Changeset 519
 Timestamp:
 May 20, 2008, 11:54:40 AM (15 years ago)
 Location:
 branches/rate
 Files:

 2 edited
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 Unmodified
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branches/rate/eml/stage_separators/tray.mso
r517 r519 483 483 Pallete = false; 484 484 Icon = "icon/Tray"; 485 Brief = " Basic equations of a tray column model.";485 Brief = "Descrition of variables of the equilibrium interface."; 486 486 Info = 487 "This model contains only the main equations of a column tray nonequilibrium model without 488 the hidraulic equations."; 487 "This model contains only the variables of the equilibrium interface."; 489 488 490 489 PARAMETERS … … 568 567 "Component Molar Balance" 569 568 diff(M_liq)=Inlet.F*Inlet.z + InletL.F*InletL.z 570  OutletL.F*OutletL.z + interf.NL ;569  OutletL.F*OutletL.z + interf.NL*interf.x; 571 570 572 571 diff(M_vap)=InletFV.F*InletFV.z + InletV.F*InletV.z 573  OutletV.F*OutletV.z  interf.NV ;572  OutletV.F*OutletV.z  interf.NV*interf.y; 574 573 575 574 "Energy Balance" 
branches/rate/sample/stage_separators/sample_tray.mso
r517 r519 255 255 inL.P = 150 * 'kPa'; 256 256 inL.T = 290 * 'K'; 257 inL.F = 62* 'kmol/h';257 inL.F = 90 * 'kmol/h'; 258 258 inL.z = [0.1641, 0.8359]; 259 259 260 260 inV.P = 150 * 'kPa'; 261 inV.T = 340 * 'K';261 inV.T = 500 * 'K'; 262 262 inV.z = [0.0584, 0.9416]; 263 263 # inV.F = 62 * 'kmol/h'; … … 265 265 t1.OutletV.F = 120 * 'kmol/h'; 266 266 # t1.OutletL.F = 120 * 'kmol/h'; 267 t1.interf.a = 140 * 'm^2';267 t1.interf.a = 40 * 'm^2'; 268 268 t1.interf.htL = 10.01 * 'kW/m^2/K'; 269 269 t1.interf.htV = 0.025 * 'kW/m^2/K';
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