Changeset 911
- Timestamp:
- Feb 20, 2010, 1:56:44 AM (13 years ago)
- Location:
- branches/gui/sample
- Files:
-
- 6 edited
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/sample/case_study/sample_flash.mso
r804 r911 52 52 53 53 EQUATIONS 54 fl.OutletL .F = 400*sqrt(fl.Level/'m') * 'kmol/h';54 fl.OutletLiquid.F = 400*sqrt(fl.Geometry.Level/'m') * 'kmol/h'; 55 55 56 56 SPECIFY … … 60 60 s1.Composition = [0.2379,0.3082,0.09958,0.1373,0.08872,0.1283]; 61 61 62 fl.OutletV .F = 68.5 * 'kmol/h';63 Q.OutletQ .Q= 0 * 'kJ/h';62 fl.OutletVapour.F = 68.5 * 'kmol/h'; 63 Q.OutletQ = 0 * 'kJ/h'; 64 64 65 65 SET 66 fl. V = 50 * 'm^3';67 fl. diameter = 2 * 'm';68 fl. orientation = "vertical";69 # fl. orientation = "horizontal";66 fl.Geometry.Lenght = 10 * 'm'; 67 fl.Geometry.Diameter = 2 * 'm'; 68 fl.Geometry.Orientation = "vertical"; 69 # fl.Geometry.Orientation = "horizontal"; 70 70 71 71 INITIAL 72 fl.OutletL.T = 338 * 'K'; 73 fl.Level = 0.4 * 'm'; 74 75 fl.OutletL.z(1) = 0.1; 76 fl.OutletL.z(2) = 0.1; 77 fl.OutletL.z(3) = 0.1; 78 fl.OutletL.z(4) = 0.1; 79 fl.OutletL.z(5) = 0.1; 72 fl.OutletLiquid.T = 338 * 'K'; 73 fl.Geometry.Level = 0.4 * 'm'; 74 fl.OutletLiquid.z([1:5]) = 0.1; 80 75 81 76 OPTIONS … … 118 113 s1.Composition = [0.2379,0.3082,0.09959,0.1373,0.08872,0.1283]; 119 114 120 fl.OutletL .P = 2.5 * 'atm';115 fl.OutletLiquid.P = 2.5 * 'atm'; 121 116 122 #Q.OutletQ .Q= 0 * 'kJ/h';123 fl.OutletL .T = 315.06 * 'K';117 #Q.OutletQ = 0 * 'kJ/h'; 118 fl.OutletLiquid.T = 315.06 * 'K'; 124 119 125 120 OPTIONS … … 137 132 138 133 139 fl.OutletV .F'kmol/h';134 fl.OutletVapour.F'kmol/h'; 140 135 141 136 end … … 150 145 RESPONSE 151 146 152 fl.OutletV .z(1);153 fl.OutletV .F'kmol/h';147 fl.OutletVapour.z(1); 148 fl.OutletVapour.F'kmol/h'; 154 149 155 150 end -
branches/gui/sample/sensitivity/sense_flash.mso
r804 r911 52 52 53 53 EQUATIONS 54 fl.OutletL .F = 400*sqrt(fl.Level/'m') * 'kmol/h';54 fl.OutletLiquid.F = 400*sqrt(fl.Geometry.Level/'m') * 'kmol/h'; 55 55 56 56 SPECIFY … … 60 60 s1.Composition = [0.2379,0.3082,0.09958,0.1373,0.08872,0.1283]; 61 61 62 fl.OutletV .F = 68.5 * 'kmol/h';63 Q.OutletQ .Q= 0 * 'kJ/h';62 fl.OutletVapour.F = 68.5 * 'kmol/h'; 63 Q.OutletQ = 0 * 'kJ/h'; 64 64 65 65 SET 66 fl. V = 50 * 'm^3';67 fl. diameter = 2 * 'm';68 fl. orientation = "vertical";69 # fl. orientation = "horizontal";66 fl.Geometry.Lenght = 10 * 'm'; 67 fl.Geometry.Diameter = 2 * 'm'; 68 fl.Geometry.Orientation = "vertical"; 69 # fl.Geometry.Orientation = "horizontal"; 70 70 71 71 INITIAL 72 fl.OutletL.T = 338 * 'K'; 73 fl.Level = 0.4 * 'm'; 74 75 fl.OutletL.z(1) = 0.1; 76 fl.OutletL.z(2) = 0.1; 77 fl.OutletL.z(3) = 0.1; 78 fl.OutletL.z(4) = 0.1; 79 fl.OutletL.z(5) = 0.1; 72 fl.OutletLiquid.T = 338 * 'K'; 73 fl.Geometry.Level = 0.4 * 'm'; 74 fl.OutletLiquid.z([1:5]) = 0.1; 80 75 81 76 OPTIONS … … 118 113 s1.Composition = [0.2379,0.3082,0.09959,0.1373,0.08872,0.1283]; 119 114 120 fl.OutletL .P = 2.5 * 'atm';115 fl.OutletLiquid.P = 2.5 * 'atm'; 121 116 122 #Q.OutletQ .Q= 0 * 'kJ/h';123 fl.OutletL .T = 315.06 * 'K';117 #Q.OutletQ = 0 * 'kJ/h'; 118 fl.OutletLiquid.T = 315.06 * 'K'; 124 119 125 120 OPTIONS … … 136 131 RESPONSE 137 132 138 fl.OutletV .F'kmol/h';133 fl.OutletVapour.F'kmol/h'; 139 134 140 135 end … … 151 146 152 147 153 fl.OutletV .F'kmol/h';148 fl.OutletVapour.F'kmol/h'; 154 149 155 150 end -
branches/gui/sample/stage_separators/ColumnPacked_Diagram.mso
r749 r911 59 59 Packed_Section.INITIALIZATION.BottomStageComposition(4) = 0.2; 60 60 Packed_Section.INITIALIZATION.BottomStageComposition(5) = 0.2; 61 Packed_Section.INITIALIZATION. LiquidMolarHoldup = 0.01 * 'kmol';61 Packed_Section.INITIALIZATION.ColumnHoldup = 0.01; 62 62 63 63 SPECIFY -
branches/gui/sample/stage_separators/Sample_flash_PID.mso
r796 r911 155 155 156 156 SET 157 F101_1. Orientation = "vertical";158 F101_1. Heads = "flat";159 F101_1. Diameter = 3.1 * 'm';160 F101_1. Lenght = 6 * 'm';157 F101_1.Geometry.Orientation = "vertical"; 158 F101_1.Geometry.Heads = "flat"; 159 F101_1.Geometry.Diameter = 3.1 * 'm'; 160 F101_1.Geometry.Lenght = 6 * 'm'; 161 161 F101_1.Levelpercent_Initial = 0.80; 162 162 F101_1.Temperature_Initial = 373 * 'K'; -
branches/gui/sample/stage_separators/Sample_flash_PIDincr.mso
r796 r911 36 36 37 37 SET 38 F101. Orientation = "vertical";39 F101. Heads = "flat";40 F101. Diameter = 3.1 * 'm';41 F101. Lenght = 6 * 'm';38 F101.Geometry.Orientation = "vertical"; 39 F101.Geometry.Heads = "flat"; 40 F101.Geometry.Diameter = 3.1 * 'm'; 41 F101.Geometry.Lenght = 6 * 'm'; 42 42 F101.Levelpercent_Initial = 0.70; 43 43 F101.Temperature_Initial = 383 * 'K'; -
branches/gui/sample/stage_separators/Section_Column_Three_Inputs.mso
r905 r911 5 5 using "streams.mso"; 6 6 using "controllers/PIDs.mso"; 7 using "mixers_splitters/splitter.mso";8 7 using "pressure_changers/valve.mso"; 9 using "pressure_changers/pump.mso";10 8 using "controllers/heat_flow.mso"; 11 9 using "stage_separators/column.mso"; 12 using "stage_separators/reboiler.mso";13 using "stage_separators/condenser.mso";14 10 15 11 FlowSheet Section_Column_Three_Inputs
Note: See TracChangeset
for help on using the changeset viewer.