Changeset 627 for branches/gui/eml
- Timestamp:
- Sep 19, 2008, 5:23:01 PM (14 years ago)
- Location:
- branches/gui/eml/stage_separators
- Files:
-
- 2 edited
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/stage_separators/columnTeste.mso
r624 r627 71 71 SpecialTrayIndex(NumberOfTrays) as Integer (Brief="Number of trays", Default=0,Hidden=true); 72 72 FeedTrayLocation as Integer (Brief="Feed tray Location", Default=2); 73 topdown as Integer (Brief="Trays counting (1=top-down, -1=bottom-up)", Default=1,Hidden=true);74 top as Integer (Brief="Number of top tray",Hidden=true);75 bot as Integer (Brief="Number of bottom tray",Hidden=true);76 73 g as acceleration (Brief="Gravity Acceleration",Default=9.81,Hidden=true); 77 74 Mw(NComp) as molweight (Brief="Component Mol Weight",Hidden=true); … … 110 107 111 108 SET 112 top = (NumberOfTrays-1)*(1-topdown)/2+1;113 bot = NumberOfTrays/top;114 109 SpecialTrayIndex(FeedTrayLocation) =1; 115 110 Mw = PP.MolecularWeight(); … … 141 136 VapourConnector as stream (Brief="Vapour connection at the middle trays", PosX=0.55, PosY=0,Hidden=true); 142 137 138 MurphreeEff as Real (Brief = "Murphree efficiency"); 139 143 140 CONNECTIONS 144 141 145 trays([ top+topdown:topdown:bot]).OutletV to trays([top:topdown:bot-topdown]).InletV;146 trays([ top:topdown:bot-topdown]).OutletL to trays([top+topdown:topdown:bot]).InletL;142 trays([2:NumberOfTrays]).OutletV to trays([1:NumberOfTrays-1]).InletV; 143 trays([1:NumberOfTrays-1]).OutletL to trays([2:NumberOfTrays]).InletL; 147 144 148 145 LiquidConnector to trays(1).InletL; … … 184 181 185 182 for i in [1:NumberOfTrays] do 183 184 "Murphree Efficiency" 185 trays(i).OutletV.z = MurphreeEff * (trays(i).yideal - trays(i).InletV.z) + trays(i).InletV.z; 186 186 187 187 "Level of clear liquid over the weir" -
branches/gui/eml/stage_separators/trayTeste.mso
r615 r627 57 57 Level as length (Brief="Height of clear liquid on plate"); 58 58 yideal(NComp) as fraction; 59 Emv as Real (Brief = "Murphree efficiency");59 60 60 61 61 EQUATIONS … … 78 78 "Chemical Equilibrium" 79 79 PP.LiquidFugacityCoefficient(OutletL.T, OutletL.P, OutletL.z)*OutletL.z = PP.VapourFugacityCoefficient(OutletV.T, OutletV.P, yideal)*yideal; 80 81 "Murphree Efficiency"82 OutletV.z = Emv * (yideal - InletV.z) + InletV.z;83 80 84 81 "Thermal Equilibrium"
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