- Timestamp:
- Apr 3, 2008, 9:22:56 PM (15 years ago)
- File:
-
- 1 edited
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trunk/eml/costs/HeatExchangerSimplified_cost.mso
r331 r491 18 18 *------------------------------------------------------------------*# 19 19 20 using "heat_exchangers/Heat ExchangerSimplified";20 using "heat_exchangers/Heatex"; 21 21 22 22 # This model is valid if 14m^2 < A < 1100 m^2 23 23 24 Model HeatExchanger_LMTD_cost as Heat Exchanger_LMTD24 Model HeatExchanger_LMTD_cost as Heatex_LMTD 25 25 ATTRIBUTES 26 26 Pallete = true; … … 77 77 end 78 78 79 Model Shell_and_tubes_LMTD_cost as Shell_and_Tubes_LMTD79 Model Shell_and_tubes_LMTD_cost as Heatex_LMTD 80 80 ATTRIBUTES 81 81 Pallete = true; … … 98 98 Pmax as pressure (Brief="Average Pressure"); 99 99 100 EQUATIONS 101 "Average pressure" 102 Pmax = max( [HotSide.Properties.Average.P , ColdSide.Properties.Average.P] ); 103 104 "Capital Cost" 105 Ce = Cb*Fd*Fp*Fm; 106 107 "Basic Cost" 108 Cb = 'US$'*exp(Cost(1,1) + Cost(1,2)*ln(Details.A/'m^2') + Cost(1,3)*(ln(Details.A/'m^2'))^2); 109 110 "Cost Factor based on the type of the heat exchanger" 111 Fd = exp(Cost(2,1) + Cost(2,2)*ln(Details.A/'m^2') + Cost(2,3)*ln(Details.A/'m^2')); 112 113 if Pmax <= 700 * 'kPa' then 114 "Cost Factor based on the project pressure" # verificar 115 Fp = Cost(5,1) + Cost(5,2)*ln(Details.A/'m^2'); 116 else if 700 * 'kPa' < Pmax and Pmax < 2100 * 'kPa' then 117 Fp = Cost(5,1) + Cost(5,2)*ln(Details.A/'m^2'); 118 else if 2100 * 'kPa' < Pmax and Pmax < 4200 * 'kPa' then 119 Fp = Cost(6,1) + Cost(6,2)*ln(Details.A/'m^2'); 120 else if 4200 * 'kPa' < Pmax and Pmax < 6200 * 'kPa' then 121 Fp = Cost(7,1) + Cost(7,2)*ln(Details.A/'m^2'); 122 else 123 Fp = Cost(7,1) + Cost(7,2)*ln(Details.A/'m^2'); # verificar 124 end 125 end 126 end 127 end 128 129 "Cost Factor based on the construction material" 130 Fm = Cost(8,1) + Cost(8,2)*ln(Details.A/'m^2'); 131 132 end 133 134 Model HeatExchanger_NTU_cost as HeatExchanger_NTU 100 SET 101 102 ExchangerType = "Shell and Tube"; 103 104 EQUATIONS 105 "Average pressure" 106 Pmax = max( [HotSide.Properties.Average.P , ColdSide.Properties.Average.P] ); 107 108 "Capital Cost" 109 Ce = Cb*Fd*Fp*Fm; 110 111 "Basic Cost" 112 Cb = 'US$'*exp(Cost(1,1) + Cost(1,2)*ln(Details.A/'m^2') + Cost(1,3)*(ln(Details.A/'m^2'))^2); 113 114 "Cost Factor based on the type of the heat exchanger" 115 Fd = exp(Cost(2,1) + Cost(2,2)*ln(Details.A/'m^2') + Cost(2,3)*ln(Details.A/'m^2')); 116 117 if Pmax <= 700 * 'kPa' then 118 "Cost Factor based on the project pressure" # verificar 119 Fp = Cost(5,1) + Cost(5,2)*ln(Details.A/'m^2'); 120 else if 700 * 'kPa' < Pmax and Pmax < 2100 * 'kPa' then 121 Fp = Cost(5,1) + Cost(5,2)*ln(Details.A/'m^2'); 122 else if 2100 * 'kPa' < Pmax and Pmax < 4200 * 'kPa' then 123 Fp = Cost(6,1) + Cost(6,2)*ln(Details.A/'m^2'); 124 else if 4200 * 'kPa' < Pmax and Pmax < 6200 * 'kPa' then 125 Fp = Cost(7,1) + Cost(7,2)*ln(Details.A/'m^2'); 126 else 127 Fp = Cost(7,1) + Cost(7,2)*ln(Details.A/'m^2'); # verificar 128 end 129 end 130 end 131 end 132 133 "Cost Factor based on the construction material" 134 Fm = Cost(8,1) + Cost(8,2)*ln(Details.A/'m^2'); 135 136 end 137 138 Model HeatExchanger_NTU_cost as Heatex_NTU 135 139 ATTRIBUTES 136 140 Pallete = true; … … 187 191 end 188 192 189 Model Shell_and_tubes_NTU_cost as Shell_and_Tubes_NTU193 Model Shell_and_tubes_NTU_cost as Heatex_NTU 190 194 ATTRIBUTES 191 195 Pallete = true; … … 208 212 Pmax as pressure (Brief="Average Pressure"); 209 213 210 EQUATIONS 211 "Average pressure" 212 Pmax = max( [HotSide.Properties.Average.P , ColdSide.Properties.Average.P] ); 213 214 "Capital Cost" 215 Ce = Cb*Fd*Fp*Fm; 216 217 "Basic Cost" 218 Cb = 'US$'*exp(Cost(1,1) + Cost(1,2)*ln(Details.A/'m^2') + Cost(1,3)*(ln(Details.A/'m^2'))^2); 219 220 "Cost Factor based on the type of the heat exchanger" 221 Fd = exp(Cost(2,1) + Cost(2,2)*ln(Details.A/'m^2') + Cost(2,3)*ln(Details.A/'m^2')); 222 223 if Pmax <= 700 * 'kPa' then 224 "Cost Factor based on the project pressure" # verificar 225 Fp = Cost(5,1) + Cost(5,2)*ln(Details.A/'m^2'); 226 else if 700 * 'kPa' < Pmax and Pmax < 2100 * 'kPa' then 227 Fp = Cost(5,1) + Cost(5,2)*ln(Details.A/'m^2'); 228 else if 2100 * 'kPa' < Pmax and Pmax < 4200 * 'kPa' then 229 Fp = Cost(6,1) + Cost(6,2)*ln(Details.A/'m^2'); 230 else if 4200 * 'kPa' < Pmax and Pmax < 6200 * 'kPa' then 231 Fp = Cost(7,1) + Cost(7,2)*ln(Details.A/'m^2'); 232 else 233 Fp = Cost(7,1) + Cost(7,2)*ln(Details.A/'m^2'); # verificar 234 end 235 end 236 end 237 end 238 239 "Cost Factor based on the construction material" 240 Fm = Cost(8,1) + Cost(8,2)*ln(Details.A/'m^2'); 241 242 end 243 214 SET 215 216 ExchangerType = "Shell and Tube"; 217 218 EQUATIONS 219 "Average pressure" 220 Pmax = max( [HotSide.Properties.Average.P , ColdSide.Properties.Average.P] ); 221 222 "Capital Cost" 223 Ce = Cb*Fd*Fp*Fm; 224 225 "Basic Cost" 226 Cb = 'US$'*exp(Cost(1,1) + Cost(1,2)*ln(Details.A/'m^2') + Cost(1,3)*(ln(Details.A/'m^2'))^2); 227 228 "Cost Factor based on the type of the heat exchanger" 229 Fd = exp(Cost(2,1) + Cost(2,2)*ln(Details.A/'m^2') + Cost(2,3)*ln(Details.A/'m^2')); 230 231 if Pmax <= 700 * 'kPa' then 232 "Cost Factor based on the project pressure" # verificar 233 Fp = Cost(5,1) + Cost(5,2)*ln(Details.A/'m^2'); 234 else if 700 * 'kPa' < Pmax and Pmax < 2100 * 'kPa' then 235 Fp = Cost(5,1) + Cost(5,2)*ln(Details.A/'m^2'); 236 else if 2100 * 'kPa' < Pmax and Pmax < 4200 * 'kPa' then 237 Fp = Cost(6,1) + Cost(6,2)*ln(Details.A/'m^2'); 238 else if 4200 * 'kPa' < Pmax and Pmax < 6200 * 'kPa' then 239 Fp = Cost(7,1) + Cost(7,2)*ln(Details.A/'m^2'); 240 else 241 Fp = Cost(7,1) + Cost(7,2)*ln(Details.A/'m^2'); # verificar 242 end 243 end 244 end 245 end 246 247 "Cost Factor based on the construction material" 248 Fm = Cost(8,1) + Cost(8,2)*ln(Details.A/'m^2'); 249 250 end 251
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