Changeset 522 for trunk/sample/stage_separators/sample_tray.mso
- Timestamp:
- May 21, 2008, 8:21:12 PM (15 years ago)
- File:
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- 1 edited
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trunk/sample/stage_separators/sample_tray.mso
r514 r522 220 220 TimeEnd = 100; 221 221 end 222 223 FlowSheet trayRate_Test 224 PARAMETERS 225 PP as Plugin(Brief="Physical Properties", 226 Type="PP", 227 Components = [ "n-pentane", "benzene"], 228 LiquidModel = "PR", 229 VapourModel = "PR" 230 ); 231 NComp as Integer; 232 233 SET 234 NComp = PP.NumberOfComponents; 235 236 DEVICES 237 t1 as trayRate; 238 feed as source; 239 feedV as source; 240 inL as liquid_stream; 241 inV as vapour_stream; 242 243 CONNECTIONS 244 feed.Outlet to t1.Inlet; 245 feedV.Outlet to t1.InletFV; 246 inL to t1.InletL; 247 inV to t1.InletV; 248 249 SPECIFY 250 feed.Outlet.F = 116 * 'kmol/h'; 251 feed.Outlet.T = 280 * 'K'; 252 feed.Outlet.P = 150 * 'kPa'; 253 feed.Outlet.z = [0.5, 0.5]; 254 255 feedV.Outlet.F = 0 * 'kmol/h'; 256 feedV.Outlet.T = 280 * 'K'; 257 feedV.Outlet.P = 150 * 'atm'; 258 feedV.Outlet.z = [0.5, 0.5]; 259 260 inL.P = 150 * 'kPa'; 261 inL.T = 290 * 'K'; 262 inL.F = 90 * 'kmol/h'; 263 inL.z = [0.1641, 0.8359]; 264 265 inV.P = 150 * 'kPa'; 266 inV.T = 500 * 'K'; 267 inV.z = [0.0584, 0.9416]; 268 # inV.F = 62 * 'kmol/h'; 269 270 t1.OutletV.F = 120 * 'kmol/h'; 271 # t1.OutletL.F = 120 * 'kmol/h'; 272 t1.interf.a = 40 * 'm^2'; 273 t1.interf.htL = 10.01 * 'kW/m^2/K'; 274 t1.interf.htV = 0.025 * 'kW/m^2/K'; 275 t1.interf.kL = 0.00933 * 'm/s'; 276 t1.interf.kV = 0.000236 * 'm/s'; 277 278 SET 279 t1.V = 4 * 'ft^3'; 280 t1.Ah = 0.394 * 'ft^2'; 281 t1.lw = 20.94 * 'in'; 282 t1.hw = 0.125 * 'ft'; 283 t1.beta = 0.6; 284 t1.alfa = 4; 285 t1.Ap = 3.94 * 'ft^2'; 286 t1.Q = 0 * 'kW'; 287 288 INITIAL 289 t1.OutletL.T = 295 *'K'; 290 t1.OutletV.T = 290 *'K'; 291 t1.Level = 0.9 * t1.hw; 292 t1.OutletL.z(1) = 0.5; 293 t1.OutletV.z(1) = 0.6; 294 t1.MV = 1.0*'mol' ; 295 296 OPTIONS 297 TimeStep = 0.1; 298 TimeEnd = 10; 299 TimeUnit = 's'; 300 GuessFile = "trayRate_Test.rlt"; 301 end
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