Changeset 634
- Timestamp:
- Sep 23, 2008, 9:42:24 PM (14 years ago)
- Location:
- trunk/sample
- Files:
-
- 7 edited
Legend:
- Unmodified
- Added
- Removed
-
trunk/sample/controllers/Sample_flash_pid.mso
r537 r634 120 120 EQUATIONS 121 121 #Feed stream 122 s1. Outlet.z= [0.3, 0.3, 0.4];123 s1. Outlet.P = 5 * 'atm';122 s1.Composition = [0.3, 0.3, 0.4]; 123 s1.P = 5 * 'atm'; 124 124 125 125 #Disturbance 126 126 if time < 0.5*'h' then 127 s1. Outlet.T = 338 * 'K';128 s1. Outlet.F = 496.3 * 'kmol/h';127 s1.T = 338 * 'K'; 128 s1.F = 496.3 * 'kmol/h'; 129 129 else 130 s1. Outlet.T = 360 * 'K';131 s1. Outlet.F = 450 * 'kmol/h';130 s1.T = 360 * 'K'; 131 s1.F = 450 * 'kmol/h'; 132 132 end 133 133 -
trunk/sample/controllers/sample_PIDIncr_MIMO.mso
r530 r634 243 243 244 244 if time < 1 * 'h' then 245 feed. Outlet.F = 113.4 * 'kmol/h';245 feed.F = 113.4 * 'kmol/h'; 246 246 else 247 feed. Outlet.F = 120 * 'kmol/h';247 feed.F = 120 * 'kmol/h'; 248 248 end 249 249 250 250 SPECIFY 251 feed. Outlet.T = 290 * 'K';252 feed. Outlet.P = 6 * 'bar';253 feed. Outlet.z= 1/NComp;251 feed.T = 290 * 'K'; 252 feed.P = 6 * 'bar'; 253 feed.Composition = 1/NComp; 254 254 255 255 zero.F = 0 * 'kmol/h'; -
trunk/sample/controllers/sample_PID_MIMO.mso
r530 r634 244 244 245 245 if time < 1 * 'h' then 246 feed. Outlet.F = 113.4 * 'kmol/h';246 feed.F = 113.4 * 'kmol/h'; 247 247 else 248 feed. Outlet.F = 120 * 'kmol/h';248 feed.F = 120 * 'kmol/h'; 249 249 end 250 250 251 251 SPECIFY 252 feed. Outlet.T = 291 * 'K';253 feed. Outlet.P = 568.3 * 'kPa';254 feed. Outlet.z= 1/NComp;252 feed.T = 291 * 'K'; 253 feed.P = 568.3 * 'kPa'; 254 feed.Composition= 1/NComp; 255 255 256 256 zero.F = 0 * 'kmol/h'; -
trunk/sample/miscellaneous/sample_streams.mso
r218 r634 70 70 71 71 SPECIFY 72 sl. Outlet.F = 10 * 'kmol/h';73 sl. Outlet.T = 300 * 'K';74 sl. Outlet.P = 100 * 'kPa';75 sl. Outlet.z= [0.24596, 0.370278, 0.383762];76 # sl.Outlet.v = 0.0; #liquid stream 72 sl.F = 10 * 'kmol/h'; 73 sl.T = 300 * 'K'; 74 sl.P = 100 * 'kPa'; 75 sl.Composition= [0.24596, 0.370278, 0.383762]; 76 77 77 78 78 79 sv. Outlet.F = 10 * 'kmol/h';79 sv.F = 10 * 'kmol/h'; 80 80 #sv.Outlet.h = 20248 * 'J/mol'; 81 sv. Outlet.T = 300 * 'K';82 sv. Outlet.P = 100 * 'kPa';81 sv.T = 300 * 'K'; 82 sv.P = 100 * 'kPa'; 83 83 #sv.Outlet.z = [0.824212, 0.12577, 0.0500176]; 84 84 # sv.Outlet.v = 1.0; #vapor stream … … 86 86 EQUATIONS 87 87 "Liquid-Vapour equilibrium" 88 PP.VapourFugacityCoefficient(sv.Outlet.T, sv.Outlet.P, sv. Outlet.z) * sv.Outlet.z=89 PP.LiquidFugacityCoefficient(sl.Outlet.T, sl.Outlet.P, sl. Outlet.z) * sl.Outlet.z;88 PP.VapourFugacityCoefficient(sv.Outlet.T, sv.Outlet.P, sv.Composition) * sv.Composition = 89 PP.LiquidFugacityCoefficient(sl.Outlet.T, sl.Outlet.P, sl.Composition) * sl.Composition; 90 90 91 91 OPTIONS -
trunk/sample/reactors/sample_cstr.mso
r245 r634 54 54 55 55 SPECIFY 56 s1. Outlet.F = 52126 * 'mol/h';57 s1. Outlet.P = 1 * 'atm';58 s1. Outlet.T = 534.67* 'degR';59 s1. Outlet.z= [0.0468, 0.0783, 0.8749, 0];56 s1.F = 52126 * 'mol/h'; 57 s1.P = 1 * 'atm'; 58 s1.T = 534.67* 'degR'; 59 s1.Composition= [0.0468, 0.0783, 0.8749, 0]; 60 60 61 61 Reac.Vr = 300 * 'gal'; -
trunk/sample/reactors/sample_equil.mso
r426 r634 75 75 76 76 SPECIFY 77 Fin. Outlet.F = 2*'mol/s';78 Fin. Outlet.z= [0.5, 0.5, 0.0, 0.0];79 Fin. Outlet.P = 1*'atm';80 Fin. Outlet.T = 1100*'K';77 Fin.F = 2*'mol/s'; 78 Fin.Composition= [0.5, 0.5, 0.0, 0.0]; 79 Fin.P = 1*'atm'; 80 Fin.T = 1100*'K'; 81 81 82 82 R.Outlet.P = 1*'bar'; -
trunk/sample/reactors/sample_pfr.mso
r213 r634 79 79 80 80 SPECIFY 81 s1. Outlet.F = 138/1000 * 'kmol/h';82 s1. Outlet.T = 1035 * 'K';83 s1. Outlet.P = 1.6 * 'atm';84 s1. Outlet.z= [1, 0, 0];81 s1.F = 138/1000 * 'kmol/h'; 82 s1.T = 1035 * 'K'; 83 s1.P = 1.6 * 'atm'; 84 s1.Composition = [1, 0, 0]; 85 85 86 86 "Adiabatic"
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