Changeset 873 for branches/gui/eml/stage_separators/tray.mso
- Timestamp:
- Oct 29, 2009, 3:47:18 PM (13 years ago)
- File:
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- 1 edited
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branches/gui/eml/stage_separators/tray.mso
r866 r873 321 321 322 322 miL as viscosity (Brief="Liquid dynamic viscosity", DisplayUnit='kg/m/s'); 323 # miV as viscosity (Brief="Vapor dynamic viscosity", DisplayUnit='kg/m/s');324 323 rhoL as dens_mass; 325 324 rhoV as dens_mass; … … 329 328 uL as velocity (Brief="volume flow rate of liquid, m^3/m^2/s", Lower=-10, Upper=1000); 330 329 uV as velocity (Brief="volume flow rate of vapor, m^3/m^2/s", Lower=-10, Upper=1000); 331 #dp as length (Brief="Particle diameter", Default=1e-3, Lower=0, Upper=10);332 #invK as positive (Brief="Wall factor", Default=1, Upper=10);333 #Rev as Real (Brief="Reynolds number of the vapor stream", Default=4000);334 330 Al as area (Brief="Area occupied by the liquid", Default=0.001, Upper=10); 335 331 hl as positive (Brief="Column holdup", Unit='m^3/m^3', Default=0.01,Upper=10); … … 346 342 M = ML*OutletLiquid.z + MV*OutletVapour.z; 347 343 348 "Mol fraction normalisation"344 "Mol Fraction Normalisation" 349 345 sum(OutletLiquid.z)= 1.0; 346 347 "Mol Fraction Constraint" 350 348 sum(OutletLiquid.z)= sum(OutletVapour.z); 351 349 … … 374 372 miL = PP.LiquidViscosity(OutletLiquid.T, OutletLiquid.P, OutletLiquid.z); 375 373 376 #"Vapour viscosity"377 # miV = PP.VapourViscosity(InletVapour.T, InletVapour.P, InletVapour.z);378 379 374 "Volume flow rate of liquid, m^3/m^2/s" 380 375 uL * Al = OutletLiquid.F * vL; 381 376 377 "Pressure Drop" 382 378 deltaP = InletVapour.P - OutletVapour.P; 383 379 384 380 end 385 381
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