkwjA@R빍bX9@?rh?rh?= ?`@`? 8 8ZT?`?@"???2@`֡?lD @֜W@0?`?bubblePointTemperaturebubblePointTemperaturedensitydensitydensity/volume (pure)density/volume (pure)dewPointTemperaturedewPointTemperature enthalpyenthalpy enthalpyF enthalpyFentropyentropy!entropyFentropyFfugacityfugacityfugacityCoefficientfugacityCoefficient heatCapacityheatCapacityCpKK logFugacityCoefficientlogFugacityCoefficientsurfaceTensionsurfaceTensionsurfaceTension (pure)surfaceTension (pure)thermalConductivitythermalConductivity04thermalConductivity (pure)thermalConductivity (pure))1 viscosity viscosity& viscosity (pure)viscosity (pure)" volumevolumeVapor Vapor phaseLiquid Liquid phase   T8m4?'Hydrogen/Ethylene T=123.15-248.15K p229imported from PR.IPDtF_?)Ethylene/C2 T=200-255K P=2.2-26.7bar p503imported from PR.IPD'?Nitrogen/Ethylene p298imported from PR.IPD8m4?'Hydrogen/Ethylene T=123.15-248.15K p229imported from PR.IPDݓZ!Hydrogen/C2 T=149.61-189.57K p233imported from PR.IPD߾3? Hydrogen/Nitrogen T=90-113K p210imported from PR.IPDtF_?)Ethylene/C2 T=200-255K P=2.2-26.7bar p503imported from PR.IPDݓZ!Hydrogen/C2 T=149.61-189.57K p233imported from PR.IPD"u?Nitrogen/C2 T=200-290K p300imported from PR.IPD'?Nitrogen/Ethylene p298imported from PR.IPD߾3? Hydrogen/Nitrogen T=90-113K p210imported from PR.IPD"u?Nitrogen/C2 T=200-290K p300imported from PR.IPD  aCH2CH3ͪ?A`"? rh.@CH2M O?HzG?Zd;O ,@aCH2CH3ͪ?A`"? rh.@CH2M O?HzG?Zd;O ,@ V瞯<ethane productionethane productionbKrx-WSethane production0c:\werk\CO\COCO\bin\data\DefaultComponentLib.pcdEthane74-84-0EthaneC2H6>@Ethylene74-85-1EthyleneC2H4 <@Hydrogen 1333-74-0HydrogenH2 @ Ethane prodVapor$4.16667e-006*C(Ethylene)*C(Hydrogen)-136330?؀My>Pethane production74-84-0Ethane>@g@C2H6ethane productionEthane74-85-1Ethylene <@p-e@C2H4ethane productionEthylene 1333-74-0Hydrogen @c4@H2ethane productionHydrogen 7727-37-9Nitrogen<@`fVS@N2ethane productionNitrogen ????????????thermalConductivity.Dmoles?? / molenthalpyF.DmolFraction??viscosity.Dtemperature????enthalpyF.Dpressure??thermalConductivity.Dpressure?? thermalConductivity.Dtemperature??heatCapacity.DmolFraction??entropyF.Dmoles??density.Dpressure?@?@enthalpy.Dmoles??#logFugacityCoefficient.DmolFractionentropy.Dtemperature??viscosity.Dmoles???? / mol volume.Dmoles@@@@enthalpy?? enthalpyF??fugacity.Dtemperature??volume.Dpressure@@@@surfaceTension.DmolFraction??fugacityCoefficient.Dmoles / molenthalpy.DmolFraction??enthalpy.Dpressure??logFugacityCoefficientfugacity.Dpressure fugacityCoefficient.DmolFractionvolume.DmolFraction@@@@density?@?@enthalpyF.Dtemperature??entropyF.DmolFraction??thermalConductivity??surfaceTension.Dtemperature??surfaceTension??density.DmolFraction?@?@heatCapacity.Dtemperature??#logFugacityCoefficient.Dtemperatureviscosity.DmolFraction????fugacityCoefficient.DpressuresurfaceTension.Dmoles?? / molenthalpy.Dtemperature??entropy.Dpressure??density.Dmoles?@?@ / mol thermalConductivity.DmolFraction??logFugacityCoefficient.Dmoles / molenthalpyF.Dmoles??surfaceTension.Dpressure??entropy.DmolFraction??entropyF.Dtemperature??entropyF??volume@@@@entropy??heatCapacity.Dpressure??fugacityCoefficient logFugacityCoefficient.Dpressureviscosity.Dpressure?? heatCapacity??entropy.Dmoles?? fugacityCoefficient.DtemperatureentropyF.Dpressure?? viscosity????volume.Dtemperature@@@@fugacity.Dmoles?? / moldensity.Dtemperature?@?@heatCapacity.Dmoles??@ &{776B42B7-D0E5-4C4B-87E8-E1C4AAD38C32} Pressure drop?? Temperature?? Heat duty??Reactor volume@@@@ Catalyst mass??Catalyst volume@@@@Catalyst density@?@?TotalMassBalancePropertiesFraction?? TotalFlowMass??TotalFlowEnthalpy??&{FCC17C95-0B2E-4946-B873-A35B10C4B6E1} Pressure drop?? Temperature?? Heat duty??&{603DF4B9-4F88-475D-A458-85F56125DA70} Pressure drop?? Temperature?? Heat duty??ReactionPackagePropertiesrate-homogeneous?@?@&{43312205-B251-4EEB-B585-4D82BB019C56}%Length??Diameter?? Roughness?? Temperature?? Heat duty??Catalyst loading@?@?Catalyst particle diameter??Wall heat transfer coefficient??Ambient Temperature??Heating/cooling tube diameter??Tube heat transfer coefficient?? Heating/Cooling tube temperature??Position?? Ethane flow?? Ethylene flow?? Hydrogen flow??Pressure?? Total flow??Density?@?@ Viscosity??Superficial velocity??Rate Ethane prod?@?@ EnthalpyF??Ethane flow profile??Ethylene flow profile??Hydrogen flow profile??Temperature profile??Pressure profile??Total flow profile??Density profile?@?@Viscosity profile????Superficial velocity profile??Ethane prod rate profile?@?@EnthalpyF profile??Enthalpy profile?? Tolerance??Catalyst porosity??&{EF130956-4BC7-49EB-8B04-65965125EA19} streamParams#Component mole flow(Ethane)@kg1@s-1??$Component mole flow(Ethane)@s-1@mol1??&Component mole flow(Ethylene)@s-1@mol1?? Length@m1??Mole flow@s-1@mol1??&{708D633D-65E6-4C80-9C7F-55206BD6F1C4}COFE_ControllerCOFE_FlowConstraint Mole flow?? Mass flow??&{5E216BDD-C82F-45FE-830C-61FDDD2D9BC7} Pressure drop??EbubblePointTemperaturedensitydensity.Dmolesdensity.DmolFractiondensity.Dpressuredensity.DtemperaturedewPointTemperatureenthalpyenthalpy.Dmolesenthalpy.DmolFractionenthalpy.Dpressureenthalpy.Dtemperatureentropyentropy.Dmolesentropy.DmolFractionentropy.Dpressureentropy.Dtemperaturefugacityfugacity.Dmolesfugacity.DmolFractionfugacity.Dpressurefugacity.DtemperaturefugacityCoefficientfugacityCoefficient.Dmoles fugacityCoefficient.DmolFractionfugacityCoefficient.Dpressure fugacityCoefficient.Dtemperature heatCapacityheatCapacity.DmolesheatCapacity.DmolFractionheatCapacity.DpressureheatCapacity.DtemperaturelogFugacityCoefficientlogFugacityCoefficient.Dmoles#logFugacityCoefficient.DmolFraction logFugacityCoefficient.Dpressure#logFugacityCoefficient.DtemperaturesurfaceTensionsurfaceTension.DmolessurfaceTension.DmolFractionsurfaceTension.DpressuresurfaceTension.DtemperaturethermalConductivitythermalConductivity.Dmoles thermalConductivity.DmolFractionthermalConductivity.Dpressure thermalConductivity.Dtemperature viscosityviscosity.Dmolesviscosity.DmolFractionviscosity.Dpressureviscosity.Dtemperaturevolume volume.Dmolesvolume.DmolFractionvolume.Dpressurevolume.DtemperaturebubblePointPressuredewPointPressure enthalpyFenthalpyF.DmolesenthalpyF.DmolFractionenthalpyF.DpressureenthalpyF.DtemperatureentropyFentropyF.DmolesentropyF.DmolFractionentropyF.DpressureentropyF.DtemperatureVaporethane productionVaporLiquidethane productionLiquid VaporLiquiddefaultdefault material templateethane production r feed default`6A@tŌr@W׊?:5``6ARr@`!u`?=Tde`6ARr@`!u`?=Tde-C6?|=?Report Intervals$Number of slices for output profilesd Packed bedReactor has catalyst packingCatalyst loading Catalyst mass per reactor volume@?חACatalyst porosity'Relative void space of catalyst packingffffff?ffffff??Catalyst particle diameter,Particle diameter for catalyst pressure drop?MbP?MbP?|=?Wall heat transfer coefficient?Heat transfer coefficient for heat transfer to the reactor wall?@Y@ _BAmbient Temperature9Ambient temperature for heat transfer to the reactor wall?fffffr@fffffr@ _BNumber of heating/cooling tubesNumber of heating/cooling tubes'Heating/cooling tube diameter<Tube diameter for heat transfer to the heating/cooling tubes? F%u? F%u?|= _BTube heat transfer coefficientHHeat transfer coefficient for heat transfer to the heating/cooling tubes?@ _B Heating/Cooling tube temperature:Temperature for heat transfer to the heating/cooling tubes?fffffx@fffffx@ _B Ethane prod PositionPosition along the reactor?e??433333???433333?gfffff?????433333??gfffff???433333??gfffff????gfffff?433333????gfffff?433333????gfffff?433333????gfffff?433333??gfffff??333333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333??@333333@gfffff@@@@333333@gfffff@@@@333333@gfffff@@@@433333@gfffff@@@@Ethane flow profile%Ethane flow profile along the reactor?e|m8?aEGG?6/ nQ?HڲV?Wu[?.IO`?D/b?;Źd?7rg?6li?㸑 k?۴ xl?ZӼn?H;p?ʛlq?+Cq?2ܛr?3RUs?)Zt?(?t?{"Su?ꊀu?dbZv?-ڿw?1nw?Hԓx?wQيx?=y?dQy?˚ly?| y#[z?$Yz?Ȝ {?P}{?!X{?,|?D~|?k~|? }?&b}?ܨ}? .[}?VU-~?âk~?S!~?aQ 2~?QBT$?q~P?4sN#?@E6Y?'h?e ?h n!?;H7?=ΎgL? h~`?kt?7"f?zDD? 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W?juW?yW?-M:V?.aBvV?ԄA%V?O"U?REU?t<|?U?8t7T?^T?4iT?/*+&T?pS?}S?Iǵ_dS?s!&S?zR?Gs1kR?tvR?\,=R?t3LpR?H/Q?F|L Q?ŀ yiQ? 6Q?Temperature profile%Temperature profile along the reactor?e@tŌr@p(Is@s@(6s@}#s@JF@Zs@޴s@Czs@js@jts@,Vs@As@ޙ˳'ws@RFns@ϥZes@x\s@Ts@‡-Ms@uX{fEs@u >s@kd7s@WM}1s@5Q+s@NWj%s@ us@S_es@SeFs@wohs@4@ s@0Zs@] s@F5r@CEr@6r@gl*r@r@ =r@ r@I#r@35r@Nr@UU+r@x-r@+qr@czr@Qsr@%r@ݮkr@]Sr@y&;r@֯r@9mr@= r@`6A`6A`6A~`6A?`6A`6A`6A`6AC`6A`6A`6A`6AH`6A `6A`6A`6AO`6A`6A`6A`6AX`6A`6A`6A`6Ab`6A%`6A`6A`6An`6A1`6A`6A`6Az`6A>`6ATotal flow profile$Total flow profile along the reactor?eW׊?'?˘? )s?_L/?QΗ?#v?Q6?ִ??"?*_h?N])?-SI?f=?$F{?ֱF?*tV?̚?WZK?́%?&^?*6?3?0V?gƓ?`z ?Gx?2??n:? i?շu?\?f6ܐ?b3I֐?`KА?Xʐ?}jĐ?I?W$? \˴?&D-?7ժ?㈎ ?Q\G^? RϜ?]?!?2ɏ?n)X??\/??|?%3+ax?OΫ!t?DFq?фm?[{%zj?K$e0g?c?`!u`?Density profile!Density profile along the reactor@?e7:T@-{7 @pWT@ =@iν{e@zk ́@meځ@v@vr@G{@ >R{>_]v>Nqr^>Z;/F>S d.>5>Z>1>hP>4>*TI>+g>"nsf>@q>/^5_>QN>>>->`m~> j>C;J>&><@C>F>H>>&K>P>N >'>z㗍>8l>{>jft1s>7|fk>&JM[c>d[>TIbT> }M>IG>u@>s<:>Dj5>>Ҧj/>:g{=*>g$>dѢ>_51>0a>ضEL>̢ >HZ{ >Ȯ)>p>AJ>,Hc>p#&>>*>Yc>(H>#G>_>.&>V>V=8>(P>N`/7>eiD>ן>sH>E>|D>z>M>jI>o- >ߵ ->Ro[>u>xj> hu5>ZLf/>܉[> y>ȷI>>>Ξ>Ia>n;>!˱>Mg>KU>r~&> >ޫ>Ū>(7%>8e>|W>Rٞ>Superficial velocity profile.Superficial velocity profile along the reactor?e j C??k].D?adC?Kt~C?MX?;~>?5ִ6>?,8o8E=?"7=?)S'q=?|#5=?:2Tx7?Ph7?)7?Od'7? }7?%7?7?by]7?_s7?)Wo7?[27?$G7?R[;"7?LmM7?w7?D7?Ethane prod rate profile*Ethane prod rate profile along the reactor@?e"4e?[iX? -":?*??jg? ?WBܓ0?[2\?A$h?'L?TBd ?P?KG=?lM?@?C!c?)Q 4?e?AqS?0p]?/??ah?@?oln?I]ݥ?(J?,-d0?p ? $̋?bT耬?-YU?_8?;ە(?L%&?hH/?S2jYeE?Hf?&o?ҕǣ?:Q?ᶭ9N?a9?}E?ٕX? T}b.?U`?_?;d J?o[1OB?א F?nU?on??5BG'?ܫ?':ն:6?upZ}?[Poo\͔? D$?mJI??Җ R?H1YÑ?ΰT:?5ݶ?>=8?trA~?啎??eη־ތ?s=b?!tH?bQ?~n!Љ?bR?ݳs?~͇?Υz.?hz*?+`?5,r?L&D?goc?U^R?wKe?.Jq?o6ɰy?Btt ?㜁?6:3?&S΀?{k?/3 ?}C_??+~? }?KEW}? |?C?|?T-~{?Enthalpy profile"Enthalpy profile along the reactor@?eS2#lJu@y]*m@Ii@zoZ~@d*|@'9jz@Ax@"x35w@x~u@:րs@I)r@Wp@i$vm@j@c$g@TZd@ Ȳw*b@X^@vJY@LplT@?QN@xCQE@N8@[W@ [/V&p*ۖ;OEuM9ىRj= VEYzϰ\J `Ɣao: c;wdw'lno\[,oTrp@[bpfRqR+Tqe!r#lȃrc5Rr?=sj ss;Rs;b2-C6?rX#Parameter Plot ~ϯ?e+?ArialArialArial{hs@SZ@??SZ@m ??z5@vJz?|Gzt?MbP?vJz?mol / s ??zem[4@ϰor@ZMt@@?ϰor@ZMt@pr@pr@K ??z@}%??|Gz?}%? mol / m s ?@?@4Reactor / Ethane flow profile vs. Reactor / Position@pkT?e??433333???433333?gfffff?????433333??gfffff???433333??gfffff????gfffff?433333????gfffff?433333????gfffff?433333????gfffff?433333??gfffff??333333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333??@333333@gfffff@@@@333333@gfffff@@@@333333@gfffff@@@@433333@gfffff@@@@|m8?aEGG?6/ nQ?HڲV?Wu[?.IO`?D/b?;Źd?7rg?6li?㸑 k?۴ xl?ZӼn?H;p?ʛlq?+Cq?2ܛr?3RUs?)Zt?(?t?{"Su?ꊀu?dbZv?-ڿw?1nw?Hԓx?wQيx?=y?dQy?˚ly?| y#[z?$Yz?Ȝ {?P}{?!X{?,|?D~|?k~|? }?&b}?ܨ}? .[}?VU-~?âk~?S!~?aQ 2~?QBT$?q~P?4sN#?@E6Y?'h?e ?h n!?;H7?=ΎgL? h~`?kt?7"f?zDD? BP?nCy]?i?|pLzu?c?D63?׮?nd?w?%V/?S ?,jɁ?xҁ?z ܁?W8?홓?H?u_?eq?PU?c ?t?GZ$?Vm,?y(#3?9:?ve@?dNG?cM?pkT?PositionEthane flow profile6Reactor / Ethylene flow profile vs. Reactor / Position@1JP?)]]?e??433333???433333?gfffff?????433333??gfffff???433333??gfffff????gfffff?433333????gfffff?433333????gfffff?433333????gfffff?433333??gfffff??333333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333???gfffff??433333??@333333@gfffff@@@@333333@gfffff@@@@333333@gfffff@@@@433333@gfffff@@@@)]]?h,<ޕ?}S ߂?L!#h/?s?r ?chaI?$0h?ݕ^J~? B7}?0|?u4{?:ANqCz?{ETQ\y?Ax?މNw?}nv?`kv?+3Wieu?.(0t? *K t?-gs?,r?D;a7r?{mq?w q?ܚ'p?10!p?m Ro?qmn?*n;֑m?W8l"0l? M=k?,ۇ3k?ĩ|yj? 5gi?9s@kd7s@WM}1s@5Q+s@NWj%s@ us@S_es@SeFs@wohs@4@ s@0Zs@] s@F5r@CEr@6r@gl*r@r@ =r@ r@I#r@35r@Nr@UU+r@x-r@+qr@czr@Qsr@%r@ݮkr@]Sr@y&;r@֯r@9mr@= r@=8?trA~?啎??eη־ތ?s=b?!tH?bQ?~n!Љ?bR?ݳs?~͇?Υz.?hz*?+`?5,r?L&D?goc?U^R?wKe?.Jq?o6ɰy?Btt ?㜁?6:3?&S΀?{k?/3 ?}C_??+~? }?KEW}? |?C?|?T-~{?PositionEthane prod rate profile