Changeset 110 for mso/eml/heat_exchangers/HEX_Engine.mso
- Timestamp:
- Jan 12, 2007, 4:44:02 PM (15 years ago)
- File:
-
- 1 edited
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mso/eml/heat_exchangers/HEX_Engine.mso
r100 r110 69 69 Hot as stream; # Inlet Hot Stream 70 70 Cold as stream; # Inlet Cold Stream 71 71 72 end 72 73 … … 78 79 Hot as stream_therm; # Outlet Hot Stream 79 80 Cold as stream_therm; # Outlet Cold Stream 81 80 82 end 81 83 … … 94 96 rho as dens_mass (Brief="Stream Density" ,Default=1000, Lower=1e-3, Upper=5e5); 95 97 Mu as viscosity (Brief="Stream Viscosity",Lower=0.0001); 96 Cp as cp_mol (Brief="Stream Molar Heat Capacity", Upper=1 0e10);98 Cp as cp_mol (Brief="Stream Molar Heat Capacity", Upper=1e10); 97 99 K as conductivity (Brief="Stream Thermal Conductivity", Default=1.0, Lower=1e-5, Upper=500); 100 98 101 end 99 102 … … 106 109 rho as dens_mass (Brief="Stream Density" ,Default=1000, Lower=1e-3, Upper=5e5); 107 110 Mu as viscosity (Brief="Stream Viscosity",Default=1, Lower=1e-5, Upper=1e5); 108 Cp as cp_mol (Brief="Stream Molar Heat Capacity", Upper=1 0e10);111 Cp as cp_mol (Brief="Stream Molar Heat Capacity", Upper=1e10); 109 112 K as conductivity (Brief="Stream Thermal Conductivity", Default=1.0, Lower=1e-5, Upper=500); 113 110 114 end 111 115 … … 116 120 VARIABLES 117 121 Mu as viscosity (Brief="Stream Viscosity",Default=1, Lower=1e-5, Upper=1e5); 118 Cp as cp_mol (Brief="Stream Molar Heat Capacity", Upper=1 0e10);122 Cp as cp_mol (Brief="Stream Molar Heat Capacity", Upper=1e10); 119 123 K as conductivity (Brief="Stream Thermal Conductivity", Default=1.0, Lower=1e-5, Upper=500); 120 124 Twall as temperature (Brief="Wall Temperature",Lower=50); 125 121 126 end 122 127 … … 130 135 Outlet as Properties_In_Out; # Properties at Outlet Stream 131 136 Wall as Properties_Wall; # Properties at Wall Temperature 137 132 138 end 133 139 … … 170 176 Phi as positive (Brief="Phi Correction",Default=1,Lower=1e-3); 171 177 Vtube as velocity (Brief="Tube Side Velocity",Lower=1e-8); 178 172 179 end 173 180 … … 231 238 #===================================================================== 232 239 VARIABLES 240 233 241 Rtube as positive (Brief="Tube Resistance",Unit="m^2*K/kW",Lower=1e-6); 234 242 Rwall as positive (Brief="Wall Resistance",Unit="m^2*K/kW",Lower=1e-6); … … 236 244 Rfi as positive (Brief="Inside Fouling Resistance",Unit="m^2*K/kW",Default=1e-6,Lower=0); 237 245 Rfo as positive (Brief="Outside Fouling Resistance",Unit="m^2*K/kW",Default=1e-6,Lower=0); 246 238 247 end 239 248 … … 257 266 "Number of Units Transference" 258 267 NTU*Cmin = Ud*A; 268 259 269 end 260 270 … … 266 276 PressureDrop as Tube_Pdrop; #Tube Side Pressure Drop 267 277 HeatTransfer as Tube_Heat_Transfer; #Tube Side Heat Transfer 278 268 279 end 269 280 … … 275 286 PressureDrop as Shell_Pdrop; # Shell Side Pressure Drop 276 287 HeatTransfer as Shell_Heat_Transfer; # Shell Side Heat Transfer 288 277 289 end 278 290 … … 284 296 Pdrop as press_delta (Brief="Pressure Drop",Default=0.01, Lower=0); 285 297 FPdrop as Real (Brief="Pressure Drop : Fraction of Inlet",Lower=0,Upper=0.8); 298 286 299 end 287 300 … … 293 306 Hot as Basic_Pdrop;# Hot Stream 294 307 Cold as Basic_Pdrop;# Cold Stream 308 295 309 end 296 310 … … 309 323 Phi as positive (Brief="Phi Correction",Default=1,Lower=1e-3); 310 324 Vmean as velocity (Brief="Tube Velocity",Lower=1e-8); 325 311 326 end 312 327 … … 322 337 fi as fricfactor (Brief="Friction Factor", Default=0.05, Lower=1e-10, Upper=2000); 323 338 Re as positive (Brief="Reynolds Number",Default=100,Lower=1); 339 324 340 end 325 341 … … 331 347 HeatTransfer as DoublePipe_HeatTransfer; 332 348 PressureDrop as DoublePipe_PressureDrop; 333 end 349 350 end
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