Changeset 806 for branches/gui/eml/stage_separators/reboiler.mso
 Timestamp:
 Jul 28, 2009, 6:24:54 PM (13 years ago)
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 1 edited
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branches/gui/eml/stage_separators/reboiler.mso
r805 r806 183 183 Pdrop as press_delta (Brief="Pressure Drop in the reboiler", Symbol = "\Delta P"); 184 184 FlowConstant as Real (Brief = "Flow Constant"); 185 k as Real (Brief = "Flow Constant", Hidden = true, Unit='mol /J');185 k as Real (Brief = "Flow Constant", Hidden = true, Unit='mol^3/(kg*m^2)'); 186 186 187 187 SET 188 188 189 k = 1*'mol /J';189 k = 1*'mol^3/(kg*m^2)'; 190 190 191 191 VARIABLES … … 194 194 in InletQ as power (Brief="Heat Duty", PosX=1, PosY=0.08, Symbol="Q_{in}", Protected = true); 195 195 196 out TI as control_signal (Brief="Temperature Indicator of Reboiler", Protected = true, PosX=0.44, PosY=0); 197 out PI as control_signal (Brief="Pressure Indicator of Reboiler", Protected = true, PosX=0.35, PosY=0); 198 196 199 EQUATIONS 197 200 … … 208 211 OutletVapour.P = InletLiquid.P  Pdrop ; 209 212 210 "Fake Vapourisation Fraction" 211 OutletVapour.v = 0.6; 213 #"Fake Vapourisation Fraction" 214 # OutletVapour.v = 0.6; 215 212 216 "Fake output temperature" 213 OutletVapour.T = 300*'K';214 217 OutletVapour.T = (58+273)*'K'; 218 215 219 #OutletVapour.v = PP.VapourFraction(OutletVapour.T, OutletVapour.P, OutletVapour.z); 216 220 #OutletVapour.h = OutletVapor.v * PP.VapourEnthalpy(OutletVapour.T, OutletVapour.P, OutletVapour.z) 217 221 # + (1OutletVapor.v) * PP.LiquidEnthalpy(OutletVapour.T, OutletVapour.P, OutletVapour.z) 218 222 223 "Temperature indicator" 224 TI * 'K' = OutletVapour.T; 225 226 "Pressure indicator" 227 PI * 'atm' = OutletVapour.P; 228 219 229 "Flow through the reboiler" 220 OutletVapour.F = FlowConstant*k*InletQ;230 OutletVapour.F^3 = FlowConstant*k*InletQ; 221 231 222 232 end
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