- Timestamp:
- Aug 30, 2007, 1:12:27 PM (15 years ago)
- Location:
- trunk/eml
- Files:
-
- 11 edited
Legend:
- Unmodified
- Added
- Removed
-
trunk/eml/pressure_changers/compressor.mso
r351 r353 26 26 Brief = "Model of a centrifugal compressor."; 27 27 Info = 28 "Assumptions: 29 30 31 28 "== Assumptions == 29 * Steady State; 30 * Only Vapor; 31 * Adiabatic. 32 32 33 Specify:34 35 36 37 33 == Specify == 34 * the inlet stream; 35 * the outlet pressure (Outlet.P); 36 * the Isentropic efficiency (Effs). 37 "; 38 38 39 39 PARAMETERS -
trunk/eml/pressure_changers/pump.mso
r351 r353 26 26 Brief = "Model of a centrifugal pump."; 27 27 Info = 28 "Assumptions: 29 30 31 32 28 "== Assumptions == 29 * Steady State; 30 * Only Liquid; 31 * Adiabatic; 32 * Isentropic. 33 33 34 Specify:35 36 37 34 == Specify == 35 * the inlet stream; 36 * the Pressure Increase Pdiff. 37 "; 38 38 39 39 PARAMETERS -
trunk/eml/pressure_changers/turbine.mso
r351 r353 26 26 Brief = "Model of a Hidraulic Turbine."; 27 27 Info = 28 "Assumptions: 29 30 31 32 28 "== Assumptions == 29 * Steady State; 30 * Only Liquid; 31 * Adiabatic; 32 * Isentropic. 33 33 34 Specify: 35 36 37 38 39 40 34 == Specify == 35 * the inlet stream; 36 * the Pressure Increase (Pdiff) OR the outlet pressure (Outlet.P); 37 * the Turbine efficiency (Eff); 38 * the Brake efficiency (Meff); 39 * the Volumetric expansivity (Beta). 40 "; 41 41 42 42 PARAMETERS -
trunk/eml/pressure_changers/valve.mso
r351 r353 27 27 Brief = "Model of a valve."; 28 28 Info = 29 "Model of valves: 30 31 32 33 34 29 "== Model of valves == 30 * Linear; 31 * Parabolic; 32 * Equal; 33 * Quick; 34 * Hyperbolic. 35 35 36 Assumptions: 37 38 39 36 == Assumptions == 37 * Steady State; 38 * Liquid; 39 * Isentalpic. 40 40 41 Specify: 42 43 44 45 46 47 41 == Specify == 42 * the valve type; 43 * the inlet stream; 44 * the Volumetric Flow (Qv); 45 * the Valve Coefficient (cv); 46 * the opening (x). 47 "; 48 48 49 49 PARAMETERS … … 142 142 Brief = "Model of a very simple valve - used in distillation column models."; 143 143 Info = 144 "Assumptions: 145 146 147 148 144 "== Assumptions == 145 * no flashing liquid in the valve; 146 * the flow in the valve is adiabatic; 147 * dynamics in the valve are neglected; 148 * linear flow type. 149 149 150 Specify: 151 152 150 == Specify == 151 * the inlet stream 152 * the plug position (x) OR outlet temperature (Outlet.T) OR outlet pressure (Outlet.P) 153 153 154 154 OR 155 155 156 157 158 159 156 * the inlet stream excluding its flow (Inlet.F) 157 * the outlet pressure (Outlet.P) OR outlet flow (Outlet.F) 158 * the plug position (x) 159 "; 160 160 161 161 PARAMETERS -
trunk/eml/stage_separators/batch_dist.mso
r352 r353 25 25 Brief = "Model of a Batch Differential Distillation."; 26 26 Info = 27 "Assumptions: 28 29 30 27 "== Assumptions == 28 * perfect mixing of both phases; 29 * thermodynamics equilibrium; 30 * no liquid entrainment in the vapour stream. 31 31 32 Specify: 33 34 35 32 == Specify == 33 * the inlet stream; 34 * the liquid inlet stream; 35 * the molar flow of the vapour outlet stream. 36 36 37 Initial Conditions: 38 39 40 41 37 == Initial Conditions == 38 * the distillator temperature (T); 39 * the distillator liquid level (Level); 40 * (NoComps - 1) compositions in the distillator or in the OutletV. 41 "; 42 42 43 43 PARAMETERS -
trunk/eml/stage_separators/column.mso
r300 r353 50 50 Brief = "Model of a column section."; 51 51 Info = 52 "Model of a column section containing: 53 54 55 Specify: 56 57 58 59 60 61 Initial Conditions: 62 63 64 65 52 "== Model of a column section containing == 53 * NTrays trays. 54 55 == Specify == 56 * the feed stream of each tray (Inlet); 57 * the Murphree eficiency for each tray Emv; 58 * the InletL stream of the top tray; 59 * the InletV stream of the bottom tray. 60 61 == Initial Conditions == 62 * the trays temperature (OutletL.T); 63 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 64 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray. 65 "; 66 66 67 67 PARAMETERS … … 110 110 Brief = "Model of a distillation column with dynamic condenser and dynamic reboiler."; 111 111 Info = 112 "Specify: 113 114 115 116 117 118 119 120 121 Initial Conditions: 122 123 124 125 126 127 128 129 130 131 132 133 112 "== Specify == 113 * the feed stream of each tray (Inlet); 114 * the Murphree eficiency for each tray Emv; 115 * the pump pressure difference; 116 * the heat supllied in reboiler and condenser; 117 * the condenser vapor outlet flow (OutletV.F); 118 * the reboiler liquid outlet flow (OutletL.F); 119 * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac. 120 121 == Initial Conditions == 122 * the trays temperature (OutletL.T); 123 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 124 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 125 126 * the condenser temperature (OutletL.T); 127 * the condenser liquid level (Level); 128 * (NoComps - 1) OutletL (OR OutletV) compositions; 129 130 * the reboiler temperature (OutletL.T); 131 * the reboiler liquid level (Level); 132 * (NoComps - 1) OutletL (OR OutletV) compositions. 133 "; 134 134 135 135 PARAMETERS … … 209 209 Brief = "Model of a distillation column with steady condenser and steady reboiler."; 210 210 Info = 211 "Specify: 212 213 214 215 216 217 218 219 220 221 Initial Conditions: 222 223 224 225 226 227 228 229 230 231 232 233 211 "== Specify == 212 * the feed stream of each tray (Inlet); 213 * the Murphree eficiency for each tray Emv; 214 * the pump head; 215 * the condenser pressure drop; 216 * the heat supllied in top and bottom tanks; 217 * the heat supllied in condenser and reboiler; 218 * the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product; 219 * both top splitter outlet flows OR one of the splitter outlet flows and the splitter frac. 220 221 == Initial Conditions == 222 * the trays temperature (OutletL.T); 223 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 224 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 225 226 * the top tank temperature (OutletL.T); 227 * the top tank liquid level (Level); 228 * (NoComps - 1) OutletL (OR OutletV) compositions; 229 230 * the bottom tank temperature (OutletL.T); 231 * the bottom tank liquid level (Level); 232 * (NoComps - 1) OutletL (OR OutletV) compositions. 233 "; 234 234 235 235 PARAMETERS … … 314 314 Brief = "Model of a distillation column with dynamic condenser and steady reboiler."; 315 315 Info = 316 "Specify: 317 318 319 320 321 322 323 324 325 Initial Conditions: 326 327 328 329 330 331 332 333 334 335 336 337 316 "== Specify == 317 * the feed stream of each tray (Inlet); 318 * the Murphree eficiency for each tray Emv; 319 * the pump head; 320 * the condenser vapor outlet flow (OutletV.F); 321 * the heat supllied in bottom tank; 322 * the heat supllied in condenser and reboiler; 323 * the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product; 324 325 == Initial Conditions == 326 * the trays temperature (OutletL.T); 327 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 328 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 329 330 * the condenser temperature (OutletL.T); 331 * the condenser liquid level (Level); 332 * (NoComps - 1) OutletL (OR OutletV) compositions; 333 334 * the bottom tank temperature (OutletL.T); 335 * the bottom tank liquid level (Level); 336 * (NoComps - 1) OutletL (OR OutletV) compositions. 337 "; 338 338 339 339 PARAMETERS … … 414 414 Brief = "Model of a distillation column with steady condenser and dynamic reboiler."; 415 415 Info = 416 "Specify: 417 418 419 420 421 422 423 424 425 426 Initial Conditions: 427 428 429 430 431 432 433 434 435 436 437 438 416 "== Specify == 417 * the feed stream of each tray (Inlet); 418 * the Murphree eficiency for each tray (Emv); 419 * the pump pressure difference; 420 * the heat supllied in reboiler and condenser; 421 * the heat supllied in the top tank; 422 * the condenser pressure drop; 423 * the reboiler liquid outlet flow (OutletL.F); 424 * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac. 425 426 == Initial Conditions == 427 * the trays temperature (OutletL.T); 428 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 429 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 430 431 * the top tank temperature (OutletL.T); 432 * the top tank liquid level (Level); 433 * (NoComps - 1) OutletL (OR OutletV) compositions; 434 435 * the reboiler temperature (OutletL.T); 436 * the reboiler liquid level (Level); 437 * (NoComps - 1) OutletL (OR OutletV) compositions. 438 "; 439 439 440 440 PARAMETERS … … 510 510 Brief = "Model of a rectifier column with dynamic condenser."; 511 511 Info = 512 "Specify: 513 514 515 516 517 518 519 520 521 Initial Conditions: 522 523 524 525 526 527 528 529 512 "== Specify == 513 * the feed stream of each tray (Inlet); 514 * the Murphree eficiency for each tray Emv; 515 * the InletV stream of the bottom tray; 516 * the pump pressure difference; 517 * the heat supllied in the condenser; 518 * the condenser vapor outlet flow (OutletV.F); 519 * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac. 520 521 == Initial Conditions == 522 * the trays temperature (OutletL.T); 523 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 524 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 525 526 * the condenser temperature (OutletL.T); 527 * the condenser liquid level (Level); 528 * (NoComps - 1) OutletL (OR OutletV) compositions; 529 "; 530 530 531 531 PARAMETERS … … 590 590 Brief = "Model of a rectifier column with steady condenser."; 591 591 Info = 592 "Specify: 593 594 595 596 597 598 599 600 601 602 Initial Conditions: 603 604 605 606 607 608 609 610 592 "== Specify == 593 * the feed stream of each tray (Inlet); 594 * the Murphree eficiency for each tray Emv; 595 * the InletV stream of the bottom tray; 596 * the pump head; 597 * the condenser pressure drop; 598 * the heat supllied in the top tank; 599 * the heat supllied in condenser; 600 * both top splitter outlet flows OR one of the splitter outlet flows and the splitter frac. 601 602 == Initial Conditions == 603 * the trays temperature (OutletL.T); 604 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 605 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 606 607 * the top tank temperature (OutletL.T); 608 * the top tank liquid level (Level); 609 * (NoComps - 1) OutletL (OR OutletV) compositions; 610 "; 611 611 612 612 PARAMETERS … … 670 670 Brief = "Model of a refluxed stripping column with dynamic condenser."; 671 671 Info = 672 "Specify: 673 674 675 676 677 678 679 680 681 Initial Conditions: 682 683 684 685 686 687 688 689 672 "== Specify == 673 * the feed stream of each tray (Inlet); 674 * the Murphree eficiency for each tray Emv; 675 * the InletV stream of the bottom tray; 676 * the pump pressure difference; 677 * the heat supllied in the condenser; 678 * the condenser vapor outlet flow (OutletV.F); 679 * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac. 680 681 == Initial Conditions == 682 * the trays temperature (OutletL.T); 683 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 684 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 685 686 * the condenser temperature (OutletL.T); 687 * the condenser liquid level (Level); 688 * (NoComps - 1) OutletL (OR OutletV) compositions; 689 "; 690 690 691 691 PARAMETERS … … 750 750 Brief = "Model of a refluxed stripping column with steady condenser."; 751 751 Info = 752 "Specify: 753 754 755 756 757 758 759 760 761 762 Initial Conditions: 763 764 765 766 767 768 769 770 752 "== Specify == 753 * the feed stream of each tray (Inlet); 754 * the Murphree eficiency for each tray Emv; 755 * the InletV stream of the bottom tray; 756 * the pump head; 757 * the condenser pressure drop; 758 * the heat supllied in the top tank; 759 * the heat supllied in condenser; 760 * both top splitter outlet flows OR one of the splitter outlet flows and the splitter frac. 761 762 == Initial Conditions == 763 * the trays temperature (OutletL.T); 764 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 765 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 766 767 * the top tank temperature (OutletL.T); 768 * the top tank liquid level (Level); 769 * (NoComps - 1) OutletL (OR OutletV) compositions; 770 "; 771 771 772 772 PARAMETERS … … 830 830 Brief = "Model of a refluxed absorption column with dynamic condenser."; 831 831 Info = 832 "Specify: 833 834 835 836 837 838 839 840 841 Initial Conditions: 842 843 844 845 846 847 848 849 832 "== Specify == 833 * the feed stream of each tray (Inlet); 834 * the Murphree eficiency for each tray Emv; 835 * the InletV stream of the bottom tray; 836 * the pump pressure difference; 837 * the heat supllied in the condenser; 838 * the condenser vapor outlet flow (OutletV.F); 839 * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac. 840 841 == Initial Conditions == 842 * the trays temperature (OutletL.T); 843 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 844 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 845 846 * the condenser temperature (OutletL.T); 847 * the condenser liquid level (Level); 848 * (NoComps - 1) OutletL (OR OutletV) compositions; 849 "; 850 850 851 851 PARAMETERS … … 911 911 Brief = "Model of a refluxed absorption column with steady condenser."; 912 912 Info = 913 "Specify: 914 915 916 917 918 919 920 921 922 923 Initial Conditions: 924 925 926 927 928 929 930 931 913 "== Specify == 914 * the feed stream of each tray (Inlet); 915 * the Murphree eficiency for each tray Emv; 916 * the InletV stream of the bottom tray; 917 * the pump head; 918 * the condenser pressure drop; 919 * the heat supllied in the top tank; 920 * the heat supllied in condenser; 921 * both top splitter outlet flows OR one of the splitter outlet flows and the splitter frac. 922 923 == Initial Conditions == 924 * the trays temperature (OutletL.T); 925 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 926 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 927 928 * the top tank temperature (OutletL.T); 929 * the top tank liquid level (Level); 930 * (NoComps - 1) OutletL (OR OutletV) compositions; 931 "; 932 932 933 933 PARAMETERS … … 991 991 Brief = "Model of a reboiled stripping column with dynamic reboiler."; 992 992 Info = 993 "Specify: 994 995 996 997 998 999 1000 Initial Conditions: 1001 1002 1003 1004 1005 1006 1007 1008 993 "== Specify == 994 * the feed stream of each tray (Inlet); 995 * the Murphree eficiency for each tray Emv; 996 * the InletL stream of the top tray; 997 * the heat supllied in the reboiler; 998 * the reboiler liquid outlet flow (OutletL.F); 999 1000 == Initial Conditions == 1001 * the trays temperature (OutletL.T); 1002 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 1003 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 1004 1005 * the reboiler temperature (OutletL.T); 1006 * the reboiler liquid level (Level); 1007 * (NoComps - 1) OutletL (OR OutletV) compositions. 1008 "; 1009 1009 1010 1010 PARAMETERS … … 1069 1069 Brief = "Model of a reboiled stripping column with steady reboiler."; 1070 1070 Info = 1071 "Specify: 1072 1073 1074 1075 1076 1077 1078 1079 Initial Conditions: 1080 1081 1082 1083 1084 1085 1086 1087 1071 "== Specify == 1072 * the feed stream of each tray (Inlet); 1073 * the Murphree eficiency for each tray (Emv); 1074 * the InletL stream of the top tray; 1075 * the heat supllied in bottom tank; 1076 * the heat supllied in the reboiler; 1077 * the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product; 1078 1079 == Initial Conditions == 1080 * the trays temperature (OutletL.T); 1081 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 1082 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 1083 1084 * the bottom tank temperature (OutletL.T); 1085 * the bottom tank liquid level (Level); 1086 * (NoComps - 1) OutletL (OR OutletV) compositions. 1087 "; 1088 1088 1089 1089 PARAMETERS … … 1150 1150 Brief = "Model of a reboiled absorption column with dynamic reboiler."; 1151 1151 Info = 1152 "Specify: 1153 1154 1155 1156 1157 1158 1159 Initial Conditions: 1160 1161 1162 1163 1164 1165 1166 1167 1152 "== Specify == 1153 * the feed stream of each tray (Inlet); 1154 * the Murphree eficiency for each tray Emv; 1155 * the InletL stream of the top tray; 1156 * the heat supllied in the reboiler; 1157 * the reboiler liquid outlet flow (OutletL.F); 1158 1159 == Initial Conditions == 1160 * the trays temperature (OutletL.T); 1161 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 1162 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 1163 1164 * the reboiler temperature (OutletL.T); 1165 * the reboiler liquid level (Level); 1166 * (NoComps - 1) OutletL (OR OutletV) compositions. 1167 "; 1168 1168 1169 1169 PARAMETERS … … 1228 1228 Brief = "Model of a reboiled absorption column with steady reboiler."; 1229 1229 Info = 1230 "Specify: 1231 1232 1233 1234 1235 1236 1237 1238 Initial Conditions: 1239 1240 1241 1242 1243 1244 1245 1246 1230 "== Specify == 1231 * the feed stream of each tray (Inlet); 1232 * the Murphree eficiency for each tray (Emv); 1233 * the InletL stream of the top tray; 1234 * the heat supllied in bottom tank; 1235 * the heat supllied in the reboiler; 1236 * the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product; 1237 1238 == Initial Conditions == 1239 * the trays temperature (OutletL.T); 1240 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 1241 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 1242 1243 * the bottom tank temperature (OutletL.T); 1244 * the bottom tank liquid level (Level); 1245 * (NoComps - 1) OutletL (OR OutletV) compositions. 1246 "; 1247 1247 1248 1248 PARAMETERS … … 1305 1305 Brief = "Model of a reactive distillation column with dynamic condenser and reboiler."; 1306 1306 Info = 1307 "Specify: 1308 1309 1310 1311 1312 1313 1314 1315 1316 1317 Initial Conditions: 1318 1319 1320 1321 1322 1323 1324 1325 1326 1327 1328 1329 1307 "== Specify == 1308 * the reaction related variables for each tray, condenser and reboiler; 1309 * the feed stream of each tray (Inlet); 1310 * the Murphree eficiency for each tray Emv; 1311 * the pump pressure difference; 1312 * the heat supllied in reboiler and condenser; 1313 * the condenser vapor outlet flow (OutletV.F); 1314 * the reboiler liquid outlet flow (OutletL.F); 1315 * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac. 1316 1317 == Initial Conditions == 1318 * the trays temperature (OutletL.T); 1319 * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); 1320 * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; 1321 1322 * the condenser temperature (OutletL.T); 1323 * the condenser liquid level (Level); 1324 * (NoComps - 1) OutletL (OR OutletV) compositions; 1325 1326 * the reboiler temperature (OutletL.T); 1327 * the reboiler liquid level (Level); 1328 * (NoComps - 1) OutletL (OR OutletV) compositions. 1329 "; 1330 1330 1331 1331 PARAMETERS -
trunk/eml/stage_separators/condenser.mso
r352 r353 26 26 Brief = "Model of a dynamic condenser."; 27 27 Info = 28 "Assumptions: 29 30 31 32 Specify: 33 34 35 36 37 Initial Conditions: 38 39 40 41 28 "== Assumptions == 29 * perfect mixing of both phases; 30 * thermodynamics equilibrium. 31 32 == Specify == 33 * the inlet stream; 34 * the outlet flows: OutletV.F and OutletL.F; 35 * the heat supply. 36 37 == Initial Conditions == 38 * the condenser temperature (OutletL.T); 39 * the condenser liquid level (Level); 40 * (NoComps - 1) OutletL (OR OutletV) compositions. 41 "; 42 42 43 43 PARAMETERS … … 112 112 Brief = "Model of a Steady State condenser with no thermodynamics equilibrium."; 113 113 Info = 114 "Assumptions: 115 116 117 118 Specify: 119 120 121 122 114 "== Assumptions == 115 * perfect mixing of both phases; 116 * no thermodynamics equilibrium. 117 118 == Specify == 119 * the inlet stream; 120 * the pressure drop in the condenser; 121 * the heat supply. 122 "; 123 123 124 124 PARAMETERS … … 153 153 Brief = "Model of a Condenser with reaction in liquid phase."; 154 154 Info = 155 "Assumptions: 156 157 158 159 160 Specify: 161 162 163 164 165 166 Initial Conditions: 167 168 169 170 155 "== Assumptions == 156 * perfect mixing of both phases; 157 * thermodynamics equilibrium; 158 * the reaction only takes place in liquid phase. 159 160 == Specify == 161 * the reaction related variables; 162 * the inlet stream; 163 * the outlet flows: OutletV.F and OutletL.F; 164 * the heat supply. 165 166 == Initial Conditions == 167 * the condenser temperature (OutletL.T); 168 * the condenser liquid level (Level); 169 * (NoComps - 1) OutletL (OR OutletV) compositions. 170 "; 171 171 172 172 PARAMETERS -
trunk/eml/stage_separators/flash.mso
r352 r353 25 25 Brief = "Model of a dynamic flash."; 26 26 Info = 27 "Assumptions: 28 29 30 Specify: 31 32 33 34 Initial Conditions: 35 36 37 38 27 "== Assumptions == 28 * both phases are perfectly mixed. 29 30 == Specify == 31 * the feed stream; 32 * the outlet flows: OutletV.F and OutletL.F. 33 34 == Initial Conditions == 35 * the flash initial temperature (OutletL.T); 36 * the flash initial level (Level); 37 * (NoComps - 1) OutletL (OR OutletV) compositions. 38 "; 39 39 40 40 PARAMETERS … … 133 133 Brief = "Model of a Steady State flash."; 134 134 Info = 135 "Assumptions: 136 137 138 Specify: 139 140 141 142 135 "== Assumptions == 136 * both phases are perfectly mixed. 137 138 == Specify == 139 * the feed stream; 140 * the outlet pressure (OutletV.P); 141 * the outlet temperature OR the heat supplied. 142 "; 143 143 144 144 PARAMETERS … … 180 180 Icon = "icon/Flash"; 181 181 Brief = "Model of a static PH flash."; 182 Info = " 183 This model is for using the flashPH 184 routine available on VRTherm. 185 186 Assumptions: 187 * perfect mixing of both phases; 188 189 Specify: 190 * the feed stream; 191 * the heat duty; 192 * the outlet pressure. 193 "; 182 Info = 183 "This model is for using the flashPH routine available on VRTherm. 184 185 == Assumptions == 186 * perfect mixing of both phases; 187 188 == Specify == 189 * the feed stream; 190 * the heat duty; 191 * the outlet pressure. 192 "; 194 193 195 194 PARAMETERS … … 234 233 Icon = "icon/Flash"; 235 234 Brief = "Another model of a static PH flash."; 236 Info = "237 238 239 240 241 242 243 Assumptions: 244 245 246 Specify: 247 248 249 250 235 Info = 236 "This model shows how to model a pressure enthalpy flash 237 directly with the EMSO modeling language. 238 239 This model is for demonstration purposes only, the flashPH 240 routine available on VRTherm is much more robust. 241 242 == Assumptions == 243 * perfect mixing of both phases; 244 245 == Specify == 246 * the feed stream; 247 * the heat duty; 248 * the outlet pressure. 249 "; 251 250 252 251 PARAMETERS -
trunk/eml/stage_separators/reboiler.mso
r352 r353 25 25 Icon = "icon/Reboiler"; 26 26 Brief = "Model of a dynamic reboiler - kettle."; 27 Info = " 28 <h2>Assumptions</h2> 29 <ul> 30 <li>perfect mixing of both phases; 31 <li>thermodynamics equilibrium; 32 <li>no liquid entrainment in the vapour stream. 33 </ul> 34 35 <h2>Specify</h2> 36 <ul> 37 <li> the inlet stream; 38 <li> the liquid inlet stream; 39 <li> the outlet flows: OutletV.F and OutletL.F; 40 <li> the heat supply. 41 </ul> 42 43 <h2>Initial Conditions</h2> 44 <ul> 45 <li> the reboiler temperature (OutletL.T); 46 <li> the reboiler liquid level (Level); 47 <li> (NoComps - 1) OutletL (OR OutletV) compositions. 48 </ul> 49 "; 27 Info = 28 "== Assumptions == 29 30 * perfect mixing of both phases; 31 * thermodynamics equilibrium; 32 * no liquid entrainment in the vapour stream. 33 34 == Specify == 35 36 * the inlet stream; 37 * the liquid inlet stream; 38 * the outlet flows: OutletV.F and OutletL.F; 39 * the heat supply. 40 41 == Initial Conditions == 42 43 * the reboiler temperature (OutletL.T); 44 * the reboiler liquid level (Level); 45 * (NoComps - 1) OutletL (OR OutletV) compositions. 46 "; 50 47 51 48 PARAMETERS … … 125 122 Brief = "Model of a Steady State reboiler with no thermodynamics equilibrium - thermosyphon."; 126 123 Info = 127 "Assumptions: 128 129 130 131 132 Specify: 133 134 135 124 "== Assumptions == 125 * perfect mixing of both phases; 126 * no thermodynamics equilibrium; 127 * no liquid entrainment in the vapour stream. 128 129 == Specify == 130 * the InletL stream; 131 * the heat supply OR the outlet temperature (OutletV.T); 132 "; 136 133 137 134 PARAMETERS … … 176 173 Brief = "Model of a Steady State reboiler with fake calculation of outlet conditions."; 177 174 Info = 178 179 180 181 175 "Model of a Steady State reboiler with fake calculation of 176 vaporisation fraction and output temperature, but with a real 177 calculation of the output stream enthalpy. 178 "; 182 179 183 180 PARAMETERS … … 222 219 Brief = "Model of a dynamic reboiler with reaction."; 223 220 Info = 224 "Assumptions: 225 226 227 228 229 230 Specify: 231 232 233 234 235 236 237 Initial Conditions: 238 239 240 241 221 "== Assumptions == 222 * perfect mixing of both phases; 223 * thermodynamics equilibrium; 224 * no liquid entrainment in the vapour stream; 225 * the reaction takes place only in the liquid phase. 226 227 == Specify == 228 * the kinetics variables; 229 * the inlet stream; 230 * the liquid inlet stream; 231 * the outlet flows: OutletV.F and OutletL.F; 232 * the heat supply. 233 234 == Initial Conditions == 235 * the reboiler temperature (OutletL.T); 236 * the reboiler liquid level (Level); 237 * (NoComps - 1) OutletL (OR OutletV) compositions. 238 "; 242 239 243 240 PARAMETERS -
trunk/eml/stage_separators/tank.mso
r352 r353 42 42 Brief = "Model of a cylindrical tank."; 43 43 Info = 44 "Specify: 45 46 47 48 49 Initial Conditions: 50 51 52 53 44 "== Specify == 45 * the Inlet stream; 46 * the outlet flow; 47 * the tank Q. 48 49 == Initial Conditions == 50 * the tank initial temperature (OutletL.T); 51 * the tank initial level (Level); 52 * (NoComps - 1) OutletL (OR OutletV) compositions. 53 "; 54 54 55 55 PARAMETERS … … 101 101 Brief = "Model of a tank with a lain cylinder geometry."; 102 102 Info = 103 "Specify: 104 105 106 107 108 Initial Conditions: 109 110 111 112 103 "== Specify == 104 * the Inlet stream; 105 * the outlet flow; 106 * the tank Q. 107 108 == Initial Conditions == 109 * the tank initial temperature (OutletL.T); 110 * the tank initial level (Level); 111 * (NoComps - 1) OutletL (OR OutletV) compositions. 112 "; 113 113 114 114 PARAMETERS … … 161 161 Brief = "Model of a simplified tank."; 162 162 Info = 163 "Specify: 164 165 166 Initial Conditions: 167 168 163 "== Specify == 164 * the Inlet flow rate; 165 166 == Initial Conditions == 167 * the tank initial level (Level); 168 "; 169 169 170 170 PARAMETERS … … 191 191 Brief = "Model of a tank with feed stream."; 192 192 Info = 193 "Specify: 194 195 196 197 198 199 Initial Conditions: 200 201 202 203 193 "== Specify == 194 * the Inlet stream; 195 * the Feed stream; 196 * the outlet flow; 197 * the tank Q. 198 199 == Initial Conditions == 200 * the tank initial temperature (OutletL.T); 201 * the tank initial level (Level); 202 * (NoComps - 1) OutletL (OR OutletV) compositions. 203 "; 204 204 205 205 PARAMETERS -
trunk/eml/stage_separators/tray.mso
r351 r353 26 26 Brief = "Basic equations of a tray column model."; 27 27 Info = 28 29 30 31 Assumptions 32 33 34 35 36 37 28 "This model contains only the main equations of a column tray equilibrium model without 29 the hidraulic equations. 30 31 == Assumptions == 32 * both phases (liquid and vapour) exists all the time; 33 * thermodymanic equilibrium with Murphree plate efficiency; 34 * no entrainment of liquid or vapour phase; 35 * no weeping; 36 * the dymanics in the downcomer are neglected. 37 "; 38 38 39 39 PARAMETERS … … 111 111 Brief = "Complete model of a column tray."; 112 112 Info = 113 "Specify: 114 115 116 117 118 119 Initial: 120 121 122 123 113 "== Specify == 114 * the Feed stream 115 * the Liquid inlet stream 116 * the Vapour inlet stream 117 * the Vapour outlet flow (OutletV.F) 118 119 == Initial == 120 * the plate temperature (OutletL.T) 121 * the liquid height (Level) OR the liquid flow OutletL.F 122 * (NoComps - 1) OutletL compositions 123 "; 124 124 125 125 PARAMETERS … … 160 160 Brief = "Model of a tray with reaction."; 161 161 Info = 162 "Assumptions 163 164 165 166 167 168 169 Specify: 170 171 172 173 174 175 176 Initial: 177 178 179 180 162 "== Assumptions == 163 * both phases (liquid and vapour) exists all the time; 164 * thermodymanic equilibrium with Murphree plate efficiency; 165 * no entrainment of liquid or vapour phase; 166 * no weeping; 167 * the dymanics in the downcomer are neglected. 168 169 == Specify == 170 * the Feed stream; 171 * the Liquid inlet stream; 172 * the Vapour inlet stream; 173 * the Vapour outlet flow (OutletV.F); 174 * the reaction related variables. 175 176 == Initial == 177 * the plate temperature (OutletL.T) 178 * the liquid height (Level) OR the liquid flow OutletL.F 179 * (NoComps - 1) OutletL compositions 180 "; 181 181 182 182 PARAMETERS
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