[565] | 1 | #*------------------------------------------------------------------- |
---|
| 2 | * EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC. |
---|
| 3 | * |
---|
| 4 | * This LIBRARY is free software; you can distribute it and/or modify |
---|
| 5 | * it under the therms of the ALSOC FREE LICENSE as available at |
---|
| 6 | * http://www.enq.ufrgs.br/alsoc. |
---|
| 7 | * |
---|
| 8 | * EMSO Copyright (C) 2004 - 2007 ALSOC, original code |
---|
| 9 | * from http://www.rps.eng.br Copyright (C) 2002-2004. |
---|
| 10 | * All rights reserved. |
---|
| 11 | * |
---|
| 12 | * EMSO is distributed under the therms of the ALSOC LICENSE as |
---|
| 13 | * available at http://www.enq.ufrgs.br/alsoc. |
---|
| 14 | * |
---|
| 15 | *-------------------------------------------------------------------- |
---|
| 16 | * Author: Núbia do Carmo Ferreira |
---|
| 17 | * $Id: HeatExchangerDetailed.mso 197 2007-03-08 14:31:57Z bicca $ |
---|
| 18 | *------------------------------------------------------------------*# |
---|
| 19 | |
---|
| 20 | using "heat_exchangers/Heatex"; |
---|
| 21 | |
---|
| 22 | # This model is valid if 14m^2 < A < 1100 m^2 |
---|
| 23 | |
---|
| 24 | Model HeatExchanger_LMTD_cost as Heatex_LMTD |
---|
| 25 | ATTRIBUTES |
---|
| 26 | Pallete = true; |
---|
| 27 | Icon = "icon/HeatExchanger_LMTD"; |
---|
| 28 | Brief = "Heat Exchanger Block - LMTD Method"; |
---|
| 29 | Info = |
---|
| 30 | "to be documented."; |
---|
| 31 | |
---|
| 32 | PARAMETERS |
---|
| 33 | Material as Switcher (Valid = ["Stainless steel 316", "Stainless steel 304", "Stainless steel 347", "Nickel 200", "Monel 400", "Inconel 600", "Incoloy 825", "Titanium", "Hastelloy"], |
---|
| 34 | Default = "Stainless steel 316"); |
---|
| 35 | Cost(8,3) as Real; |
---|
| 36 | |
---|
| 37 | VARIABLES |
---|
| 38 | Ce as currency (Brief="Capital Cost"); |
---|
| 39 | Cb as currency (Brief="Basic Cost"); |
---|
| 40 | Fd as positive (Brief="Cost Factor based on the type of the heat exchanger"); |
---|
| 41 | Fp as positive (Brief="Cost Factor based on the project pressure"); |
---|
| 42 | Fm as positive (Brief="Cost Factor based on the construction material"); |
---|
| 43 | Pmax as pressure (Brief="Average Pressure"); |
---|
| 44 | |
---|
| 45 | EQUATIONS |
---|
| 46 | "Average pressure" |
---|
| 47 | Pmax = max( [(0.5*InletHot.P+0.5*OutletHot.P) , (0.5*InletCold.P+0.5*OutletCold.P)] ); |
---|
| 48 | |
---|
| 49 | |
---|
| 50 | "Capital Cost" |
---|
| 51 | Ce = Cb*Fd*Fp*Fm; |
---|
| 52 | |
---|
| 53 | "Basic Cost" |
---|
| 54 | Cb = 'US$'*exp(Cost(1,1) + Cost(1,2)*ln(A/'m^2') + Cost(1,3)*(ln(A/'m^2'))^2); |
---|
| 55 | |
---|
| 56 | "Cost Factor based on the type of the heat exchanger" |
---|
| 57 | Fd = exp(Cost(2,1) + Cost(2,2)*ln(A/'m^2') + Cost(2,3)*ln(A/'m^2')); |
---|
| 58 | |
---|
| 59 | if Pmax <= 700 * 'kPa' then |
---|
| 60 | "Cost Factor based on the project pressure" # verificar |
---|
| 61 | Fp = Cost(5,1) + Cost(5,2)*ln(A/'m^2'); |
---|
| 62 | else if 700 * 'kPa' < Pmax and Pmax < 2100 * 'kPa' then |
---|
| 63 | Fp = Cost(5,1) + Cost(5,2)*ln(A/'m^2'); |
---|
| 64 | else if 2100 * 'kPa' < Pmax and Pmax < 4200 * 'kPa' then |
---|
| 65 | Fp = Cost(6,1) + Cost(6,2)*ln(A/'m^2'); |
---|
| 66 | else if 4200 * 'kPa' < Pmax and Pmax < 6200 * 'kPa' then |
---|
| 67 | Fp = Cost(7,1) + Cost(7,2)*ln(A/'m^2'); |
---|
| 68 | else |
---|
| 69 | Fp = Cost(7,1) + Cost(7,2)*ln(A/'m^2'); # verificar |
---|
| 70 | end |
---|
| 71 | end |
---|
| 72 | end |
---|
| 73 | end |
---|
| 74 | |
---|
| 75 | "Cost Factor based on the construction material" |
---|
| 76 | Fm = Cost(8,1) + Cost(8,2)*ln(A/'m^2'); |
---|
| 77 | |
---|
| 78 | end |
---|
| 79 | |
---|
| 80 | Model Shell_and_tubes_LMTD_cost as Heatex_LMTD |
---|
| 81 | ATTRIBUTES |
---|
| 82 | Pallete = true; |
---|
| 83 | Icon = "icon/Shell_and_Tubes_LMTD"; |
---|
| 84 | Brief = "Shell and Tubes Heat Exchanger with 1 or 2 shell pass - LMTD Method"; |
---|
| 85 | Info = |
---|
| 86 | "to be documented."; |
---|
| 87 | |
---|
| 88 | PARAMETERS |
---|
| 89 | Material as Switcher (Valid = ["Stainless steel 316", "Stainless steel 304", "Stainless steel 347", "Nickel 200", "Monel 400", "Inconel 600", "Incoloy 825", "Titanium", "Hastelloy"], |
---|
| 90 | Default = "Stainless steel 316"); |
---|
| 91 | Cost(8,3) as Real; |
---|
| 92 | |
---|
| 93 | VARIABLES |
---|
| 94 | Ce as currency (Brief="Capital Cost"); |
---|
| 95 | Cb as currency (Brief="Basic Cost"); |
---|
| 96 | Fd as positive (Brief="Cost Factor based on the type of the heat exchanger"); |
---|
| 97 | Fp as positive (Brief="Cost Factor based on the project pressure"); |
---|
| 98 | Fm as positive (Brief="Cost Factor based on the construction material"); |
---|
| 99 | Pmax as pressure (Brief="Average Pressure"); |
---|
| 100 | |
---|
| 101 | SET |
---|
| 102 | |
---|
| 103 | ExchangerType = "Shell and Tube"; |
---|
| 104 | |
---|
| 105 | EQUATIONS |
---|
| 106 | "Average pressure" |
---|
| 107 | Pmax = max( [(0.5*InletHot.P+0.5*OutletHot.P) , (0.5*InletCold.P+0.5*OutletCold.P)] ); |
---|
| 108 | |
---|
| 109 | "Capital Cost" |
---|
| 110 | Ce = Cb*Fd*Fp*Fm; |
---|
| 111 | |
---|
| 112 | "Basic Cost" |
---|
| 113 | Cb = 'US$'*exp(Cost(1,1) + Cost(1,2)*ln(A/'m^2') + Cost(1,3)*(ln(A/'m^2'))^2); |
---|
| 114 | |
---|
| 115 | "Cost Factor based on the type of the heat exchanger" |
---|
| 116 | Fd = exp(Cost(2,1) + Cost(2,2)*ln(A/'m^2') + Cost(2,3)*ln(A/'m^2')); |
---|
| 117 | |
---|
| 118 | if Pmax <= 700 * 'kPa' then |
---|
| 119 | "Cost Factor based on the project pressure" # verificar |
---|
| 120 | Fp = Cost(5,1) + Cost(5,2)*ln(A/'m^2'); |
---|
| 121 | else if 700 * 'kPa' < Pmax and Pmax < 2100 * 'kPa' then |
---|
| 122 | Fp = Cost(5,1) + Cost(5,2)*ln(A/'m^2'); |
---|
| 123 | else if 2100 * 'kPa' < Pmax and Pmax < 4200 * 'kPa' then |
---|
| 124 | Fp = Cost(6,1) + Cost(6,2)*ln(A/'m^2'); |
---|
| 125 | else if 4200 * 'kPa' < Pmax and Pmax < 6200 * 'kPa' then |
---|
| 126 | Fp = Cost(7,1) + Cost(7,2)*ln(A/'m^2'); |
---|
| 127 | else |
---|
| 128 | Fp = Cost(7,1) + Cost(7,2)*ln(A/'m^2'); # verificar |
---|
| 129 | end |
---|
| 130 | end |
---|
| 131 | end |
---|
| 132 | end |
---|
| 133 | |
---|
| 134 | "Cost Factor based on the construction material" |
---|
| 135 | Fm = Cost(8,1) + Cost(8,2)*ln(A/'m^2'); |
---|
| 136 | |
---|
| 137 | end |
---|
| 138 | |
---|
| 139 | Model HeatExchanger_NTU_cost as Heatex_NTU |
---|
| 140 | ATTRIBUTES |
---|
| 141 | Pallete = true; |
---|
| 142 | Icon = "icon/HeatExchanger_NTU"; |
---|
| 143 | Brief = "Heat Exchanger Block - NTU Method"; |
---|
| 144 | Info = |
---|
| 145 | "to be documented."; |
---|
| 146 | |
---|
| 147 | PARAMETERS |
---|
| 148 | Material as Switcher (Valid = ["Stainless steel 316", "Stainless steel 304", "Stainless steel 347", "Nickel 200", "Monel 400", "Inconel 600", "Incoloy 825", "Titanium", "Hastelloy"], |
---|
| 149 | Default = "Stainless steel 316"); |
---|
| 150 | Cost(8,3) as Real; |
---|
| 151 | |
---|
| 152 | VARIABLES |
---|
| 153 | Ce as currency (Brief="Capital Cost"); |
---|
| 154 | Cb as currency (Brief="Basic Cost"); |
---|
| 155 | Fd as positive (Brief="Cost Factor based on the type of the heat exchanger"); |
---|
| 156 | Fp as positive (Brief="Cost Factor based on the project pressure"); |
---|
| 157 | Fm as positive (Brief="Cost Factor based on the construction material"); |
---|
| 158 | Pmax as pressure (Brief="Average Pressure"); |
---|
| 159 | |
---|
| 160 | EQUATIONS |
---|
| 161 | "Average pressure" |
---|
| 162 | Pmax = max( [(0.5*InletHot.P+0.5*OutletHot.P) , (0.5*InletCold.P+0.5*OutletCold.P)] ); |
---|
| 163 | |
---|
| 164 | "Capital Cost" |
---|
| 165 | Ce = Cb*Fd*Fp*Fm; |
---|
| 166 | |
---|
| 167 | "Basic Cost" |
---|
| 168 | Cb = 'US$'*exp(Cost(1,1) + Cost(1,2)*ln(A/'m^2') + Cost(1,3)*(ln(A/'m^2'))^2); |
---|
| 169 | |
---|
| 170 | "Cost Factor based on the type of the heat exchanger" |
---|
| 171 | Fd = exp(Cost(2,1) + Cost(2,2)*ln(A/'m^2') + Cost(2,3)*ln(A/'m^2')); |
---|
| 172 | |
---|
| 173 | if Pmax <= 700 * 'kPa' then |
---|
| 174 | "Cost Factor based on the project pressure" # verificar |
---|
| 175 | Fp = Cost(5,1) + Cost(5,2)*ln(A/'m^2'); |
---|
| 176 | else if 700 * 'kPa' < Pmax and Pmax < 2100 * 'kPa' then |
---|
| 177 | Fp = Cost(5,1) + Cost(5,2)*ln(A/'m^2'); |
---|
| 178 | else if 2100 * 'kPa' < Pmax and Pmax < 4200 * 'kPa' then |
---|
| 179 | Fp = Cost(6,1) + Cost(6,2)*ln(A/'m^2'); |
---|
| 180 | else if 4200 * 'kPa' < Pmax and Pmax < 6200 * 'kPa' then |
---|
| 181 | Fp = Cost(7,1) + Cost(7,2)*ln(A/'m^2'); |
---|
| 182 | else |
---|
| 183 | Fp = Cost(7,1) + Cost(7,2)*ln(A/'m^2'); # verificar |
---|
| 184 | end |
---|
| 185 | end |
---|
| 186 | end |
---|
| 187 | end |
---|
| 188 | |
---|
| 189 | "Cost Factor based on the construction material" |
---|
| 190 | Fm = Cost(8,1) + Cost(8,2)*ln(A/'m^2'); |
---|
| 191 | |
---|
| 192 | end |
---|
| 193 | |
---|
| 194 | Model Shell_and_tubes_NTU_cost as Heatex_NTU |
---|
| 195 | ATTRIBUTES |
---|
| 196 | Pallete = true; |
---|
| 197 | Icon = "icon/Shell_and_Tubes_NTU"; |
---|
| 198 | Brief = "Shell and Tubes Heat Exchanger with 1 or 2 shell pass - NTU Method"; |
---|
| 199 | Info = |
---|
| 200 | "to be documented."; |
---|
| 201 | |
---|
| 202 | PARAMETERS |
---|
| 203 | Material as Switcher (Valid = ["Stainless steel 316", "Stainless steel 304", "Stainless steel 347", "Nickel 200", "Monel 400", "Inconel 600", "Incoloy 825", "Titanium", "Hastelloy"], |
---|
| 204 | Default = "Stainless steel 316"); |
---|
| 205 | Cost(8,3) as Real; |
---|
| 206 | |
---|
| 207 | VARIABLES |
---|
| 208 | Ce as currency (Brief="Capital Cost"); |
---|
| 209 | Cb as currency (Brief="Basic Cost"); |
---|
| 210 | Fd as positive (Brief="Cost Factor based on the type of the heat exchanger"); |
---|
| 211 | Fp as positive (Brief="Cost Factor based on the project pressure"); |
---|
| 212 | Fm as positive (Brief="Cost Factor based on the construction material"); |
---|
| 213 | Pmax as pressure (Brief="Average Pressure"); |
---|
| 214 | |
---|
| 215 | SET |
---|
| 216 | |
---|
| 217 | ExchangerType = "Shell and Tube"; |
---|
| 218 | |
---|
| 219 | EQUATIONS |
---|
| 220 | "Average pressure" |
---|
| 221 | Pmax = max( [(0.5*InletHot.P+0.5*OutletHot.P) , (0.5*InletCold.P+0.5*OutletCold.P)] ); |
---|
| 222 | |
---|
| 223 | "Capital Cost" |
---|
| 224 | Ce = Cb*Fd*Fp*Fm; |
---|
| 225 | |
---|
| 226 | "Basic Cost" |
---|
| 227 | Cb = 'US$'*exp(Cost(1,1) + Cost(1,2)*ln(A/'m^2') + Cost(1,3)*(ln(A/'m^2'))^2); |
---|
| 228 | |
---|
| 229 | "Cost Factor based on the type of the heat exchanger" |
---|
| 230 | Fd = exp(Cost(2,1) + Cost(2,2)*ln(A/'m^2') + Cost(2,3)*ln(A/'m^2')); |
---|
| 231 | |
---|
| 232 | if Pmax <= 700 * 'kPa' then |
---|
| 233 | "Cost Factor based on the project pressure" # verificar |
---|
| 234 | Fp = Cost(5,1) + Cost(5,2)*ln(A/'m^2'); |
---|
| 235 | else if 700 * 'kPa' < Pmax and Pmax < 2100 * 'kPa' then |
---|
| 236 | Fp = Cost(5,1) + Cost(5,2)*ln(A/'m^2'); |
---|
| 237 | else if 2100 * 'kPa' < Pmax and Pmax < 4200 * 'kPa' then |
---|
| 238 | Fp = Cost(6,1) + Cost(6,2)*ln(A/'m^2'); |
---|
| 239 | else if 4200 * 'kPa' < Pmax and Pmax < 6200 * 'kPa' then |
---|
| 240 | Fp = Cost(7,1) + Cost(7,2)*ln(A/'m^2'); |
---|
| 241 | else |
---|
| 242 | Fp = Cost(7,1) + Cost(7,2)*ln(A/'m^2'); # verificar |
---|
| 243 | end |
---|
| 244 | end |
---|
| 245 | end |
---|
| 246 | end |
---|
| 247 | |
---|
| 248 | "Cost Factor based on the construction material" |
---|
| 249 | Fm = Cost(8,1) + Cost(8,2)*ln(A/'m^2'); |
---|
| 250 | |
---|
| 251 | end |
---|
| 252 | |
---|