Changeset 732
- Timestamp:
- Feb 26, 2009, 6:47:01 PM (15 years ago)
- Location:
- branches/gui
- Files:
-
- 4 edited
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/costs/column_cost.mso
r354 r732 16 16 * Author: Núbia do Carmo Ferreira 17 17 * $Id: column.mso 210 2007-03-15 12:52:28Z arge $ 18 *--------------------------------------------------------------------- *#18 *---------------------------------------------------------------------# 19 19 20 20 using "stage_separators/column"; 21 21 22 #*---------------------------------------------------------------------- 22 23 24 25 Needs to be Updated !!!!!!! 26 27 28 #---------------------------------------------------------------------- 23 29 * Model of cost of a distillation column containing: 24 30 * - NTrays like tray; … … 33 39 * 0.6m < D < 4.8m 34 40 * 35 *--------------------------------------------------------------------- *#41 *---------------------------------------------------------------------# 36 42 37 43 Model Distillation_kettle_cond_cost as Distillation_kettle_cond … … 156 162 * - a pump in reflux stream. 157 163 * 158 * ------------------------------------------------------------------ *#164 * ------------------------------------------------------------------# 159 165 Model Distillation_thermosyphon_subcooling_cost as Distillation_thermosyphon_subcooling 160 166 ATTRIBUTES … … 279 285 * - a pump in reflux stream. 280 286 * 281 * ------------------------------------------------------------------ *#287 * ------------------------------------------------------------------# 282 288 Model Distillation_thermosyphon_cond_cost as Distillation_thermosyphon_cond 283 289 ATTRIBUTES … … 399 405 * - a pump in reflux stream. 400 406 * 401 * ------------------------------------------------------------------ *#407 * ------------------------------------------------------------------# 402 408 Model Distillation_kettle_subcooling_cost as Distillation_kettle_subcooling 403 409 ATTRIBUTES … … 509 515 Ws = dens_mass_material*Di*(Lt + 0.8116*Di)*Tp*Pi; 510 516 end 517 518 *# -
branches/gui/eml/costs/flash_cost.mso
r331 r732 74 74 Ce = Cb*Fm + Ca; 75 75 76 switch orientation76 switch Orientation 77 77 case "vertical": 78 78 -
branches/gui/sample/costs/sample_distillation_kettle_cond_cost.mso
r581 r732 24 24 * Author: Núbia do Carmo Ferreira 25 25 * $Id: sample_column.mso 247 2007-04-24 13:44:18Z rafael $ 26 *--------------------------------------------------------------------*# 26 *--------------------------------------------------------------------# 27 28 29 30 Needs to be Updated 31 27 32 28 33 using "costs/column_cost"; … … 142 147 #Dynamic = false; 143 148 end 149 *# -
branches/gui/sample/costs/sample_flash_cost.mso
r581 r732 51 51 52 52 EQUATIONS 53 fl.OutletL .F = 400*sqrt(fl.Level/'m') * 'kmol/h';53 fl.OutletLiquid.F = 400*sqrt(fl.Level/'m') * 'kmol/h'; 54 54 55 55 SPECIFY … … 59 59 s1.Composition = [0.2379,0.3082,0.09958,0.1373,0.08872,0.1283]; 60 60 61 fl.OutletV .F = 68.5 * 'kmol/h';61 fl.OutletVapour.F = 68.5 * 'kmol/h'; 62 62 Q.OutletQ = 0 * 'kJ/h'; 63 63 64 64 SET 65 fl.V = 50 * 'm^3';66 fl. diameter = 2 * 'm';67 fl. orientation = "vertical";65 fl.VesselVolume = 50 * 'm^3'; 66 fl.Diameter = 2 * 'm'; 67 fl.Orientation = "vertical"; 68 68 # fl.orientation = "horizontal"; 69 69 … … 83 83 fl.Cost(6,:) = [1.7,0,0];#For "Stainless steell 304" 84 84 85 INITIAL 86 fl.OutletL.T = 338 * 'K'; 87 fl.Level = 0.4 * 'm'; 85 SET 86 87 fl.Levelpercent_Initial =0.4 * 'm'; 88 fl.Temperature_Initial = 338 * 'K'; 89 fl.Composition_Initial=0.1; 88 90 89 fl.OutletL.z(1) = 0.1; 90 fl.OutletL.z(2) = 0.1; 91 fl.OutletL.z(3) = 0.1; 92 fl.OutletL.z(4) = 0.1; 93 fl.OutletL.z(5) = 0.1; 94 95 OPTIONS 91 OPTIONS 96 92 Dynamic = true; 97 93 TimeStep = 0.1;
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