Changeset 496 for branches/packed
- Timestamp:
- Apr 9, 2008, 4:42:26 PM (15 years ago)
- Location:
- branches/packed/eml
- Files:
-
- 2 added
- 2 edited
Legend:
- Unmodified
- Added
- Removed
-
branches/packed/eml/stage_separators/PackedStage.mso
r495 r496 33 33 out OutletV as vapour_stream (Brief="Outlet vapour stream", PosX=0.8043, PosY=0, Symbol="_{outV}"); 34 34 35 M(NComp) as mol (Brief="Molar Holdup in the tray" );36 ML as mol (Brief="Molar liquid holdup" );37 MV as mol (Brief="Molar vapour holdup" );38 E as energy (Brief="Total Energy Holdup on tray" );39 vL as volume_mol (Brief="Liquid Molar Volume" );40 vV as volume_mol (Brief="Vapour Molar volume" );35 M(NComp) as mol (Brief="Molar Holdup in the tray", Default=0.01, Lower=0, Upper=100); 36 ML as mol (Brief="Molar liquid holdup", Default=0.01, Lower=0, Upper=100); 37 MV as mol (Brief="Molar vapour holdup", Default=0.01, Lower=0, Upper=100); 38 E as energy (Brief="Total Energy Holdup on tray", Default=-500); 39 vL as volume_mol (Brief="Liquid Molar Volume", Lower=0); 40 vV as volume_mol (Brief="Vapour Molar volume", Lower=0); 41 41 42 42 miL as viscosity (Brief="Liquid dynamic viscosity", DisplayUnit='kg/m/s'); … … 47 47 # miw as viscosity (Brief="Water viscosity"); 48 48 49 uL as velocity (Brief="volume flow rate of liquid, m^3/m^2/s", Lower = -10, Default = 0.007);50 uV as velocity (Brief="volume flow rate of vapor, m^3/m^2/s", Lower = -10, Default = 1.14);51 dp as length (Brief="Particle diameter", Default=1e-3 );52 invK as Real(Brief="Wall factor");53 Rev as Real (Brief="Reynolds number of the vapor stream", Lower = 0,Default=100);49 uL as velocity (Brief="volume flow rate of liquid, m^3/m^2/s", Lower=-10, Upper=100); 50 uV as velocity (Brief="volume flow rate of vapor, m^3/m^2/s", Lower=-10, Upper=100); 51 dp as length (Brief="Particle diameter", Default=1e-3, Lower=0, Upper=10); 52 invK as positive (Brief="Wall factor"); 53 Rev as Real (Brief="Reynolds number of the vapor stream", Default=100); 54 54 Al as area; 55 55 hl as Real (Brief="Column holdup", Unit='m^3/m^3'); … … 151 151 "Liquid holdup" 152 152 hl = (12*miL*a^2*uL/rhoL/g)^1/3; 153 154 155 153 #* 156 154 "Liquid holdup at the loading point" … … 232 230 inV.z = [0.0584, 0.9416];#[0.5, 0.5];# 233 231 234 t1.OutletV.F = 147.1 * 'kmol/h';235 #t1.deltaP = 0.05* 'atm';232 #t1.OutletV.F = 180.1 * 'kmol/h'; 233 t1.deltaP = 0.00189536 * 'atm'; 236 234 t1.Qsil = 1; 237 235 … … 248 246 249 247 INITIAL 250 t1.OutletL.T = 3 15*'K';251 t1.ML = 0. 25* 'kmol';252 t1.OutletL.z(1) = 0.1 641;248 t1.OutletL.T = 340 *'K';#347.54 *'K'; 249 t1.ML = 0.02 * 'kmol';#0.0131283 * 'kmol'; 250 t1.OutletL.z(1) = 0.1;#0.112595; 253 251 254 252 OPTIONS 253 #InitialFile = "packedStage_Test_1"; 255 254 DAESolver(File="sundials"); 256 255 TimeStep = 10; … … 309 308 310 309 #t1.OutletV.P = 2.30409 * 'atm'; 311 t1.OutletV.F = 165 * 'kmol/h';312 #t1.deltaP = 0.0026* 'atm';310 #t1.OutletV.F = 165 * 'kmol/h'; 311 t1.deltaP = 0.0214961 * 'atm'; 313 312 t1.Qsil = 10; 314 313 … … 326 325 327 326 INITIAL 328 t1.OutletL.T = 290*'K';329 t1.ML = 0.00 2* 'kmol';330 t1.OutletL.z([1:4]) = [0. 226, 0.425, 0.035, 0.025];327 t1.OutletL.T = 305.912 *'K'; 328 t1.ML = 0.00327166 * 'kmol'; 329 t1.OutletL.z([1:4]) = [0.169668, 0.511287, 0.0321714, 0.046279]; 331 330 332 331 OPTIONS 333 332 DAESolver(File="sundials"); 334 #InitialFile = " /home/paula/tray_Test_2.rlt";333 #InitialFile = "packedStage_Test_2"; 335 334 TimeStep = 10; 336 335 TimeEnd = 100; -
branches/packed/eml/streams.mso
r352 r496 35 35 36 36 VARIABLES 37 F as flow_mol (Brief = "Stream Molar Flow Rate" );37 F as flow_mol (Brief = "Stream Molar Flow Rate", Lower=-1e2); 38 38 T as temperature (Brief = "Stream Temperature"); 39 39 P as pressure (Brief = "Stream Pressure");
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