Changeset 910
- Timestamp:
- Feb 20, 2010, 1:24:41 AM (12 years ago)
- Location:
- branches/gui
- Files:
-
- 1 deleted
- 6 edited
-
eml/mixers_splitters/splitter.mso (modified) (1 diff)
-
eml/stage_separators/column.mso (modified) (1 diff)
-
sample/controllers/Column_MPID.rlt (modified) (43 diffs)
-
sample/controllers/Column_ctrl.rlt (deleted)
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sample/controllers/sample_PIDIncr_MIMO.mso (modified) (7 diffs)
-
sample/controllers/sample_PID_MIMO.mso (modified) (8 diffs)
-
sample/controllers/sample_tanks_pid.mso (modified) (5 diffs)
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/mixers_splitters/splitter.mso
r838 r910 249 249 SplitFlow_RefluxStream as fraction (Brief = "split of the outlet Reflux stream", Default=0.33); 250 250 SplitFlow_DistillateStream as fraction (Brief = "split of the outlet Distillate stream", Default=0.33); 251 RefluxRatio as positive (Brief = "Reflux Ratio", Default=10, Lower = 0. 5);251 RefluxRatio as positive (Brief = "Reflux Ratio", Default=10, Lower = 0.05); 252 252 253 253 EQUATIONS -
branches/gui/eml/stage_separators/column.mso
r901 r910 35 35 using "condenser"; 36 36 using "mixers_splitters/splitter"; 37 using "tank";38 37 using "pressure_changers/pump"; 39 38 -
branches/gui/sample/controllers/Column_MPID.rlt
r342 r910 1 1 Column_MPID 2 2 0 362 2 0 18000 3 3 Column_MPID 4 4 0 0 5 5 6 45 6 30 7 7 NComp 8 8 1 1 2 5 5 0 9 9 10 10 0 11 Qcmin12 1 1 2 -1.38889e+006 -1.38889e+006 013 14 015 Qcmax16 1 1 2 -138889 -138889 017 18 019 11 Qrmin 20 1 1 2 277 778 277778 012 1 1 2 277.778 277.778 0 21 13 22 14 0 23 15 Qrmax 24 1 1 2 1.38889e+006 1.38889e+006 0 25 26 0 27 Frmin 28 1 1 2 0 0 0 29 30 0 31 Frmax 32 1 1 2 60 60 0 33 34 0 35 Fcmin 36 1 1 2 0 0 0 37 38 0 39 Fcmax 40 1 1 2 120 120 0 41 42 0 43 Hmint 44 1 1 2 0 0 0 45 46 0 47 Hmaxt 48 1 1 2 2 2 0 49 50 0 51 Hminb 52 1 1 2 0 0 0 53 54 0 55 Hmaxb 56 1 1 2 2 2 0 57 58 0 59 Pmax 60 1 1 2 9.86923 9.86923 0 61 62 0 63 Pmin 64 1 1 2 0.493462 0.493462 0 65 66 0 67 Tmax 68 1 1 2 303.15 303.15 0 69 70 0 71 Tmin 72 1 1 2 253.15 253.15 0 16 1 1 2 1388.89 1388.89 0 73 17 74 18 0 … … 88 32 1 89 33 OutletQ 90 0 1 91 energy_stream 92 0 0 93 94 1 95 Q 96 1 1 2 -138889 -138889 0 97 98 0 34 1 1 2 -763.889 -829.524 0 99 35 100 36 0 … … 108 44 1 109 45 OutletQ 110 0 1 111 energy_stream 112 0 0 113 114 1 115 Q 116 1 1 2 2.5e+006 1.83417e+006 0 117 118 0 119 120 0 121 122 0 123 Had_top 124 1 1 2 0.5 0.381277 0 125 126 0 127 Had_bot 128 1 1 2 0.5 0.608179 0 129 130 0 131 Pad 132 1 1 2 0.157895 0.252819 0 46 1 1 2 899.993 994.695 0 47 48 0 133 49 134 50 0 … … 137 53 138 54 0 139 Tad140 1 1 2 0.7 0.920007 0141 142 0143 55 T_sp 144 56 1 1 2 288.15 288.15 0 … … 146 58 0 147 59 RR 148 1 1 2 9.9 4.52278060 1 1 2 0.979036 0.717312 0 149 61 150 62 0 151 63 LC_sp 152 1 1 2 1 1064 1 1 2 0.5 0.5 0 153 65 154 66 0 155 67 LR_sp 156 1 1 2 1 1068 1 1 2 0.5 0.5 0 157 69 158 70 0 159 71 xtop 160 1 1 2 0.0 02431 0.00223881072 1 1 2 0.05 0.000939896 0 161 73 162 74 0 163 75 xbot 164 1 1 2 1.06721e-006 0.000168876076 1 1 2 0.1 9.71358e-005 0 165 77 166 78 0 … … 175 87 col 176 88 0 1 177 Distillation_kettle_cond 178 0 0 179 180 10 181 NComp 182 0 0 183 184 0 185 NTrays 89 Section_Column 90 0 1 91 SectionColumnBasic 92 0 0 93 94 34 95 NComp 96 0 0 97 98 0 99 NumberOfFeeds 100 1 1 2 1 1 0 101 102 0 103 FeedTrayLocation 104 1 3 2 5 5 2 2 2 2 2 2 0 105 106 0 107 NumberOfTrays 186 108 1 1 2 8 8 0 187 109 188 110 0 189 topdown 190 1 1 2 1 1 0 191 192 0 193 top 194 1 1 2 1 1 0 195 196 0 197 bot 198 1 1 2 8 8 0 199 200 0 201 trays 111 LiqSideTrayIndex 112 1 8 2 0 0 2 1 1 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 0 113 114 0 115 VapSideTrayIndex 116 1 8 2 0 0 2 1 1 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 0 117 118 0 119 LiquidSideStreamLocation 120 1 1 2 2 2 0 121 122 0 123 VapourSideStreamLocation 124 1 1 2 2 2 0 125 126 0 127 TrayDiameter 128 1 1 2 1.6 1.6 0 129 130 0 131 TraySpacing 132 1 1 2 0.6 0.6 0 133 134 0 135 Fraction_HoleArea 136 1 1 2 0.1 0.1 0 137 138 0 139 Fraction_DowncomerArea 140 1 1 2 0.2 0.2 0 141 142 0 143 WeirLength 144 1 1 2 0.531876 0.531876 0 145 146 0 147 WeirHeight 148 1 1 2 0.0381 0.0381 0 149 150 0 151 TrayLiquidPasses 152 1 1 2 1 1 0 153 154 0 155 HeatSupply 156 1 1 2 0 0 0 157 158 0 159 AerationFraction 160 1 1 2 0.6 0.6 0 161 162 0 163 DryPdropCoeff 164 1 1 2 4 4 0 165 166 0 167 MurphreeEff 168 1 1 2 1 1 0 169 170 0 171 INITIALIZATION 172 0 1 173 InitializeSection 174 0 0 175 176 6 177 NComp 178 1 1 2 1 1 0 179 180 0 181 TopTemperature 182 1 1 2 290 290 0 183 184 0 185 BottomTemperature 186 1 1 2 330 330 0 187 188 0 189 LevelFraction 190 1 1 2 0.1 0.1 0 191 192 0 193 TopComposition 194 1 5 2 0.2 0.2 2 0.2 0.2 2 0.4 0.4 2 0.05 0.05 2 0.15 0.15 0 195 196 0 197 BottomComposition 198 1 5 2 0.1 0.1 2 0.4 0.4 2 0.1 0.1 2 0.3 0.3 2 0.1 0.1 0 199 200 0 201 202 0 203 CONTROL 204 0 1 205 ControlSection 206 0 0 207 208 5 209 NComp 210 0 0 211 212 0 213 Tindicator_TrayNumber 214 1 1 2 1 1 0 215 216 0 217 Pindicator_TrayNumber 218 1 1 2 1 1 0 219 220 0 221 zindicator_TrayNumber 222 1 1 2 1 1 0 223 224 0 225 zindicator_Component 226 1 1 2 1 1 0 227 228 0 229 230 0 231 TCI 232 1 1 2 290 327.831 0 233 234 0 235 PCI 236 1 1 2 4.44588 6.47643 0 237 238 0 239 LiquidInlet 240 0 1 241 stream 242 0 0 243 244 7 245 NComp 246 0 0 247 248 0 249 F 250 1 1 2 58.7421 54.9199 0 251 252 0 253 T 254 1 1 2 259.994 288.154 0 255 256 0 257 P 258 1 1 2 1.95797 4.04365 0 259 260 0 261 h 262 1 1 2 -25185.7 -21158.3 0 263 264 0 265 v 266 1 1 2 0 0 0 267 268 0 269 z 270 1 5 2 0.2 0.294992 2 0.2 0.113679 2 0.4 0.296382 2 0.05 0.000939896 2 0.15 0.294007 0 271 272 0 273 274 0 275 VapourOutlet 276 0 1 277 vapour_stream 278 0 1 279 stream 280 0 0 281 282 7 283 NComp 284 0 0 285 286 0 287 F 288 1 1 2 124.191 131.478 0 289 290 0 291 T 292 1 1 2 290 327.831 0 293 294 0 295 P 296 1 1 2 4.44588 6.47643 0 297 298 0 299 h 300 1 1 2 -1301.67 1553.42 0 301 302 0 303 v 304 1 1 2 1 1 0 305 306 0 307 z 308 1 5 2 0.129182 0.294931 2 0.0268093 0.113854 2 0.758442 0.296326 2 0.00190025 0.000942317 2 0.083666 0.293946 0 309 310 0 311 312 0 313 314 0 315 VapourDrawOff 316 0 1 317 vapour_stream 318 0 1 319 stream 320 0 0 321 322 7 323 NComp 324 0 0 325 326 0 327 F 328 1 1 2 0 0 0 329 330 0 331 T 332 1 1 2 295.714 338.341 0 333 334 0 335 P 336 1 1 2 4.68273 6.4767 0 337 338 0 339 h 340 1 1 2 -923.748 2707.62 0 341 342 0 343 v 344 1 1 2 1 1 0 345 346 0 347 z 348 1 5 2 0.134924 0.279466 2 0.0360305 0.210389 2 0.735505 0.216813 2 0.00386346 0.00372388 2 0.0896774 0.289608 0 349 350 0 351 352 0 353 354 0 355 LiquidDrawOff 356 0 1 357 liquid_stream 358 0 1 359 stream 360 0 0 361 362 7 363 NComp 364 0 0 365 366 0 367 F 368 1 1 2 0 0 0 369 370 0 371 T 372 1 1 2 295.714 338.341 0 373 374 0 375 P 376 1 1 2 4.68273 6.4767 0 377 378 0 379 h 380 1 1 2 -21659.1 -17302.5 0 381 382 0 383 v 384 1 1 2 0 0 0 385 386 0 387 z 388 1 5 2 0.185714 0.199851 2 0.228571 0.48354 2 0.357143 0.0677287 2 0.0857143 0.0219601 2 0.142857 0.22692 0 389 390 0 391 392 0 393 394 0 395 TRAYS 202 396 0 1 203 397 tray 204 0 1 205 trayBasic 206 0 0 207 208 18 209 NComp 210 0 0 211 212 0 213 V 214 1 8 2 0.113267 0.113267 2 0.113267 0.113267 2 0.113267 0.113267 2 0.113267 0.113267 2 0.113267 0.113267 2 0.113267 0.113267 2 0.113267 0.113267 2 0.113267 0.113267 0 215 216 0 217 Q 398 0 0 399 400 42 401 NComp 402 1 8 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 0 403 404 0 405 Mw 406 2 8 5 2 58.123 58.123 2 72.1498 72.1498 2 42.0804 42.0804 2 78.1134 78.1134 2 56.1072 56.1072 2 58.123 58.123 2 72.1498 72.1498 2 42.0804 42.0804 2 78.1134 78.1134 2 56.1072 56.1072 2 58.123 58.123 2 72.1498 72.1498 2 42.0804 42.0804 2 78.1134 78.1134 2 56.1072 56.1072 2 58.123 58.123 2 72.1498 72.1498 2 42.0804 42.0804 2 78.1134 78.1134 2 56.1072 56.1072 2 58.123 58.123 2 72.1498 72.1498 2 42.0804 42.0804 2 78.1134 78.1134 2 56.1072 56.1072 2 58.123 58.123 2 72.1498 72.1498 2 42.0804 42.0804 2 78.1134 78.1134 2 56.1072 56.1072 2 58.123 58.123 2 72.1498 72.1498 2 42.0804 42.0804 2 78.1134 78.1134 2 56.1072 56.1072 2 58.123 58.123 2 72.1498 72.1498 2 42.0804 42.0804 2 78.1134 78.1134 2 56.1072 56.1072 0 407 408 0 409 Gconst 410 1 8 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 0 411 412 0 413 zero_flow 218 414 1 8 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 0 219 415 220 416 0 221 Ap 222 1 8 2 0.366038 0.366038 2 0.366038 0.366038 2 0.366038 0.366038 2 0.366038 0.366038 2 0.366038 0.366038 2 0.366038 0.366038 2 0.366038 0.366038 2 0.366038 0.366038 0 417 low_flow 418 1 8 2 1e-006 1e-006 2 1e-006 1e-006 2 1e-006 1e-006 2 1e-006 1e-006 2 1e-006 1e-006 2 1e-006 1e-006 2 1e-006 1e-006 2 1e-006 1e-006 0 419 420 0 421 Pi 422 1 8 2 3.14159 3.14159 2 3.14159 3.14159 2 3.14159 3.14159 2 3.14159 3.14159 2 3.14159 3.14159 2 3.14159 3.14159 2 3.14159 3.14159 2 3.14159 3.14159 0 423 424 0 425 TrayDiameter_ 426 1 8 2 1.6 1.6 2 1.6 1.6 2 1.6 1.6 2 1.6 1.6 2 1.6 1.6 2 1.6 1.6 2 1.6 1.6 2 1.6 1.6 0 427 428 0 429 TraySpacing_ 430 1 8 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 0 431 432 0 433 Fraction_HoleArea_ 434 1 8 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 0 435 436 0 437 Fraction_DowncomerArea_ 438 1 8 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 0 439 440 0 441 WeirLength_ 442 1 8 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 0 443 444 0 445 WeirHeight_ 446 1 8 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 0 447 448 0 449 TrayLiquidPasses_ 450 1 8 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 0 451 452 0 453 HeatSupply_ 454 1 8 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 0 455 456 0 457 AerationFraction_ 458 1 8 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 0 459 460 0 461 DryPdropCoeff_ 462 1 8 2 4 4 2 4 4 2 4 4 2 4 4 2 4 4 2 4 4 2 4 4 2 4 4 0 463 464 0 465 MurphreeEff_ 466 1 8 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 0 467 468 0 469 PlateArea_ 470 1 8 2 1.6085 1.6085 2 1.6085 1.6085 2 1.6085 1.6085 2 1.6085 1.6085 2 1.6085 1.6085 2 1.6085 1.6085 2 1.6085 1.6085 2 1.6085 1.6085 0 471 472 0 473 TrayVolume_ 474 1 8 2 1.20637 1.20637 2 1.20637 1.20637 2 1.20637 1.20637 2 1.20637 1.20637 2 1.20637 1.20637 2 1.20637 1.20637 2 1.20637 1.20637 2 1.20637 1.20637 0 475 476 0 477 HolesArea_ 478 1 8 2 0.201062 0.201062 2 0.201062 0.201062 2 0.201062 0.201062 2 0.201062 0.201062 2 0.201062 0.201062 2 0.201062 0.201062 2 0.201062 0.201062 2 0.201062 0.201062 0 479 480 0 481 FeeheryCoeff 482 1 8 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 0 483 484 0 485 ElgueCoeff 486 1 8 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 0 487 488 0 489 OlsenCoeff 490 1 8 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 0 223 491 224 492 0 … … 245 513 246 514 0 247 z248 2 8 5 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 0249 250 0251 515 h 252 516 1 8 2 0 0 2 0 0 2 0 0 2 0 0 2 -24198.8 -24198.8 2 0 0 2 0 0 2 0 0 0 … … 254 518 0 255 519 v 520 1 8 2 0 0 2 0 0 2 0 0 2 0 0 2 -6.65306e-111 -4.95446e-021 2 0 0 2 0 0 2 0 0 0 521 522 0 523 z 524 2 8 5 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 2 0.1 0.1 0 525 526 0 527 528 0 529 LiquidSideStream 530 0 1 531 liquid_stream 532 0 1 533 stream 534 0 0 535 536 7 537 NComp 538 0 0 539 540 0 541 F 256 542 1 8 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 0 257 543 258 544 0 259 260 0261 InletL262 0 1263 stream264 0 0265 266 7267 NComp268 0 0269 270 0271 F272 1 8 2 2376 345.075 2 67.8376 349.617 2 67.0609 353.231 2 65.5297 355.838 2 62.6417 356.782 2 130.414 472.324 2 130.902 471.872 2 127.243 464.261 0273 274 0275 545 T 276 1 8 2 2 88.145 299.146 2 306.076 301.474 2 312.389 303.297 2 315.118 304.825 2 317.688 306.208 2 321.671 308.163 2 338.59 314.811 2 350.145 323.811 0546 1 8 2 290 327.831 2 295.714 338.341 2 301.429 343.771 2 307.143 347.241 2 312.857 350.581 2 318.571 367.842 2 324.286 379.355 2 330 388.631 0 277 547 278 548 0 279 549 P 280 1 8 2 2.13175 3.02174 2 1.99474 2.87939 2 2.01567 2.89602 2 2.03637 2.91353 2 2.05656 2.93172 2 2.07768 2.95093 2 2.08882 2.97206 2 2.10072 2.99507 0 281 282 0 283 z 284 2 8 5 2 0.216067 0.225278 2 0.453839 0.427493 2 0.0889142 0.0993579 2 0.002431 0.00223881 2 0.238749 0.245633 2 0.115517 0.232212 2 0.704422 0.43261 2 0.0318101 0.0784609 2 0.011216 0.00224445 2 0.137036 0.254473 2 0.0816194 0.233421 2 0.766618 0.440952 2 0.0247083 0.0649518 2 0.0300791 0.0022818 2 0.0969754 0.258393 2 0.0712076 0.229804 2 0.751719 0.453588 2 0.0232357 0.0567608 2 0.0699815 0.00255721 2 0.0838566 0.25729 2 0.0654303 0.223257 2 0.684741 0.46677 2 0.022213 0.0519626 2 0.150489 0.00579214 2 0.077127 0.252218 2 0.0581338 0.212259 2 0.559295 0.443231 2 0.0206085 0.048523 2 0.292678 0.0541487 2 0.0692843 0.241839 2 0.0161595 0.184244 2 0.550926 0.512761 2 0.00244302 0.0229758 2 0.408244 0.0598919 2 0.0222281 0.220128 2 0.00337574 0.131744 2 0.386578 0.599099 2 0.000231511 0.00891079 2 0.604387 0.0936884 2 0.00542713 0.166558 0 550 1 8 2 4.44588 6.47643 2 4.68273 6.4767 2 4.86379 6.47697 2 4.97476 6.47724 2 5.00107 6.47751 2 4.92826 6.4779 2 4.74233 6.47835 2 4.43009 6.47883 0 285 551 286 552 0 287 553 h 288 1 8 2 -2 4464.6 -22667.8 2 -23729.6 -22457 2 -23337.4 -22302.5 2 -23286.2 -22194 2 -23458.7 -22127.6 2 -23869.8 -22285 2 -22649.4 -21861.6 2 -22573.7 -21388.50554 1 8 2 -21564.3 -17886.5 2 -21659.1 -17302.5 2 -21723.5 -17061.1 2 -21756.8 -17100.4 2 -21758.3 -17385.2 2 -21727.2 -15529.3 2 -21662.7 -14448.1 2 -21564.1 -14168.6 0 289 555 290 556 0 … … 293 559 294 560 0 295 296 0 297 InletV 561 z 562 2 8 5 2 0.2 0.258552 2 0.2 0.341378 2 0.4 0.108731 2 0.05 0.00749947 2 0.15 0.283839 2 0.185714 0.199851 2 0.228571 0.48354 2 0.357143 0.0677287 2 0.0857143 0.0219601 2 0.142857 0.22692 2 0.171429 0.165067 2 0.257143 0.538916 2 0.314286 0.0581515 2 0.121429 0.0496143 2 0.135714 0.188251 2 0.157143 0.146056 2 0.285714 0.533747 2 0.271429 0.0544364 2 0.157143 0.0995321 2 0.128571 0.166229 2 0.142857 0.132172 2 0.314286 0.482404 2 0.228571 0.0514509 2 0.192857 0.183289 2 0.121429 0.150684 2 0.128571 0.0701675 2 0.342857 0.608104 2 0.185714 0.0133428 2 0.228571 0.221018 2 0.114286 0.0873675 2 0.114286 0.0310307 2 0.371429 0.634936 2 0.142857 0.00300382 2 0.264286 0.288961 2 0.107143 0.0420687 2 0.1 0.0116008 2 0.4 0.555139 2 0.1 0.000593265 2 0.3 0.415481 2 0.1 0.0171862 0 563 564 0 565 566 0 567 568 0 569 VapourSideStream 570 0 1 571 vapour_stream 298 572 0 1 299 573 stream … … 306 580 0 307 581 F 308 1 8 2 157.075 180.642 2 156.161 184.935 2 154.482 188.526 2 151.76 190.873 2 105.019 195.159 2 105.763 197.505 2 104.631 192.539 2 104.12 171.7030582 1 8 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 2 0 0 0 309 583 310 584 0 311 585 T 312 1 8 2 312.389 303.297 2 315.118 304.825 2 317.688 306.208 2 321.671 308.163 2 338.59 314.811 2 350.145 323.811 2 362.61 339.798 2 372.805 376.960586 1 8 2 290 327.831 2 295.714 338.341 2 301.429 343.771 2 307.143 347.241 2 312.857 350.581 2 318.571 367.842 2 324.286 379.355 2 330 388.631 0 313 587 314 588 0 315 589 P 316 1 8 2 2.01567 2.89602 2 2.03637 2.91353 2 2.05656 2.93172 2 2.07768 2.95093 2 2.08882 2.97206 2 2.10072 2.99507 2 2.11306 3.01902 2 2.11694 3.0261 0 317 318 0 319 z 320 2 8 5 2 0.19431 0.313986 2 0.438533 0.135983 2 0.158161 0.243588 2 0.00540359 0.00021968 2 0.203593 0.306224 2 0.180157 0.319472 2 0.463897 0.146421 2 0.155743 0.218226 2 0.0134695 0.000260005 2 0.186734 0.315621 2 0.176725 0.319553 2 0.454584 0.156798 2 0.15642 0.20419 2 0.0302026 0.00061627 2 0.182068 0.318844 2 0.176349 0.319073 2 0.421301 0.157385 2 0.158534 0.197946 2 0.0626561 0.00596944 2 0.18116 0.319627 2 0.0713704 0.322388 2 0.671627 0.222996 2 0.0253071 0.105598 2 0.146653 0.00836341 2 0.0850433 0.340654 2 0.0198135 0.281272 2 0.660874 0.337595 2 0.00299747 0.0478942 2 0.289075 0.0174206 2 0.0272407 0.315819 2 0.0041542 0.188188 2 0.461852 0.487056 2 0.000285643 0.0170887 2 0.527039 0.083123 2 0.00666892 0.224545 2 0.00062743 0.0371672 2 0.215783 0.349199 2 2.11641e-005 0.00235249 2 0.782378 0.565324 2 0.00119075 0.0459566 0 590 1 8 2 4.44588 6.47643 2 4.68273 6.4767 2 4.86379 6.47697 2 4.97476 6.47724 2 5.00107 6.47751 2 4.92826 6.4779 2 4.74233 6.47835 2 4.43009 6.47883 0 321 591 322 592 0 323 593 h 324 1 8 2 881.474 -187.814 2 1172.19 -52.1841 2 1436.41 73.6926 2 1835.38 256.045 2 4009.91 922.367 2 5379.65 1917.81 2 6468.61 3825.02 2 7027.31 7775.920594 1 8 2 -1301.67 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0.0633127 0.984519 2 0.0621171 0.952491 2 0.0609554 0.94071 2 0.0598262 0.941901 0 419 775 420 776 0 421 777 MV 422 1 8 2 0. 00796695 0.0103627 2 0.00789565 0.0103482 2 0.00792088 0.0103481 2 0.007956 0.0103603 2 0.00758931 0.00994256 2 0.00727852 0.00978325 2 0.00710808 0.00958363 2 0.00691079 0.009286820778 1 8 2 0.246159 0.31224 2 0.254787 0.302932 2 0.25992 0.298139 2 0.260956 0.294949 2 0.257347 0.282372 2 0.24863 0.271451 2 0.23444 0.264837 2 0.214526 0.258954 0 423 779 424 780 0 425 781 E 426 1 8 2 - 4054.92 -6743.11 2 -3912.22 -6688.82 2 -3882.48 -6645.54 2 -3906.19 -6609.07 2 -5014.78 -7411.85 2 -4690.98 -7137.76 2 -4727.98 -6808.47 2 -4836.33 -6590.650782 1 8 2 -2340.25 -13146.4 2 -2261.47 -11811.5 2 -2160.51 -11228.2 2 -2038.25 -11042.8 2 -1896.69 -16755.2 2 -1738.98 -13798.6 2 -1569.4 -12157.9 2 -1393.26 -11624.8 0 427 783 428 784 0 429 785 vL 430 1 8 2 0.000108193 0.000102012 2 0.000110439 0.000102775 2 0.000110232 0.000103446 2 0.000108529 0.000103991 2 0.000105304 0.000103306 2 0.000107208 0.000106242 2 0.000103863 0.000109371 2 9.96842e-005 0.0001090390786 1 8 2 8.95117e-005 0.000106737 2 9.13071e-005 0.000112087 2 9.31196e-005 0.000113917 2 9.4949e-005 0.000113627 2 9.67953e-005 0.000111768 2 9.86584e-005 0.000118449 2 0.000100539 0.0001208 2 0.000102436 0.000119042 0 431 787 432 788 0 433 789 vV 434 1 8 2 0.0 119087 0.00799046 2 0.0120104 0.00798264 2 0.011988 0.00796769 2 0.0119724 0.00794976 2 0.0120153 0.00795103 2 0.0125078 0.00804451 2 0.0128654 0.00819458 2 0.0132871 0.008528230790 1 8 2 0.00487588 0.00361822 2 0.00471078 0.00372912 2 0.00461774 0.00379031 2 0.00459941 0.00383437 2 0.00466391 0.00388259 2 0.00482743 0.00402853 2 0.00511962 0.00412606 2 0.00559486 0.00422564 0 435 791 436 792 0 437 793 Level 438 1 8 2 0.0 502454 0.0832281 2 0.0503694 0.0837658 2 0.0500281 0.0841895 2 0.0492166 0.0844322 2 0.0603203 0.0934705 2 0.060728 0.0944325 2 0.0596079 0.0948907 2 0.0585823 0.09307020794 1 8 2 0.00381 0.0476352 2 0.00381 0.0476848 2 0.00381 0.0474557 2 0.00381 0.0468948 2 0.00381 0.0684102 2 0.00381 0.0701408 2 0.00381 0.0706482 2 0.00381 0.0697083 0 439 795 440 796 0 441 797 yideal 442 2 8 5 2 0.23745 0.299778 2 0.331965 0.126032 2 0.181553 0.285164 2 0.00161993 0.000201758 2 0.247412 0.288824 2 0.19431 0.313986 2 0.438533 0.135983 2 0.158161 0.243588 2 0.00540359 0.00021968 2 0.203593 0.306224 2 0.180157 0.319472 2 0.463897 0.146421 2 0.155743 0.218226 2 0.0134695 0.000260005 2 0.186734 0.315621 2 0.176725 0.319553 2 0.454584 0.156798 2 0.15642 0.20419 2 0.0302026 0.00061627 2 0.182068 0.318844 2 0.176349 0.319073 2 0.421301 0.157385 2 0.158534 0.197946 2 0.0626561 0.00596944 2 0.18116 0.319627 2 0.0713704 0.322388 2 0.671627 0.222996 2 0.0253071 0.105598 2 0.146653 0.00836341 2 0.0850433 0.340654 2 0.0198135 0.281272 2 0.660874 0.337595 2 0.00299747 0.0478942 2 0.289075 0.0174206 2 0.0272407 0.315819 2 0.0041542 0.188188 2 0.461852 0.487056 2 0.000285643 0.0170887 2 0.527039 0.083123 2 0.00666892 0.224545 0 443 444 0 445 Emv 446 1 8 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 2 1 1 0 447 448 0 449 450 8 451 Ah 452 1 8 2 0.0366038 0.0366038 2 0.0366038 0.0366038 2 0.0366038 0.0366038 2 0.0366038 0.0366038 2 0.0366038 0.0366038 2 0.0366038 0.0366038 2 0.0366038 0.0366038 2 0.0366038 0.0366038 0 453 454 0 455 lw 456 1 8 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 2 0.531876 0.531876 0 457 458 0 459 g 460 1 8 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 2 9.81 9.81 0 461 462 0 463 hw 464 1 8 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 2 0.0381 0.0381 0 465 466 0 467 beta 468 1 8 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 2 0.6 0.6 0 469 470 0 471 alfa 472 1 8 2 4 4 2 4 4 2 4 4 2 4 4 2 4 4 2 4 4 2 4 4 2 4 4 0 798 2 8 5 2 0.129182 0.294931 2 0.0268093 0.113854 2 0.758442 0.296326 2 0.00190025 0.000942317 2 0.083666 0.293946 2 0.134924 0.279466 2 0.0360305 0.210389 2 0.735505 0.216813 2 0.00386346 0.00372388 2 0.0896774 0.289608 2 0.140865 0.255605 2 0.0478268 0.266646 2 0.708358 0.201931 2 0.00651629 0.00962617 2 0.0964336 0.266192 2 0.147081 0.242315 2 0.0630071 0.285985 2 0.675655 0.19997 2 0.0100929 0.0206403 2 0.104164 0.251091 2 0.153692 0.236164 2 0.0827448 0.279545 2 0.635417 0.200989 2 0.0149328 0.0398051 2 0.113213 0.243498 2 0.160897 0.16497 2 0.108822 0.509002 2 0.584623 0.0645214 2 0.0215501 0.0738507 2 0.124109 0.187656 2 0.169023 0.0868263 2 0.144095 0.665503 2 0.518399 0.0166455 2 0.0307676 0.123242 2 0.137715 0.107783 2 0.178653 0.037911 2 0.193475 0.698877 2 0.428354 0.00372723 2 0.0439962 0.208323 2 0.155522 0.0511617 0 473 799 474 800 0 475 801 rhoL 476 1 8 2 6 23.346 612.323 2 623.745 610.956 2 630.71 610.049 2 647.058 610.094 2 677.548 621.034 2 689.575 618.403 2 728.005 621.012 2 772.101 657.1150802 1 8 2 616.774 569.109 2 624.542 569.206 2 631.894 573.765 2 638.852 584.291 2 645.435 603.255 2 651.66 596.722 2 657.542 601.596 2 663.096 623.07 0 477 803 478 804 0 479 805 rhoV 480 1 8 2 5.11509 6.9538 2 5.17388 7.03401 2 5.19752 7.09659 2 5.19143 7.12235 2 5.58833 7.33884 2 5.67945 7.54178 2 5.65355 7.72606 2 5.61639 7.81591 0 481 482 0 483 484 0 485 cond 486 0 1 487 condenser 488 0 0 489 490 14 491 NComp 492 0 0 493 494 0 495 V 496 1 1 2 2 2 0 497 498 0 499 Across 500 1 1 2 1 1 0 501 502 0 503 InletV 806 1 8 2 9.91884 15.3083 2 10.2574 15.3759 2 10.4708 15.3436 2 10.5406 15.2281 2 10.4509 16.2157 2 10.1893 16.829 2 9.74661 17.0217 2 14.9239 16.8905 0 807 808 0 809 810 0 811 VapourDrawOffFlow 812 1 1 2 0 0 0 813 814 0 815 LiquidDrawOffFlow 816 1 1 2 0 0 0 817 818 0 819 VapourInlet 504 820 0 1 505 821 stream … … 512 828 0 513 829 F 514 1 1 2 159.169 175.5910830 1 1 2 8138.57 143.587 0 515 831 516 832 0 517 833 T 518 1 1 2 3 06.076 301.4740834 1 1 2 350 399.471 0 519 835 520 836 0 521 837 P 522 1 1 2 1.99474 2.87939 0 838 1 1 2 6.76159 6.4793 0 839 840 0 841 h 842 1 1 2 3723.4 10824.3 0 843 844 0 845 v 846 1 1 2 1 1 0 523 847 524 848 0 525 849 z 526 1 5 2 0.23745 0.299778 2 0.331965 0.126032 2 0.181553 0.285164 2 0.00161993 0.000201758 2 0.247412 0.288824 0 850 1 5 2 0.176413 0.0137089 2 0.223393 0.600595 2 0.384932 0.000720825 2 0.0581468 0.364799 2 0.157115 0.0201758 0 851 852 0 853 854 0 855 LiquidOutlet 856 0 1 857 liquid_stream 858 0 1 859 stream 860 0 0 861 862 7 863 NComp 864 0 0 865 866 0 867 F 868 1 1 2 0 180.433 0 869 870 0 871 T 872 1 1 2 330 388.631 0 873 874 0 875 P 876 1 1 2 4.43009 6.47883 0 527 877 528 878 0 529 879 h 530 1 1 2 223.982 -344.1180880 1 1 2 -21564.1 -14168.6 0 531 881 532 882 0 533 883 v 534 1 1 2 1 1 0 535 536 0 537 538 0 539 OutletL 540 0 1 541 liquid_stream 884 1 1 2 0 0 0 885 886 0 887 z 888 1 5 2 0.1 0.0116008 2 0.4 0.555139 2 0.1 0.000593265 2 0.3 0.415481 2 0.1 0.0171862 0 889 890 0 891 892 0 893 894 0 895 LiquidConnector 542 896 0 1 543 897 stream … … 550 904 0 551 905 F 552 1 1 2 2496 345.0750906 1 1 2 58.7421 54.9199 0 553 907 554 908 0 555 909 T 556 1 1 2 2 88.15 299.150910 1 1 2 259.994 288.154 0 557 911 558 912 0 559 913 P 560 1 1 2 1.97385 2.86383 0 914 1 1 2 1.95797 4.04365 0 915 916 0 917 h 918 1 1 2 -25185.7 -21158.3 0 919 920 0 921 v 922 1 1 2 0 0 0 561 923 562 924 0 563 925 z 564 1 5 2 0.216067 0.225278 2 0.453839 0.427493 2 0.0889142 0.0993579 2 0.002431 0.00223881 2 0.238749 0.245633 0 926 1 5 2 0.2 0.294992 2 0.2 0.113679 2 0.4 0.296382 2 0.05 0.000939896 2 0.15 0.294007 0 927 928 0 929 930 0 931 VapourConnector 932 0 1 933 stream 934 0 0 935 936 7 937 NComp 938 0 0 939 940 0 941 F 942 1 1 2 8138.57 143.587 0 943 944 0 945 T 946 1 1 2 350 399.471 0 947 948 0 949 P 950 1 1 2 6.76159 6.4793 0 565 951 566 952 0 567 953 h 568 1 1 2 -24464.6 -22667.80954 1 1 2 3723.4 10824.3 0 569 955 570 956 0 571 957 v 572 1 1 2 0 0 0 573 574 0 575 576 0 577 578 0 579 OutletV 580 0 1 581 vapour_stream 958 1 1 2 1 1 0 959 960 0 961 z 962 1 5 2 0.176413 0.0137089 2 0.223393 0.600595 2 0.384932 0.000720825 2 0.0581468 0.364799 2 0.157115 0.0201758 0 963 964 0 965 966 0 967 968 1 969 FeedTray 582 970 0 1 583 971 stream … … 590 978 0 591 979 F 592 1 1 2 1 20 76.29710980 1 1 2 113.4 113.4 0 593 981 594 982 0 595 983 T 596 1 1 2 2 88.15 299.150984 1 1 2 291 291 0 597 985 598 986 0 599 987 P 600 1 1 2 1.97385 2.86383 0 601 602 0 603 z 604 1 5 2 0.275683 0.275225 2 0.114063 0.115455 2 0.347186 0.346059 2 0.000169787 0.000183629 2 0.262899 0.263077 0 988 1 1 2 5.60868 5.60868 0 605 989 606 990 0 607 991 h 608 1 1 2 - 1341.53 -534.2930992 1 1 2 -24198.8 -24198.8 0 609 993 610 994 0 611 995 v 612 1 1 2 1 1 0 613 614 0 615 616 0 617 618 0 619 InletQ 620 0 1 621 energy_stream 622 0 0 623 624 1 625 Q 626 1 1 2 -138889 -138889 0 627 628 0 629 630 0 631 M 632 1 5 2 2.19604 1.74247 2 4.57176 3.24351 2 0.924267 0.803327 2 0.0244499 0.0169213 2 2.4229 1.89418 0 633 634 0 635 ML 636 1 1 2 10.0514 7.54544 0 637 638 0 639 MV 640 1 1 2 0.0880042 0.154969 0 641 642 0 643 E 644 1 1 2 -246422 -171702 0 645 646 0 647 vL 648 1 1 2 9.94885e-005 0.000101062 0 649 650 0 651 vV 652 1 1 2 0.0113631 0.00798514 0 653 654 0 655 Level 656 1 1 2 1 0.762554 0 657 658 0 659 660 0 661 reb 662 0 1 663 reboiler 664 0 0 665 666 16 667 NComp 668 0 0 669 670 0 671 Across 672 1 1 2 1 1 0 673 674 0 675 V 676 1 1 2 2 2 0 677 678 0 679 Inlet 680 0 1 681 stream 682 0 0 683 684 7 685 NComp 686 0 0 687 688 0 689 F 690 1 1 2 0 0 0 691 692 0 693 T 694 1 1 2 300 300 0 695 696 0 697 P 698 1 1 2 1 1 0 996 1 1 2 -6.65306e-111 -4.95446e-021 0 699 997 700 998 0 … … 703 1001 704 1002 0 1003 1004 0 1005 1006 0 1007 cond 1008 0 1 1009 condenser 1010 0 0 1011 1012 25 1013 NComp 1014 1 1 2 1 1 0 1015 1016 0 1017 Mw 1018 1 5 2 58.123 58.123 2 72.1498 72.1498 2 42.0804 42.0804 2 78.1134 78.1134 2 56.1072 56.1072 0 1019 1020 0 1021 low_flow 1022 1 1 2 1e-006 1e-006 0 1023 1024 0 1025 zero_flow 1026 1 1 2 0 0 0 1027 1028 0 1029 KfConst 1030 1 1 2 1 1 0 1031 1032 0 1033 Kfactor 1034 1 1 2 0.001 0.001 0 1035 1036 0 1037 Levelpercent_Initial 1038 1 1 2 0.5 0.5 0 1039 1040 0 1041 Initial_Temperature 1042 1 1 2 260 260 0 1043 1044 0 1045 Initial_Composition 1046 1 5 2 0.2 0.2 2 0.2 0.2 2 0.4 0.4 2 0.05 0.05 2 0.15 0.15 0 1047 1048 0 1049 Geometry 1050 0 1 1051 VesselVolume 1052 0 0 1053 1054 12 1055 PI 1056 1 1 2 3.14159 3.14159 0 1057 1058 0 1059 Gconst 1060 1 1 2 9.81 9.81 0 1061 1062 0 1063 Diameter 1064 1 1 2 1 1 0 1065 1066 0 1067 Lenght 1068 1 1 2 1 1 0 1069 1070 0 1071 Vhead_elliptical 1072 1 1 2 0.261799 0.261799 0 1073 1074 0 1075 Vhead_hemispherical 1076 1 1 2 0.523599 0.523599 0 1077 1078 0 1079 Vcylinder 1080 1 1 2 0.785398 0.785398 0 1081 1082 0 1083 radius 1084 1 1 2 0.5 0.5 0 1085 1086 0 1087 Vtotal 1088 1 1 2 0.785398 0.785398 0 1089 1090 0 1091 Vfilled 1092 1 1 2 0.392699 0.392712 0 1093 1094 0 1095 Level 1096 1 1 2 0.5 0.500016 0 1097 1098 0 1099 Across 1100 1 1 2 0.785398 0.785398 0 1101 1102 0 1103 1104 0 1105 InletVapour 1106 0 1 1107 stream 1108 0 0 1109 1110 7 1111 NComp 1112 0 0 1113 1114 0 1115 F 1116 1 1 2 124.191 131.478 0 1117 1118 0 1119 T 1120 1 1 2 290 327.831 0 1121 1122 0 1123 P 1124 1 1 2 4.44588 6.47643 0 1125 1126 0 705 1127 h 706 1 1 2 0 001128 1 1 2 -1301.67 1553.42 0 707 1129 708 1130 0 709 1131 v 710 1 1 2 0 0 0 711 712 0 713 714 0 715 InletL 1132 1 1 2 1 1 0 1133 1134 0 1135 z 1136 1 5 2 0.129182 0.294931 2 0.0268093 0.113854 2 0.758442 0.296326 2 0.00190025 0.000942317 2 0.083666 0.293946 0 1137 1138 0 1139 1140 0 1141 OutletLiquid 1142 0 1 1143 liquid_stream 716 1144 0 1 717 1145 stream … … 724 1152 0 725 1153 F 726 1 1 2 1 25.279 442.43401154 1 1 2 118.742 131.483 0 727 1155 728 1156 0 729 1157 T 730 1 1 2 362.61 339.79801158 1 1 2 260 288.157 0 731 1159 732 1160 0 733 1161 P 734 1 1 2 2.11306 3.01902 0 1162 1 1 2 1.80006 3.88574 0 1163 1164 0 1165 h 1166 1 1 2 -25185.7 -21158.3 0 1167 1168 0 1169 v 1170 1 1 2 0 0 0 735 1171 736 1172 0 737 1173 z 738 1 5 2 0.000518255 0.0613898 2 0.186866 0.556402 2 1.72828e-005 0.00238803 2 0.811611 0.296621 2 0.00098801 0.0831989 0 1174 1 5 2 0.2 0.294992 2 0.2 0.113679 2 0.4 0.296382 2 0.05 0.000939896 2 0.15 0.294007 0 1175 1176 0 1177 1178 0 1179 1180 0 1181 OutletVapour 1182 0 1 1183 vapour_stream 1184 0 1 1185 stream 1186 0 0 1187 1188 7 1189 NComp 1190 0 0 1191 1192 0 1193 F 1194 1 1 2 0 0 0 1195 1196 0 1197 T 1198 1 1 2 260 288.157 0 1199 1200 0 1201 P 1202 1 1 2 1.80006 3.88574 0 739 1203 740 1204 0 741 1205 h 742 1 1 2 -2 2577.9 -21097.501206 1 1 2 -2963.11 -1446.49 0 743 1207 744 1208 0 745 1209 v 746 1 1 2 0 0 0 747 748 0 749 750 0 751 OutletL 1210 1 1 2 1 1 0 1211 1212 0 1213 z 1214 1 5 2 0.110308 0.201936 2 0.0159767 0.0160295 2 0.804967 0.606666 2 0.000859612 3.89882e-005 2 0.0678881 0.17533 0 1215 1216 0 1217 1218 0 1219 1220 0 1221 InletQ 1222 1 1 2 -763.889 -829.524 0 1223 1224 0 1225 TI 1226 1 1 2 260 288.157 0 1227 1228 0 1229 LI 1230 1 1 2 0.5 0.500016 0 1231 1232 0 1233 PI 1234 1 1 2 1.80006 3.88574 0 1235 1236 0 1237 M 1238 1 5 2 0.936525 1.29779 2 0.933252 0.495759 2 1.89333 1.33239 2 0.233204 0.00409234 2 0.701879 1.29163 0 1239 1240 0 1241 ML 1242 1 1 2 4.66349 4.35111 0 1243 1244 0 1245 MV 1246 1 1 2 0.0346965 0.0705483 0 1247 1248 0 1249 E 1250 1 1 2 -117699 -92473.4 0 1251 1252 0 1253 vL 1254 1 1 2 8.42071e-005 9.02555e-005 0 1255 1256 0 1257 vV 1258 1 1 2 0.0113181 0.00556621 0 1259 1260 0 1261 rho 1262 1 1 2 9.47541 15.033 0 1263 1264 0 1265 Pdrop 1266 1 1 2 268.088 262.502 0 1267 1268 0 1269 1270 0 1271 reb 1272 0 1 1273 reboiler 1274 0 0 1275 1276 20 1277 NComp 1278 1 1 2 1 1 0 1279 1280 0 1281 Levelpercent_Initial 1282 1 1 2 0.5 0.5 0 1283 1284 0 1285 Initial_Temperature 1286 1 1 2 350 350 0 1287 1288 0 1289 Initial_Composition 1290 1 5 2 0.1 0.1 2 0.4 0.4 2 0.1 0.1 2 0.3 0.3 2 0.1 0.1 0 1291 1292 0 1293 Geometry 1294 0 1 1295 VesselVolume 1296 0 0 1297 1298 12 1299 PI 1300 1 1 2 3.14159 3.14159 0 1301 1302 0 1303 Gconst 1304 1 1 2 9.81 9.81 0 1305 1306 0 1307 Diameter 1308 1 1 2 1 1 0 1309 1310 0 1311 Lenght 1312 1 1 2 2 2 0 1313 1314 0 1315 Vhead_elliptical 1316 1 1 2 0.261799 0.261799 0 1317 1318 0 1319 Vhead_hemispherical 1320 1 1 2 0.523599 0.523599 0 1321 1322 0 1323 Vcylinder 1324 1 1 2 1.5708 1.5708 0 1325 1326 0 1327 radius 1328 1 1 2 0.5 0.5 0 1329 1330 0 1331 Vtotal 1332 1 1 2 1.5708 1.5708 0 1333 1334 0 1335 Vfilled 1336 1 1 2 0.785398 0.785203 0 1337 1338 0 1339 Level 1340 1 1 2 1 0.999752 0 1341 1342 0 1343 Across 1344 1 1 2 0.785398 0.785398 0 1345 1346 0 1347 1348 0 1349 InletLiquid 1350 0 1 1351 stream 1352 0 0 1353 1354 7 1355 NComp 1356 0 0 1357 1358 0 1359 F 1360 1 1 2 0 180.433 0 1361 1362 0 1363 T 1364 1 1 2 330 388.631 0 1365 1366 0 1367 P 1368 1 1 2 4.43009 6.47883 0 1369 1370 0 1371 h 1372 1 1 2 -21564.1 -14168.6 0 1373 1374 0 1375 v 1376 1 1 2 0 0 0 1377 1378 0 1379 z 1380 1 5 2 0.1 0.0116008 2 0.4 0.555139 2 0.1 0.000593265 2 0.3 0.415481 2 0.1 0.0171862 0 1381 1382 0 1383 1384 0 1385 OutletLiquid 752 1386 0 1 753 1387 liquid_stream … … 762 1396 0 763 1397 F 764 1 1 2 60 7.3580201398 1 1 2 30 36.8285 0 765 1399 766 1400 0 767 1401 T 768 1 1 2 3 72.805 376.9601402 1 1 2 350 399.471 0 769 1403 770 1404 0 771 1405 P 772 1 1 2 2.11694 3.0261 0 1406 1 1 2 6.76159 6.4793 0 1407 1408 0 1409 h 1410 1 1 2 -18461.2 -14377.8 0 1411 1412 0 1413 v 1414 1 1 2 0 0 0 773 1415 774 1416 0 775 1417 z 776 1 5 2 6.21593e-005 0.0052362 2 0.0660517 0.146684 2 1.06721e-006 0.000168876 2 0.933744 0.840322 2 0.000141024 0.00758903 0 1418 1 5 2 0.1 0.00342403 2 0.4 0.379668 2 0.1 9.71358e-005 2 0.3 0.611214 2 0.1 0.00559687 0 1419 1420 0 1421 1422 0 1423 1424 0 1425 OutletVapour 1426 0 1 1427 vapour_stream 1428 0 1 1429 stream 1430 0 0 1431 1432 7 1433 NComp 1434 0 0 1435 1436 0 1437 F 1438 1 1 2 8138.57 143.587 0 1439 1440 0 1441 T 1442 1 1 2 350 399.471 0 1443 1444 0 1445 P 1446 1 1 2 6.76159 6.4793 0 777 1447 778 1448 0 779 1449 h 780 1 1 2 -22271.8 -20620.201450 1 1 2 3723.4 10824.3 0 781 1451 782 1452 0 783 1453 v 784 1 1 2 0 0 0 785 786 0 787 788 0 789 790 0 791 OutletV 792 0 1 793 vapour_stream 1454 1 1 2 1 1 0 1455 1456 0 1457 z 1458 1 5 2 0.176413 0.0137089 2 0.223393 0.600595 2 0.384932 0.000720825 2 0.0581468 0.364799 2 0.157115 0.0201758 0 1459 1460 0 1461 1462 0 1463 1464 0 1465 InletQ 1466 1 1 2 899.993 994.695 0 1467 1468 0 1469 TI 1470 1 1 2 350 399.471 0 1471 1472 0 1473 LI 1474 1 1 2 0.5 0.499876 0 1475 1476 0 1477 PI 1478 1 1 2 6.76159 6.4793 0 1479 1480 0 1481 M 1482 1 5 2 0.771991 0.0259978 2 2.98689 2.71737 2 0.815693 0.000797215 2 2.21724 4.26632 2 0.767947 0.0420941 0 1483 1484 0 1485 ML 1486 1 1 2 7.35018 6.87275 0 1487 1488 0 1489 MV 1490 1 1 2 0.209581 0.179828 0 1491 1492 0 1493 E 1494 1 1 2 -135989 -97899.6 0 1495 1496 0 1497 vL 1498 1 1 2 0.000106854 0.000114249 0 1499 1500 0 1501 vV 1502 1 1 2 0.00374746 0.00436859 0 1503 1504 0 1505 rhoV 1506 1 1 2 14.9239 16.8905 0 1507 1508 0 1509 Pdrop 1510 1 1 2 -236.24 -0.047474 0 1511 1512 0 1513 1514 0 1515 sptop 1516 0 1 1517 splitter_column 1518 0 0 1519 1520 6 1521 Inlet 794 1522 0 1 795 1523 stream … … 802 1530 0 803 1531 F 804 1 1 2 1 04.12 171.703 01532 1 1 2 118.742 131.483 0 805 1533 806 1534 0 807 1535 T 808 1 1 2 372.805 376.9601536 1 1 2 260 288.157 0 809 1537 810 1538 0 811 1539 P 812 1 1 2 2.11694 3.0261 0 1540 1 1 2 1.80006 3.88574 0 1541 1542 0 1543 h 1544 1 1 2 -25185.7 -21158.3 0 1545 1546 0 1547 v 1548 1 1 2 0 0 0 813 1549 814 1550 0 815 1551 z 816 1 5 2 0.00062743 0.0371672 2 0.215783 0.349199 2 2.11641e-005 0.00235249 2 0.782378 0.565324 2 0.00119075 0.0459566 0 1552 1 5 2 0.2 0.294992 2 0.2 0.113679 2 0.4 0.296382 2 0.05 0.000939896 2 0.15 0.294007 0 1553 1554 0 1555 1556 0 1557 Reflux 1558 0 1 1559 stream 1560 0 0 1561 1562 7 1563 NComp 1564 0 0 1565 1566 0 1567 F 1568 1 1 2 58.7421 54.9199 0 1569 1570 0 1571 T 1572 1 1 2 260 288.157 0 1573 1574 0 1575 P 1576 1 1 2 1.80006 3.88574 0 817 1577 818 1578 0 819 1579 h 820 1 1 2 7027.31 7775.9201580 1 1 2 -25185.7 -21158.3 0 821 1581 822 1582 0 823 1583 v 824 1 1 2 1 1 0 825 826 0 827 828 0 829 830 0 831 InletQ 832 0 1 833 energy_stream 834 0 0 835 836 1 837 Q 838 1 1 2 2.5e+006 1.83417e+006 0 839 840 0 841 842 0 843 M 844 1 5 2 0.000683335 0.0662022 2 0.693142 1.79741 2 1.24922e-005 0.00223037 2 9.63276 10.1785 2 0.00153329 0.0952964 0 845 846 0 847 ML 848 1 1 2 10.255 12.0571 0 849 850 0 851 MV 852 1 1 2 0.0731423 0.0825546 0 853 854 0 855 E 856 1 1 2 -228312 -248591 0 857 858 0 859 vL 860 1 1 2 9.75136e-005 0.000100883 0 861 862 0 863 vV 864 1 1 2 0.013672 0.00949241 0 865 866 0 867 Level 868 1 1 2 1 1.21636 0 869 870 0 871 rhoV 872 1 1 2 5.61639 7.81591 0 873 874 0 875 876 0 877 sptop 878 0 1 879 splitter 1584 1 1 2 0 0 0 1585 1586 0 1587 z 1588 1 5 2 0.2 0.294992 2 0.2 0.113679 2 0.4 0.296382 2 0.05 0.000939896 2 0.15 0.294007 0 1589 1590 0 1591 1592 0 1593 Distillate 1594 0 1 1595 stream 1596 0 0 1597 1598 7 1599 NComp 1600 0 0 1601 1602 0 1603 F 1604 1 1 2 60 76.5635 0 1605 1606 0 1607 T 1608 1 1 2 260 288.157 0 1609 1610 0 1611 P 1612 1 1 2 1.80006 3.88574 0 1613 1614 0 1615 h 1616 1 1 2 -25185.7 -21158.3 0 1617 1618 0 1619 v 1620 1 1 2 0 0 0 1621 1622 0 1623 z 1624 1 5 2 0.2 0.294992 2 0.2 0.113679 2 0.4 0.296382 2 0.05 0.000939896 2 0.15 0.294007 0 1625 1626 0 1627 1628 0 1629 SplitFlow_RefluxStream 1630 1 1 2 0.494703 0.417695 0 1631 1632 0 1633 SplitFlow_DistillateStream 1634 1 1 2 0.505297 0.582305 0 1635 1636 0 1637 RefluxRatio 1638 1 1 2 0.979036 0.717312 0 1639 1640 0 1641 1642 0 1643 pump1 1644 0 1 1645 pump 880 1646 0 0 881 1647 882 1648 4 1649 NComp 1650 0 0 1651 1652 0 883 1653 Inlet 884 1654 0 1 … … 892 1662 0 893 1663 F 894 1 1 2 2496 345.07501664 1 1 2 58.7421 54.9199 0 895 1665 896 1666 0 897 1667 T 898 1 1 2 2 88.15 299.1501668 1 1 2 260 288.157 0 899 1669 900 1670 0 901 1671 P 902 1 1 2 1.97385 2.86383 0 1672 1 1 2 1.80006 3.88574 0 1673 1674 0 1675 h 1676 1 1 2 -25185.7 -21158.3 0 1677 1678 0 1679 v 1680 1 1 2 0 0 0 903 1681 904 1682 0 905 1683 z 906 1 5 2 0.216067 0.225278 2 0.453839 0.427493 2 0.0889142 0.0993579 2 0.002431 0.00223881 2 0.238749 0.245633 0 1684 1 5 2 0.2 0.294992 2 0.2 0.113679 2 0.4 0.296382 2 0.05 0.000939896 2 0.15 0.294007 0 1685 1686 0 1687 1688 0 1689 Outlet 1690 0 1 1691 liquid_stream 1692 0 1 1693 stream 1694 0 0 1695 1696 7 1697 NComp 1698 0 0 1699 1700 0 1701 F 1702 1 1 2 58.7421 54.9199 0 1703 1704 0 1705 T 1706 1 1 2 259.994 288.154 0 1707 1708 0 1709 P 1710 1 1 2 1.95797 4.04365 0 907 1711 908 1712 0 909 1713 h 910 1 1 2 -2 4464.6 -22667.801714 1 1 2 -25185.7 -21158.3 0 911 1715 912 1716 0 … … 915 1719 916 1720 0 917 918 0919 Outlet1920 0 1921 stream922 0 0923 924 7925 NComp926 0 0927 928 0929 F930 1 1 2 120 0 0931 932 0933 T934 1 1 2 288.15 299.15 0935 936 0937 P938 1 1 2 1.97385 2.86383 0939 940 0941 1721 z 942 1 5 2 0.216067 0.225278 2 0.453839 0.427493 2 0.0889142 0.0993579 2 0.002431 0.00223881 2 0.238749 0.245633 0 943 944 0 945 h 946 1 1 2 -24464.6 -22667.8 0 947 948 0 949 v 950 1 1 2 0 0 0 951 952 0 953 954 0 955 Outlet2 956 0 1 957 stream 958 0 0 959 960 7 961 NComp 962 0 0 963 964 0 965 F 966 1 1 2 2376 345.075 0 967 968 0 969 T 970 1 1 2 288.15 299.15 0 971 972 0 973 P 974 1 1 2 1.97385 2.86383 0 975 976 0 977 z 978 1 5 2 0.216067 0.225278 2 0.453839 0.427493 2 0.0889142 0.0993579 2 0.002431 0.00223881 2 0.238749 0.245633 0 979 980 0 981 h 982 1 1 2 -24464.6 -22667.8 0 983 984 0 985 v 986 1 1 2 0 0 0 987 988 0 989 990 0 991 frac 992 1 1 2 0.0480769 -1.03907e-093 0 993 994 0 995 996 0 997 pump1 998 0 1 999 pump 1000 0 0 1001 1002 4 1003 NComp 1004 0 0 1005 1006 0 1007 Inlet 1008 0 1 1009 stream 1010 0 0 1011 1012 7 1013 NComp 1014 0 0 1015 1016 0 1017 F 1018 1 1 2 2376 345.075 0 1019 1020 0 1021 T 1022 1 1 2 288.15 299.15 0 1023 1024 0 1025 P 1026 1 1 2 1.97385 2.86383 0 1027 1028 0 1029 z 1030 1 5 2 0.216067 0.225278 2 0.453839 0.427493 2 0.0889142 0.0993579 2 0.002431 0.00223881 2 0.238749 0.245633 0 1031 1032 0 1033 h 1034 1 1 2 -24464.6 -22667.8 0 1035 1036 0 1037 v 1038 1 1 2 0 0 0 1039 1040 0 1041 1042 0 1043 Outlet 1044 0 1 1045 streamPH 1046 0 1 1047 stream 1048 0 0 1049 1050 7 1051 NComp 1052 0 0 1053 1054 0 1055 F 1056 1 1 2 2376 345.075 0 1057 1058 0 1059 T 1060 1 1 2 288.145 299.146 0 1061 1062 0 1063 P 1064 1 1 2 2.13175 3.02174 0 1065 1066 0 1067 z 1068 1 5 2 0.216067 0.225278 2 0.453839 0.427493 2 0.0889142 0.0993579 2 0.002431 0.00223881 2 0.238749 0.245633 0 1069 1070 0 1071 h 1072 1 1 2 -24464.6 -22667.8 0 1073 1074 0 1075 v 1076 1 1 2 0 0 0 1077 1078 0 1079 1080 2 1081 x 1082 1 5 2 0.216067 0.225278 2 0.453839 0.427493 2 0.0889142 0.0993579 2 0.002431 0.00223881 2 0.238749 0.245633 0 1083 1084 0 1085 y 1086 1 5 2 0.277287 0.278763 2 0.11525 0.118824 2 0.343547 0.336024 2 0.000169337 0.0001868 2 0.263746 0.266202 0 1087 1088 0 1089 1090 0 1091 dP 1092 1 1 2 0.157908 0.157908 0 1093 1094 0 1722 1 5 2 0.2 0.294992 2 0.2 0.113679 2 0.4 0.296382 2 0.05 0.000939896 2 0.15 0.294007 0 1723 1724 0 1725 1726 0 1727 1728 0 1729 Pincrease 1730 1 1 2 16 16 0 1095 1731 1096 1732 0 … … 1102 1738 0 0 1103 1739 1104 1 41105 NComp 1106 001740 18 1741 NComp 1742 1 1 2 1 1 0 1107 1743 1108 1744 0 … … 1133 1769 1134 1770 0 1771 h 1772 1 1 2 -24198.8 -24198.8 0 1773 1774 0 1775 v 1776 1 1 2 -6.65306e-111 -4.95446e-021 0 1777 1778 0 1135 1779 z 1136 1780 1 5 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 0 1137 1781 1138 1782 0 1139 h 1140 1 1 2 -24198.8 -24198.8 0 1141 1142 0 1143 v 1144 1 1 2 0 0 0 1145 1146 0 1783 1784 0 1785 Composition 1786 1 5 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 0 1787 1788 0 1789 SumOfComposition 1790 1 1 2 1 1 0 1791 1792 0 1793 F 1794 1 1 2 113.4 113.4 0 1795 1796 0 1797 Fw 1798 1 1 2 6953.09 6953.09 0 1799 1800 0 1801 Fvol 1802 1 1 2 10.3298 10.3298 0 1803 1804 0 1805 T 1806 1 1 2 291 291 0 1807 1808 0 1809 T_Cdeg 1810 1 1 2 17.85 17.85 0 1811 1812 0 1813 P 1814 1 1 2 5.60868 5.60868 0 1147 1815 1148 1816 0 … … 1155 1823 1156 1824 0 1157 hl 1158 1 1 2 -24198.8 -24198.8 0 1159 1160 0 1161 hv 1162 1 1 2 -1550.12 -1550.12 0 1825 Mw 1826 1 1 2 61.3148 61.3148 0 1827 1828 0 1829 vm 1830 1 1 2 9.10914e-005 9.10914e-005 0 1831 1832 0 1833 rho 1834 1 1 2 673.112 673.112 0 1835 1836 0 1837 rhom 1838 1 1 2 10.978 10.978 0 1163 1839 1164 1840 0 … … 1167 1843 1168 1844 0 1169 Mw1170 1 1 2 61.3148 61.3148 01171 1172 01173 vm1174 1 1 2 9.10914e-005 9.10914e-005 01175 1176 01177 rho1178 1 1 2 673.112 673.112 01179 1180 01181 rhom1182 1 1 2 10.978 10.978 01183 1184 01185 Fw1186 1 1 2 6953.09 6953.09 01187 1188 01189 Fvol1190 1 1 2 10.3298 10.3298 01191 1192 01193 1194 01195 zero1196 0 11197 stream1198 0 01199 1200 71201 NComp1202 0 01203 1204 01205 F1206 1 1 2 0 0 01207 1208 01209 T1210 1 1 2 300 300 01211 1212 01213 P1214 1 1 2 1 1 01215 1216 01217 z1218 1 5 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 2 0.2 0.2 01219 1220 01221 h1222 1 1 2 0 0 01223 1224 01225 v1226 1 1 2 0 0 01227 1228 01229 1845 1230 1846 0 … … 1234 1850 0 0 1235 1851 1236 5 1237 Parameters 1238 0 1 1239 MParameters 1240 0 0 1241 1242 9 1852 33 1243 1853 alpha 1244 1 1 2 0. 3 0.301854 1 1 2 0.1 0.1 0 1245 1855 1246 1856 0 … … 1270 1880 0 1271 1881 tau 1272 1 1 2 0 001882 1 1 2 1 1 0 1273 1883 1274 1884 0 1275 1885 tauSet 1276 1 1 2 0 0 0 1277 1278 0 1279 1280 0 1281 Options 1282 0 1 1283 MOptions 1284 0 0 1285 1286 3 1287 action 1288 1 1 2 1 1 0 1289 1290 0 1291 autoMan 1292 1 1 2 0 0 0 1293 1294 0 1295 clip 1296 1 1 2 1 1 0 1297 1298 0 1299 1300 0 1301 Internal 1302 0 1 1303 MInternal_Variables 1304 0 0 1305 1306 12 1307 dderivTerm 1308 1 1 2 3331.65 4.42548e-006 0 1309 1310 0 1311 dFilt 1312 1 1 2 0.500488 -0.00670347 0 1313 1314 0 1315 error 1316 1 1 2 999.994 -0.00670214 0 1317 1318 0 1319 errorD 1320 1 1 2 999.994 -0.00670214 0 1321 1322 0 1323 errorI 1324 1 1 2 -0.999994 -0.22 0 1325 1326 0 1327 inputFilt 1328 1 1 2 1.00049 0.92 0 1329 1330 0 1331 dintTerm 1332 1 1 2 -0.0166666 -0.00366667 0 1333 1334 0 1335 doutp 1336 1 1 2 2598.97 -0.00621863 0 1337 1338 0 1339 outps 1340 1 1 2 1.00099 1.25214 0 1341 1342 0 1343 outp 1344 1 1 2 1.0005 1.12607 0 1345 1346 0 1347 dpropTerm 1348 1 1 2 999.994 -0.00670214 0 1349 1350 0 1351 setPointFilt 1352 1 1 2 0.000498 0.7 0 1353 1354 0 1355 1356 0 1357 Ports 1358 0 1 1359 MPorts 1360 0 0 1361 1362 3 1363 input 1364 1 1 2 0.7 0.920007 0 1365 1366 0 1367 output 1368 1 1 2 1 1 0 1369 1370 0 1371 setPoint 1886 1 1 2 1 1 0 1887 1888 0 1889 MinInput 1890 1 1 2 253.15 253.15 0 1891 1892 0 1893 MaxInput 1894 1 1 2 303.15 303.15 0 1895 1896 0 1897 MinOutput 1898 1 1 2 -5e+006 -5e+006 0 1899 1900 0 1901 MaxOutput 1902 1 1 2 -500000 -500000 0 1903 1904 0 1905 Input 1906 1 1 2 260 288.157 0 1907 1908 0 1909 Output 1910 1 1 2 -2.75e+006 -2.98629e+006 0 1911 1912 0 1913 SetPoint 1914 1 1 2 288.15 288.15 0 1915 1916 0 1917 PID_dderivTerm 1918 1 1 2 0 -1.92911e-011 0 1919 1920 0 1921 PID_dFilt 1922 1 1 2 0 2.37423e-008 0 1923 1924 0 1925 PID_error 1926 1 1 2 0 2.37404e-008 0 1927 1928 0 1929 PID_errorD 1930 1 1 2 0 2.37404e-008 0 1931 1932 0 1933 PID_errorI 1934 1 1 2 0.563 -0.000140213 0 1935 1936 0 1937 PID_inputFilt 1938 1 1 2 0.137 0.70014 0 1939 1940 0 1941 PID_dintTerm 1942 1 1 2 0.00938333 -2.33688e-006 0 1943 1944 0 1945 PID_doutp 1946 1 1 2 0.00563 -1.38789e-006 0 1947 1948 0 1949 PID_outps 1950 1 1 2 0 -0.105017 0 1951 1952 0 1953 PID_outp 1954 1 1 2 0.5 0.447492 0 1955 1956 0 1957 PID_dpropTerm 1958 1 1 2 0 2.37404e-008 0 1959 1960 0 1961 PID_setPointFilt 1372 1962 1 1 2 0.7 0.7 0 1373 1963 1374 1964 0 1375 1376 0 1377 AWFactor 1965 PID_input 1966 1 1 2 0.137 0.70014 0 1967 1968 0 1969 PID_output 1970 1 1 2 0.5 0.447492 0 1971 1972 0 1973 PID_setPoint 1974 1 1 2 0.7 0.7 0 1975 1976 0 1977 PID_AWFactor 1978 1 1 2 1 1 0 1979 1980 0 1981 PID_action 1378 1982 1 1 2 1 1 0 1379 1983 … … 1386 1990 0 0 1387 1991 1388 5 1389 Parameters 1390 0 1 1391 MParameters 1392 0 0 1393 1394 9 1992 33 1395 1993 alpha 1396 1 1 2 0. 3 0.301994 1 1 2 0.1 0.1 0 1397 1995 1398 1996 0 … … 1422 2020 0 1423 2021 tau 1424 1 1 2 0 002022 1 1 2 1 1 0 1425 2023 1426 2024 0 1427 2025 tauSet 1428 1 1 2 0 0 0 1429 1430 0 1431 1432 0 1433 Options 1434 0 1 1435 MOptions 1436 0 0 1437 1438 3 1439 action 2026 1 1 2 1 1 0 2027 2028 0 2029 MinInput 2030 1 1 2 0 0 0 2031 2032 0 2033 MaxInput 2034 1 1 2 1 1 0 2035 2036 0 2037 MinOutput 2038 1 1 2 0 0 0 2039 2040 0 2041 MaxOutput 2042 1 1 2 120 120 0 2043 2044 0 2045 Input 2046 1 1 2 0.5 0.500016 0 2047 2048 0 2049 Output 2050 1 1 2 60 76.5635 0 2051 2052 0 2053 SetPoint 2054 1 1 2 0.5 0.5 0 2055 2056 0 2057 PID_dderivTerm 2058 1 1 2 0 0 0 2059 2060 0 2061 PID_dFilt 2062 1 1 2 0 1.25816e-009 0 2063 2064 0 2065 PID_error 2066 1 1 2 0 1.25815e-009 0 2067 2068 0 2069 PID_errorD 2070 1 1 2 0 1.25815e-009 0 2071 2072 0 2073 PID_errorI 2074 1 1 2 0 -1.62442e-005 0 2075 2076 0 2077 PID_inputFilt 2078 1 1 2 0.5 0.500016 0 2079 2080 0 2081 PID_dintTerm 2082 1 1 2 0 -8.12211e-007 0 2083 2084 0 2085 PID_doutp 2086 1 1 2 0 8.10952e-007 0 2087 2088 0 2089 PID_outps 2090 1 1 2 0 0.276058 0 2091 2092 0 2093 PID_outp 2094 1 1 2 0.5 0.638029 0 2095 2096 0 2097 PID_dpropTerm 2098 1 1 2 0 1.25815e-009 0 2099 2100 0 2101 PID_setPointFilt 2102 1 1 2 0.5 0.5 0 2103 2104 0 2105 PID_input 2106 1 1 2 0.5 0.500016 0 2107 2108 0 2109 PID_output 2110 1 1 2 0.5 0.638029 0 2111 2112 0 2113 PID_setPoint 2114 1 1 2 0.5 0.5 0 2115 2116 0 2117 PID_AWFactor 2118 1 1 2 1 1 0 2119 2120 0 2121 PID_action 1440 2122 1 1 2 -1 -1 0 1441 2123 1442 2124 0 1443 autoMan1444 1 1 2 0 0 01445 1446 01447 clip1448 1 1 2 1 1 01449 1450 01451 1452 01453 Internal1454 0 11455 MInternal_Variables1456 0 01457 1458 121459 dderivTerm1460 1 1 2 0 0 01461 1462 01463 dFilt1464 1 1 2 0.500516 0.00339613 01465 1466 01467 error1468 1 1 2 999.994 0.00339614 01469 1470 01471 errorD1472 1 1 2 999.994 0.00339614 01473 1474 01475 errorI1476 1 1 2 -0.999994 0.11872 01477 1478 01479 inputFilt1480 1 1 2 1.00052 0.38128 01481 1482 01483 dintTerm1484 1 1 2 -0.0477909 -0.00492532 01485 1486 01487 doutp1488 1 1 2 -999.946 0.00152918 01489 1490 01491 outps1492 1 1 2 1.00105 -1.03219 01493 1494 01495 outp1496 1 1 2 1.00052 -0.0160972 01497 1498 01499 dpropTerm1500 1 1 2 999.994 0.00339614 01501 1502 01503 setPointFilt1504 1 1 2 0.000526 0.5 01505 1506 01507 1508 01509 Ports1510 0 11511 MPorts1512 0 01513 1514 31515 input1516 1 1 2 0.5 0.381277 01517 1518 01519 output1520 1 1 2 1 0 01521 1522 01523 setPoint1524 1 1 2 0.5 0.5 01525 1526 01527 1528 01529 AWFactor1530 1 1 2 0.955825 -0.829372 01531 1532 01533 2125 1534 2126 0 … … 1538 2130 0 0 1539 2131 1540 5 1541 Parameters 1542 0 1 1543 MParameters 1544 0 0 1545 1546 9 2132 33 1547 2133 alpha 1548 1 1 2 0. 3 0.302134 1 1 2 0.1 0.1 0 1549 2135 1550 2136 0 … … 1566 2152 0 1567 2153 gain 1568 1 1 2 1 102154 1 1 2 1.5 1.5 0 1569 2155 1570 2156 0 … … 1574 2160 0 1575 2161 tau 1576 1 1 2 0 002162 1 1 2 1 1 0 1577 2163 1578 2164 0 1579 2165 tauSet 1580 1 1 2 0 0 0 1581 1582 0 1583 1584 0 1585 Options 1586 0 1 1587 MOptions 1588 0 0 1589 1590 3 1591 action 2166 1 1 2 1 1 0 2167 2168 0 2169 MinInput 2170 1 1 2 0 0 0 2171 2172 0 2173 MaxInput 2174 1 1 2 1 1 0 2175 2176 0 2177 MinOutput 2178 1 1 2 0 0 0 2179 2180 0 2181 MaxOutput 2182 1 1 2 60 60 0 2183 2184 0 2185 Input 2186 1 1 2 0.5 0.499876 0 2187 2188 0 2189 Output 2190 1 1 2 30 36.8285 0 2191 2192 0 2193 SetPoint 2194 1 1 2 0.5 0.5 0 2195 2196 0 2197 PID_dderivTerm 2198 1 1 2 0 0 0 2199 2200 0 2201 PID_dFilt 2202 1 1 2 0 -7.803e-008 0 2203 2204 0 2205 PID_error 2206 1 1 2 0 -7.803e-008 0 2207 2208 0 2209 PID_errorD 2210 1 1 2 0 -7.803e-008 0 2211 2212 0 2213 PID_errorI 2214 1 1 2 0 0.000124276 0 2215 2216 0 2217 PID_inputFilt 2218 1 1 2 0.5 0.499876 0 2219 2220 0 2221 PID_dintTerm 2222 1 1 2 0 1.24276e-006 0 2223 2224 0 2225 PID_doutp 2226 1 1 2 0 -1.74709e-006 0 2227 2228 0 2229 PID_outps 2230 1 1 2 0 0.227616 0 2231 2232 0 2233 PID_outp 2234 1 1 2 0.5 0.613808 0 2235 2236 0 2237 PID_dpropTerm 2238 1 1 2 0 -7.803e-008 0 2239 2240 0 2241 PID_setPointFilt 2242 1 1 2 0.5 0.5 0 2243 2244 0 2245 PID_input 2246 1 1 2 0.5 0.499876 0 2247 2248 0 2249 PID_output 2250 1 1 2 0.5 0.613808 0 2251 2252 0 2253 PID_setPoint 2254 1 1 2 0.5 0.5 0 2255 2256 0 2257 PID_AWFactor 2258 1 1 2 1 1 0 2259 2260 0 2261 PID_action 1592 2262 1 1 2 -1 -1 0 1593 2263 1594 2264 0 1595 autoMan1596 1 1 2 0 0 01597 1598 01599 clip1600 1 1 2 1 1 01601 1602 01603 1604 01605 Internal1606 0 11607 MInternal_Variables1608 0 01609 1610 121611 dderivTerm1612 1 1 2 0 0 01613 1614 01615 dFilt1616 1 1 2 0.500544 -0.00433612 01617 1618 01619 error1620 1 1 2 999.994 -0.00433612 01621 1622 01623 errorD1624 1 1 2 999.994 -0.00433612 01625 1626 01627 errorI1628 1 1 2 -0.999994 -0.108174 01629 1630 01631 inputFilt1632 1 1 2 1.00055 0.608174 01633 1634 01635 dintTerm1636 1 1 2 -0.00955332 -0.00108174 01637 1638 01639 doutp1640 1 1 2 -999.984 0.00541786 01641 1642 01643 outps1644 1 1 2 1.0011 -0.754733 01645 1646 01647 outp1648 1 1 2 1.00055 0.122634 01649 1650 01651 dpropTerm1652 1 1 2 999.994 -0.00433612 01653 1654 01655 setPointFilt1656 1 1 2 0.000554 0.5 01657 1658 01659 1660 01661 Ports1662 0 11663 MPorts1664 0 01665 1666 31667 input1668 1 1 2 0.5 0.608179 01669 1670 01671 output1672 1 1 2 1 0.122634 01673 1674 01675 setPoint1676 1 1 2 0.5 0.5 01677 1678 01679 1680 01681 AWFactor1682 1 1 2 0.955338 1 01683 1684 01685 2265 1686 2266 0 … … 1690 2270 0 0 1691 2271 1692 5 1693 Parameters 1694 0 1 1695 MParameters 1696 0 0 1697 1698 9 2272 33 1699 2273 alpha 1700 1 1 2 0. 3 0.302274 1 1 2 0.1 0.1 0 1701 2275 1702 2276 0 … … 1726 2300 0 1727 2301 tau 1728 1 1 2 0 002302 1 1 2 1 1 0 1729 2303 1730 2304 0 1731 2305 tauSet 1732 1 1 2 0 0 0 1733 1734 0 1735 1736 0 1737 Options 1738 0 1 1739 MOptions 1740 0 0 1741 1742 3 1743 action 2306 1 1 2 1 1 0 2307 2308 0 2309 MinInput 2310 1 1 2 0.5 0.5 0 2311 2312 0 2313 MaxInput 2314 1 1 2 10 10 0 2315 2316 0 2317 MinOutput 2318 1 1 2 0 0 0 2319 2320 0 2321 MaxOutput 2322 1 1 2 120 120 0 2323 2324 0 2325 Input 2326 1 1 2 1.80006 3.88574 0 2327 2328 0 2329 Output 2330 1 1 2 0 0 0 2331 2332 0 2333 SetPoint 2334 1 1 2 4 4 0 2335 2336 0 2337 PID_dderivTerm 2338 1 1 2 0 -2.35497e-010 0 2339 2340 0 2341 PID_dFilt 2342 1 1 2 0 6.39528e-007 0 2343 2344 0 2345 PID_error 2346 1 1 2 0 6.39504e-007 0 2347 2348 0 2349 PID_errorD 2350 1 1 2 0 6.39504e-007 0 2351 2352 0 2353 PID_errorI 2354 1 1 2 0.231573 0.012027 0 2355 2356 0 2357 PID_inputFilt 2358 1 1 2 0.136848 0.356394 0 2359 2360 0 2361 PID_dintTerm 2362 1 1 2 0.00463145 -6.51241e-007 0 2363 2364 0 2365 PID_doutp 2366 1 1 2 -0.00231573 5.98634e-009 0 2367 2368 0 2369 PID_outps 2370 1 1 2 -1 -1.02003 0 2371 2372 0 2373 PID_outp 2374 1 1 2 0 -0.0100135 0 2375 2376 0 2377 PID_dpropTerm 2378 1 1 2 0 6.39504e-007 0 2379 2380 0 2381 PID_setPointFilt 2382 1 1 2 0.368421 0.368421 0 2383 2384 0 2385 PID_input 2386 1 1 2 0.136848 0.356393 0 2387 2388 0 2389 PID_output 2390 1 1 2 0 0 0 2391 2392 0 2393 PID_setPoint 2394 1 1 2 0.368421 0.368421 0 2395 2396 0 2397 PID_AWFactor 2398 1 1 2 1 -0.00270723 0 2399 2400 0 2401 PID_action 1744 2402 1 1 2 -1 -1 0 1745 2403 1746 2404 0 1747 autoMan1748 1 1 2 0 0 01749 1750 01751 clip1752 1 1 2 1 1 01753 1754 01755 1756 01757 Internal1758 0 11759 MInternal_Variables1760 0 01761 1762 121763 dderivTerm1764 1 1 2 4033.4 -3.13135e-005 01765 1766 01767 dFilt1768 1 1 2 0.500572 -0.00343921 01769 1770 01771 error1772 1 1 2 1210.52 -0.0034486 01773 1774 01775 errorD1776 1 1 2 1210.52 -0.0034486 01777 1778 01779 errorI1780 1 1 2 -0.999994 0.115606 01781 1782 01783 inputFilt1784 1 1 2 1.00058 0.252815 01785 1786 01787 dintTerm1788 1 1 2 -0.0190968 0.00231211 01789 1790 01791 doutp1792 1 1 2 -2621.95 0.0005839 01793 1794 01795 outps1796 1 1 2 1.00116 0.271618 01797 1798 01799 outp1800 1 1 2 1.00058 0.635809 01801 1802 01803 dpropTerm1804 1 1 2 1210.52 -0.0034486 01805 1806 01807 setPointFilt1808 1 1 2 0.000582 0.368421 01809 1810 01811 1812 01813 Ports1814 0 11815 MPorts1816 0 01817 1818 31819 input1820 1 1 2 0.157895 0.252819 01821 1822 01823 output1824 1 1 2 1 0.635809 01825 1826 01827 setPoint1828 1 1 2 0.368421 0.368421 01829 1830 01831 1832 01833 AWFactor1834 1 1 2 0.954847 1 01835 1836 01837 2405 1838 2406 0 1839 2407 PID11 1840 2408 0 1 1841 PIDIncr 1842 0 0 1843 1844 5 1845 Parameters 1846 0 1 1847 MParameters 1848 0 0 1849 1850 9 2409 PID 2410 0 0 2411 2412 32 1851 2413 alpha 1852 1 1 2 0. 3 0.302414 1 1 2 0.1 0.1 0 1853 2415 1854 2416 0 … … 1878 2440 0 1879 2441 tau 1880 1 1 2 0 002442 1 1 2 1 1 0 1881 2443 1882 2444 0 1883 2445 tauSet 1884 1 1 2 0 0 0 1885 1886 0 1887 1888 0 1889 Options 1890 0 1 1891 MOptions 1892 0 0 1893 1894 3 1895 action 2446 1 1 2 1 1 0 2447 2448 0 2449 MinInput 2450 1 1 2 0 0 0 2451 2452 0 2453 MaxInput 2454 1 1 2 1 1 0 2455 2456 0 2457 MinOutput 2458 1 1 2 0 0 0 2459 2460 0 2461 MaxOutput 2462 1 1 2 1 1 0 2463 2464 0 2465 Input 2466 1 1 2 0.05 0.000939896 0 2467 2468 0 2469 Output 2470 1 1 2 0.1294 0.0765216 0 2471 2472 0 2473 SetPoint 2474 1 1 2 0.001 0.001 0 2475 2476 0 2477 PID_derivTerm 2478 1 1 2 0 0 0 2479 2480 0 2481 PID_dFilt 2482 1 1 2 -0.049 6.01241e-005 0 2483 2484 0 2485 PID_error 2486 1 1 2 -0.049 6.01241e-005 0 2487 2488 0 2489 PID_errorD 2490 1 1 2 -0.049 6.01241e-005 0 2491 2492 0 2493 PID_errorI 2494 1 1 2 -0.049 6.01241e-005 0 2495 2496 0 2497 PID_inputFilt 2498 1 1 2 0.05 0.000939876 0 2499 2500 0 2501 PID_intTerm 2502 1 1 2 0 0.0390705 0 2503 2504 0 2505 PID_outp 2506 1 1 2 0.1294 0.0765216 0 2507 2508 0 2509 PID_outps 2510 1 1 2 -0.7412 -0.846957 0 2511 2512 0 2513 PID_propTerm 2514 1 1 2 -0.049 6.01241e-005 0 2515 2516 0 2517 PID_setPointFilt 2518 1 1 2 0.001 0.001 0 2519 2520 0 2521 PID_AWFactor 2522 1 1 2 1 1 0 2523 2524 0 2525 PID_action 1896 2526 1 1 2 -1 -1 0 1897 2527 1898 2528 0 1899 autoMan 1900 1 1 2 0 0 0 1901 1902 0 1903 clip 1904 1 1 2 1 1 0 1905 1906 0 1907 1908 0 1909 Internal 1910 0 1 1911 MInternal_Variables 1912 0 0 1913 1914 12 1915 dderivTerm 1916 1 1 2 0 0 0 1917 1918 0 1919 dFilt 1920 1 1 2 0.5006 6.71333e-006 0 1921 1922 0 1923 error 1924 1 1 2 998.563 6.71334e-006 0 1925 1926 0 1927 errorD 1928 1 1 2 998.563 6.71334e-006 0 1929 1930 0 1931 errorI 1932 1 1 2 -0.999994 -0.00123882 0 1933 1934 0 1935 inputFilt 1936 1 1 2 1.0006 0.00223882 0 1937 1938 0 1939 dintTerm 1940 1 1 2 -0.0159057 -2.0647e-005 0 1941 1942 0 1943 doutp 1944 1 1 2 -599.128 8.36019e-006 0 1945 1946 0 1947 outps 1948 1 1 2 -0.8 -0.8 0 1949 1950 0 1951 outp 2529 PID_input 2530 1 1 2 0.05 0.000939896 0 2531 2532 0 2533 PID_output 2534 1 1 2 0.1294 0.0765216 0 2535 2536 0 2537 PID_setPoint 2538 1 1 2 0.001 0.001 0 2539 2540 0 2541 2542 0 2543 PID22 2544 0 1 2545 PID 2546 0 0 2547 2548 32 2549 alpha 1952 2550 1 1 2 0.1 0.1 0 1953 1954 01955 dpropTerm1956 1 1 2 998.563 6.71334e-006 01957 1958 01959 setPointFilt1960 1 1 2 0.00061 0.001 01961 1962 01963 1964 01965 Ports1966 0 11967 MPorts1968 0 01969 1970 31971 input1972 1 1 2 0.002431 0.00223881 01973 1974 01975 output1976 1 1 2 0.1 0.1 01977 1978 01979 setPoint1980 1 1 2 0.001 0.001 01981 1982 01983 1984 01985 AWFactor1986 1 1 2 0.95435 1 01987 1988 01989 1990 01991 PID221992 0 11993 PIDIncr1994 0 01995 1996 51997 Parameters1998 0 11999 MParameters2000 0 02001 2002 92003 alpha2004 1 1 2 0.3 0.3 02005 2551 2006 2552 0 … … 2030 2576 0 2031 2577 tau 2032 1 1 2 0 002578 1 1 2 1 1 0 2033 2579 2034 2580 0 2035 2581 tauSet 2036 1 1 2 0 0 0 2037 2038 0 2039 2040 0 2041 Options 2042 0 1 2043 MOptions 2044 0 0 2045 2046 3 2047 action 2582 1 1 2 1 1 0 2583 2584 0 2585 MinInput 2586 1 1 2 0 0 0 2587 2588 0 2589 MaxInput 2590 1 1 2 1 1 0 2591 2592 0 2593 MinOutput 2594 1 1 2 0 0 0 2595 2596 0 2597 MaxOutput 2598 1 1 2 1 1 0 2599 2600 0 2601 Input 2602 1 1 2 0.1 9.71358e-005 0 2603 2604 0 2605 Output 2606 1 1 2 0.559994 0.598886 0 2607 2608 0 2609 SetPoint 2610 1 1 2 1e-005 1e-005 0 2611 2612 0 2613 PID_derivTerm 2614 1 1 2 0 0 0 2615 2616 0 2617 PID_dFilt 2618 1 1 2 -0.09999 -8.71371e-005 0 2619 2620 0 2621 PID_error 2622 1 1 2 -0.09999 -8.71371e-005 0 2623 2624 0 2625 PID_errorD 2626 1 1 2 -0.09999 -8.71371e-005 0 2627 2628 0 2629 PID_errorI 2630 1 1 2 -0.09999 -8.71371e-005 0 2631 2632 0 2633 PID_inputFilt 2634 1 1 2 0.1 9.71371e-005 0 2635 2636 0 2637 PID_intTerm 2638 1 1 2 0 -0.164723 0 2639 2640 0 2641 PID_outp 2642 1 1 2 0.559994 0.598886 0 2643 2644 0 2645 PID_outps 2646 1 1 2 0.119988 0.197772 0 2647 2648 0 2649 PID_propTerm 2650 1 1 2 -0.09999 -8.71371e-005 0 2651 2652 0 2653 PID_setPointFilt 2654 1 1 2 1e-005 1e-005 0 2655 2656 0 2657 PID_AWFactor 2658 1 1 2 1 1 0 2659 2660 0 2661 PID_action 2048 2662 1 1 2 -1 -1 0 2049 2663 2050 2664 0 2051 autoMan 2052 1 1 2 0 0 0 2053 2054 0 2055 clip 2056 1 1 2 1 1 0 2057 2058 0 2059 2060 0 2061 Internal 2062 0 1 2063 MInternal_Variables 2064 0 0 2065 2066 12 2067 dderivTerm 2068 1 1 2 0 0 0 2069 2070 0 2071 dFilt 2072 1 1 2 0.500628 -1.29576e-005 0 2073 2074 0 2075 error 2076 1 1 2 1000 -1.29578e-005 0 2077 2078 0 2079 errorD 2080 1 1 2 1000 -1.29578e-005 0 2081 2082 0 2083 errorI 2084 1 1 2 -0.999994 -0.000158863 0 2085 2086 0 2087 inputFilt 2088 1 1 2 1.00063 0.000168863 0 2089 2090 0 2091 dintTerm 2092 1 1 2 -0.0158974 -2.64772e-006 0 2093 2094 0 2095 doutp 2096 1 1 2 -599.992 9.36333e-006 0 2097 2098 0 2099 outps 2100 1 1 2 0 0 0 2101 2102 0 2103 outp 2104 1 1 2 0.5 0.5 0 2105 2106 0 2107 dpropTerm 2108 1 1 2 1000 -1.29578e-005 0 2109 2110 0 2111 setPointFilt 2112 1 1 2 0.000638 1e-005 0 2113 2114 0 2115 2116 0 2117 Ports 2118 0 1 2119 MPorts 2120 0 0 2121 2122 3 2123 input 2124 1 1 2 1.06721e-006 0.000168876 0 2125 2126 0 2127 output 2128 1 1 2 0.5 0.5 0 2129 2130 0 2131 setPoint 2665 PID_input 2666 1 1 2 0.1 9.71358e-005 0 2667 2668 0 2669 PID_output 2670 1 1 2 0.559994 0.598886 0 2671 2672 0 2673 PID_setPoint 2132 2674 1 1 2 1e-005 1e-005 0 2133 2675 … … 2135 2677 2136 2678 0 2137 AWFactor2138 1 1 2 0.953847 1 02139 2140 02141 2142 02143 2679 PID12 2144 2680 0 1 2145 PIDIncr 2146 0 0 2147 2148 5 2149 Parameters 2150 0 1 2151 MParameters 2152 0 0 2153 2154 9 2681 PID 2682 0 0 2683 2684 32 2155 2685 alpha 2156 1 1 2 0. 3 0.302686 1 1 2 0.1 0.1 0 2157 2687 2158 2688 0 … … 2182 2712 0 2183 2713 tau 2184 1 1 2 0 002714 1 1 2 1 1 0 2185 2715 2186 2716 0 2187 2717 tauSet 2188 1 1 2 0 0 0 2189 2190 0 2191 2192 0 2193 Options 2194 0 1 2195 MOptions 2196 0 0 2197 2198 3 2199 action 2718 1 1 2 1 1 0 2719 2720 0 2721 MinInput 2722 1 1 2 0 0 0 2723 2724 0 2725 MaxInput 2726 1 1 2 1 1 0 2727 2728 0 2729 MinOutput 2730 1 1 2 0 0 0 2731 2732 0 2733 MaxOutput 2734 1 1 2 1 1 0 2735 2736 0 2737 Input 2738 1 1 2 0.1 9.71358e-005 0 2739 2740 0 2741 Output 2742 1 1 2 0.049995 0.0494605 0 2743 2744 0 2745 SetPoint 2746 1 1 2 1e-005 1e-005 0 2747 2748 0 2749 PID_derivTerm 2750 1 1 2 0 0 0 2751 2752 0 2753 PID_dFilt 2754 1 1 2 -0.09999 -8.71371e-005 0 2755 2756 0 2757 PID_error 2758 1 1 2 -0.09999 -8.71371e-005 0 2759 2760 0 2761 PID_errorD 2762 1 1 2 -0.09999 -8.71371e-005 0 2763 2764 0 2765 PID_errorI 2766 1 1 2 -0.09999 -8.71371e-005 0 2767 2768 0 2769 PID_inputFilt 2770 1 1 2 0.1 9.71371e-005 0 2771 2772 0 2773 PID_intTerm 2774 1 1 2 0 -0.0988339 0 2775 2776 0 2777 PID_outp 2778 1 1 2 0.049995 0.0494605 0 2779 2780 0 2781 PID_outps 2782 1 1 2 -0.90001 -0.901079 0 2783 2784 0 2785 PID_propTerm 2786 1 1 2 -0.09999 -8.71371e-005 0 2787 2788 0 2789 PID_setPointFilt 2790 1 1 2 1e-005 1e-005 0 2791 2792 0 2793 PID_AWFactor 2794 1 1 2 1 1 0 2795 2796 0 2797 PID_action 2200 2798 1 1 2 -1 -1 0 2201 2799 2202 2800 0 2203 autoMan 2204 1 1 2 0 0 0 2205 2206 0 2207 clip 2208 1 1 2 1 1 0 2209 2210 0 2211 2212 0 2213 Internal 2214 0 1 2215 MInternal_Variables 2216 0 0 2217 2218 12 2219 dderivTerm 2220 1 1 2 0 0 0 2221 2222 0 2223 dFilt 2224 1 1 2 0.500656 -1.29576e-005 0 2225 2226 0 2227 error 2228 1 1 2 1000 -1.29578e-005 0 2229 2230 0 2231 errorD 2232 1 1 2 1000 -1.29578e-005 0 2233 2234 0 2235 errorI 2236 1 1 2 -0.999994 -0.000158863 0 2237 2238 0 2239 inputFilt 2240 1 1 2 1.00066 0.000168863 0 2241 2242 0 2243 dintTerm 2244 1 1 2 -0.00953334 -1.58863e-006 0 2245 2246 0 2247 doutp 2248 1 1 2 -499.997 7.27323e-006 0 2249 2250 0 2251 outps 2252 1 1 2 -1 -1 0 2253 2254 0 2255 outp 2256 1 1 2 0 0 0 2257 2258 0 2259 dpropTerm 2260 1 1 2 1000 -1.29578e-005 0 2261 2262 0 2263 setPointFilt 2264 1 1 2 0.000666 1e-005 0 2265 2266 0 2267 2268 0 2269 Ports 2270 0 1 2271 MPorts 2272 0 0 2273 2274 3 2275 input 2276 1 1 2 1.06721e-006 0.000168876 0 2277 2278 0 2279 output 2280 1 1 2 0 0 0 2281 2282 0 2283 setPoint 2801 PID_input 2802 1 1 2 0.1 9.71358e-005 0 2803 2804 0 2805 PID_output 2806 1 1 2 0.049995 0.0494605 0 2807 2808 0 2809 PID_setPoint 2284 2810 1 1 2 1e-005 1e-005 0 2285 2811 … … 2287 2813 2288 2814 0 2289 AWFactor2290 1 1 2 0.95334 1 02291 2292 02293 2294 02295 2815 PID21 2296 2816 0 1 2297 PIDIncr 2298 0 0 2299 2300 5 2301 Parameters 2302 0 1 2303 MParameters 2304 0 0 2305 2306 9 2817 PID 2818 0 0 2819 2820 32 2307 2821 alpha 2308 1 1 2 0. 3 0.302822 1 1 2 0.1 0.1 0 2309 2823 2310 2824 0 … … 2334 2848 0 2335 2849 tau 2336 1 1 2 0 002850 1 1 2 1 1 0 2337 2851 2338 2852 0 2339 2853 tauSet 2340 1 1 2 0 0 0 2341 2342 0 2343 2344 0 2345 Options 2346 0 1 2347 MOptions 2348 0 0 2349 2350 3 2351 action 2352 1 1 2 1 1 0 2353 2354 0 2355 autoMan 2356 1 1 2 0 0 0 2357 2358 0 2359 clip 2360 1 1 2 1 1 0 2361 2362 0 2363 2364 0 2365 Internal 2366 0 1 2367 MInternal_Variables 2368 0 0 2369 2370 12 2371 dderivTerm 2372 1 1 2 0 0 0 2373 2374 0 2375 dFilt 2376 1 1 2 0.500684 6.71333e-006 0 2377 2378 0 2379 error 2380 1 1 2 998.563 6.71334e-006 0 2381 2382 0 2383 errorD 2384 1 1 2 998.563 6.71334e-006 0 2385 2386 0 2387 errorI 2388 1 1 2 -0.999994 -0.00123882 0 2389 2390 0 2391 inputFilt 2392 1 1 2 1.00069 0.00223882 0 2393 2394 0 2395 dintTerm 2396 1 1 2 -0.00999994 -1.23882e-005 0 2397 2398 0 2399 doutp 2400 1 1 2 499.277 -2.83743e-006 0 2401 2402 0 2403 outps 2404 1 1 2 -1 -1 0 2405 2406 0 2407 outp 2408 1 1 2 0 0 0 2409 2410 0 2411 dpropTerm 2412 1 1 2 998.563 6.71334e-006 0 2413 2414 0 2415 setPointFilt 2416 1 1 2 0.000694 0.001 0 2417 2418 0 2419 2420 0 2421 Ports 2422 0 1 2423 MPorts 2424 0 0 2425 2426 3 2427 input 2428 1 1 2 0.002431 0.00223881 0 2429 2430 0 2431 output 2432 1 1 2 0 0 0 2433 2434 0 2435 setPoint 2854 1 1 2 1 1 0 2855 2856 0 2857 MinInput 2858 1 1 2 0 0 0 2859 2860 0 2861 MaxInput 2862 1 1 2 1 1 0 2863 2864 0 2865 MinOutput 2866 1 1 2 0 0 0 2867 2868 0 2869 MaxOutput 2870 1 1 2 1 1 0 2871 2872 0 2873 Input 2874 1 1 2 0.05 0.000939896 0 2875 2876 0 2877 Output 2878 1 1 2 0 0.0463392 0 2879 2880 0 2881 SetPoint 2436 2882 1 1 2 0.001 0.001 0 2437 2883 2438 2884 0 2439 2440 0 2441 AWFactor 2442 1 1 2 1 1 0 2443 2444 0 2445 2446 0 2885 PID_derivTerm 2886 1 1 2 0 0 0 2887 2888 0 2889 PID_dFilt 2890 1 1 2 -0.049 6.01241e-005 0 2891 2892 0 2893 PID_error 2894 1 1 2 -0.049 6.01241e-005 0 2895 2896 0 2897 PID_errorD 2898 1 1 2 -0.049 6.01241e-005 0 2899 2900 0 2901 PID_errorI 2902 1 1 2 -0.049 6.01241e-005 0 2903 2904 0 2905 PID_inputFilt 2906 1 1 2 0.05 0.000939876 0 2907 2908 0 2909 PID_intTerm 2910 1 1 2 0 0.0926182 0 2911 2912 0 2913 PID_outp 2914 1 1 2 -0.0245 0.0463392 0 2915 2916 0 2917 PID_outps 2918 1 1 2 -1.049 -0.907322 0 2919 2920 0 2921 PID_propTerm 2922 1 1 2 -0.049 6.01241e-005 0 2923 2924 0 2925 PID_setPointFilt 2926 1 1 2 0.001 0.001 0 2927 2928 0 2929 PID_AWFactor 2930 1 1 2 -0.993963 1 0 2931 2932 0 2933 PID_action 2934 1 1 2 1 1 0 2935 2936 0 2937 PID_input 2938 1 1 2 0.05 0.000939896 0 2939 2940 0 2941 PID_output 2942 1 1 2 0 0.0463392 0 2943 2944 0 2945 PID_setPoint 2946 1 1 2 0.001 0.001 0 2947 2948 0 2949 2950 0 -
branches/gui/sample/controllers/sample_PIDIncr_MIMO.mso
r735 r910 24 24 * Author: Argimiro R. Secchi 25 25 * $Id: sample_PID_MIMO.mso 313 2007-07-14 16:45:55Z arge $ 26 *-------------------------------------------------------------------- #26 *--------------------------------------------------------------------*# 27 27 28 28 using "stage_separators/column"; … … 40 40 NComp as Integer; 41 41 42 Qcmin as heat_rate (Brief="Minimum Condenser Heat supplied");43 Qcmax as heat_rate (Brief="Maximum Condenser Heat supplied");44 42 Qrmin as heat_rate (Brief="Minimum Reboiler Heat supplied"); 45 43 Qrmax as heat_rate (Brief="Maximum Reboiler Heat supplied"); 46 Frmin as flow_mol (Brief="Minimum bottom flow rate");47 Frmax as flow_mol (Brief="Maximum bottom flow rate");48 Fcmin as flow_mol (Brief="Minimum reflux flow rate");49 Fcmax as flow_mol (Brief="Maximum reflux flow rate");50 Hmint as length (Brief="Minimum liquid level in top tank");51 Hmaxt as length (Brief="Maximum liquid level in top tank");52 Hminb as length (Brief="Minimum liquid level in reboiler");53 Hmaxb as length (Brief="Maximum liquid level in reboiler");54 Pmax as pressure (Brief="Maximum column pressure");55 Pmin as pressure (Brief="Minimum column pressure");56 Tmax as temperature (Brief="Maximum column temperature");57 Tmin as temperature (Brief="Minimum column temperature");58 44 RRmax as positive (Brief="Maximum reflux ratio"); 59 45 RRmin as positive (Brief="Minimum reflux ratio"); … … 62 48 Qc as energy_source (Brief="Heat rate removed from condenser"); 63 49 Qr as energy_source (Brief="Heat rate supplied to reboiler"); 64 Had_top as Real (Brief="Dimensionless condenser level");65 Had_bot as Real (Brief="Dimensionless reboiler level");66 Pad as Real (Brief="Dimensionless pressure");67 50 P_sp as pressure (Brief="Pressure setpoint"); 68 Tad as Real (Brief="Dimensionless temperature");69 51 T_sp as temperature (Brief="Condenser temperature setpoint"); 70 52 RR as positive (Brief="Reflux ratio"); 71 LC_sp as length(Brief="Condenser level setpoint");72 LR_sp as length(Brief="Reboiler level setpoint");73 xtop as fraction (Brief="Controlled top composition");74 xbot as fraction (Brief="Controlled bottom composition");53 LC_sp as fraction (Brief="Condenser level setpoint"); 54 LR_sp as fraction (Brief="Reboiler level setpoint"); 55 out xtop as fraction (Brief="Controlled top composition"); 56 out xbot as fraction (Brief="Controlled bottom composition"); 75 57 xtop_sp as fraction (Brief="Controlled top composition setpoint"); 76 58 xbot_sp as fraction (Brief="Controlled bottom composition setpoint"); … … 80 62 81 63 DEVICES 82 col as Distillation_kettle_cond; 64 col as Section_Column; 65 cond as condenser; 66 reb as reboiler; 67 sptop as splitter_column; 68 pump1 as pump; 69 # Valve_Distillate as valve_flow; 70 # Valve_Bottom as valve_flow; 83 71 feed as source; 84 zero as stream;85 72 TCcond as PIDIncr; 86 73 LCtop as PIDIncr; … … 93 80 94 81 CONNECTIONS 95 feed.Outlet to col.trays(5).Inlet; 96 zero to col.reb.Inlet; 97 zero to col.trays([1:4]).Inlet; 98 zero to col.trays([6:col.NTrays]).Inlet; 99 Qc.OutletQ to col.cond.InletQ; 100 Qr.OutletQ to col.reb.InletQ; 82 feed.Outlet to col.FeedTray; 83 Qc.OutletQ to cond.InletQ; 84 Qr.OutletQ to reb.InletQ; 85 # sptop.Distillate to Valve_Distillate.Inlet; 86 sptop.Reflux to pump1.Inlet; 87 pump1.Outlet to col.LiquidInlet; 88 col.VapourOutlet to cond.InletVapour; 89 cond.OutletLiquid to sptop.Inlet; 90 col.LiquidOutlet to reb.InletLiquid; 91 reb.OutletVapour to col.VapourInlet; 92 # reb.OutletLiquid to Valve_Bottom.Inlet; 93 cond.TI to TCcond.Input; 94 cond.PI to PC.Input; 95 cond.LI to LCtop.Input; 96 reb.LI to LCbot.Input; 97 xtop to PID11.Input; 98 xbot to PID12.Input; 99 xtop to PID21.Input; 100 xbot to PID22.Input; 101 101 102 102 EQUATIONS 103 "Temperature Controller" 104 TCcond.Parameters.tau = 0*'s'; 105 TCcond.Parameters.tauSet = 0*'s'; 106 TCcond.Parameters.alpha = 0.3; 107 TCcond.Parameters.bias = 0.5; 108 TCcond.Parameters.gamma = 1; 109 TCcond.Parameters.beta = 1; 110 TCcond.Options.action = 1; 111 TCcond.Options.clip = 1; 112 TCcond.Options.autoMan = 0; 113 TCcond.Parameters.intTime = 60*'s'; 114 TCcond.Parameters.gain = 0.6; 115 TCcond.Parameters.derivTime = 1*'s'; 116 TCcond.Ports.setPoint = (T_sp - Tmin)/(Tmax-Tmin); 117 TCcond.Ports.input = Tad; 118 Tad = (col.cond.OutletL.T-Tmin)/(Tmax-Tmin); 119 Qc.OutletQ.Q = Qcmin+(Qcmax-Qcmin)*TCcond.Ports.output; 120 121 "Pressure Controller" 122 PC.Parameters.tau = 0*'s'; 123 PC.Parameters.tauSet = 0*'s'; 124 PC.Parameters.alpha = 0.3; 125 PC.Parameters.bias = 0; 126 PC.Parameters.gamma = 1; 127 PC.Parameters.beta = 1; 128 PC.Options.action = -1; 129 PC.Options.clip = 1; 130 PC.Options.autoMan = 0; 131 PC.Parameters.intTime = 50*'s'; 132 PC.Parameters.gain = 0.5; 133 PC.Parameters.derivTime = 1*'s'; 134 PC.Ports.setPoint = (P_sp-Pmin)/(Pmax-Pmin); 135 PC.Ports.input = Pad; 136 Pad = (col.cond.OutletV.P-Pmin)/(Pmax-Pmin); 137 col.cond.OutletV.F = (Fcmin+(Fcmax-Fcmin)*PC.Ports.output); 103 104 TCcond.SetPoint * 'K' = T_sp; 105 Qc.OutletQ = TCcond.Output * 'kJ/h'; 106 107 PC.SetPoint * 'bar' = P_sp; 108 cond.OutletVapour.F = PC.Output * 'kmol/h'; 109 110 LCtop.SetPoint = LC_sp; 111 sptop.Distillate.F = LCtop.Output * 'kmol/h'; 112 113 LCbot.SetPoint = LR_sp; 114 reb.OutletLiquid.F = LCbot.Output * 'kmol/h'; 115 116 "MIMO PID Controller" 117 PID11.SetPoint = xtop_sp; 118 PID12.SetPoint = xbot_sp; 119 120 RR = RRmin + (RRmax-RRmin) * (PID11.Output + PID12.Output); 121 122 PID21.SetPoint = xtop_sp; 123 PID22.SetPoint = xbot_sp; 124 125 Qr.OutletQ = Qrmin + (Qrmax-Qrmin) * (PID21.Output + PID22.Output); 126 127 RR * (cond.OutletVapour.F + sptop.Distillate.F) = sptop.Reflux.F; 128 xtop = cond.OutletLiquid.z(4); # benzene 129 xbot = reb.OutletLiquid.z(3); # propylene 130 131 if time < 1 * 'h' then 132 feed.F = 113.4 * 'kmol/h'; 133 else 134 feed.F = 120 * 'kmol/h'; 135 end 136 137 SPECIFY 138 feed.T = 291 * 'K'; 139 feed.P = 568.3 * 'kPa'; 140 feed.Composition = 1/NComp; 138 141 139 "Ttop Level Controller" 140 LCtop.Parameters.tau = 0*'s'; 141 LCtop.Parameters.tauSet = 0*'s'; 142 LCtop.Parameters.alpha = 0.3; 143 LCtop.Parameters.bias = 0.5; 144 LCtop.Parameters.gamma = 1; 145 LCtop.Parameters.beta = 1; 146 LCtop.Options.action = -1; 147 LCtop.Options.clip = 1; 148 LCtop.Options.autoMan = 0; 149 LCtop.Parameters.intTime = 20*'s'; 150 LCtop.Parameters.gain = 1; 151 LCtop.Parameters.derivTime = 0*'s'; 152 LCtop.Ports.setPoint = (LC_sp - Hmint)/(Hmaxt-Hmint); 153 LCtop.Ports.input = Had_top; 154 Had_top = (col.cond.Level-Hmint)/(Hmaxt-Hmint); 155 col.sptop.Outlet1.F = Fcmin + (Fcmax-Fcmin) * LCtop.Ports.output; 156 157 "Tbottom Level Controller" 158 LCbot.Parameters.tau = 0*'s'; 159 LCbot.Parameters.tauSet = 0*'s'; 160 LCbot.Parameters.alpha = 0.3; 161 LCbot.Parameters.bias = 0.5; 162 LCbot.Parameters.gamma = 1; 163 LCbot.Parameters.beta = 1; 164 LCbot.Options.action = -1; 165 LCbot.Options.clip = 1; 166 LCbot.Options.autoMan = 0; 167 LCbot.Parameters.intTime = 100*'s'; 168 LCbot.Parameters.gain = 1; 169 LCbot.Parameters.derivTime = 0*'s'; 170 LCbot.Ports.setPoint = (LR_sp - Hminb)/(Hmaxb-Hminb); 171 LCbot.Ports.input = Had_bot; 172 Had_bot = (col.reb.Level-Hminb)/(Hmaxb-Hminb); 173 col.reb.OutletL.F = Frmin + (Frmax-Frmin) * LCbot.Ports.output; 174 175 "MIMO PID Controller" 176 PID11.Parameters.tau = 0*'s'; 177 PID11.Parameters.tauSet = 0*'s'; 178 PID11.Parameters.alpha = 0.3; 179 PID11.Parameters.bias = 0.1; 180 PID11.Parameters.gamma = 1; 181 PID11.Parameters.beta = 1; 182 PID11.Options.action = -1; 183 PID11.Options.clip = 1; 184 PID11.Options.autoMan = 0; 185 PID11.Parameters.intTime = 60*'s'; 186 PID11.Parameters.gain = 0.6; 187 PID11.Parameters.derivTime = 0*'s'; 188 PID11.Ports.setPoint = xtop_sp; 189 PID11.Ports.input = xtop; 190 191 PID12.Parameters.tau = 0*'s'; 192 PID12.Parameters.tauSet = 0*'s'; 193 PID12.Parameters.alpha = 0.3; 194 PID12.Parameters.bias = 0.0; 195 PID12.Parameters.gamma = 1; 196 PID12.Parameters.beta = 1; 197 PID12.Options.action = -1; 198 PID12.Options.clip = 1; 199 PID12.Options.autoMan = 0; 200 PID12.Parameters.intTime = 100*'s'; 201 PID12.Parameters.gain = 0.5; 202 PID12.Parameters.derivTime = 0*'s'; 203 PID12.Ports.setPoint = xbot_sp; 204 PID12.Ports.input = xbot; 205 206 RR = RRmin + (RRmax-RRmin) * (PID11.Ports.output + PID12.Ports.output); 207 208 PID21.Parameters.tau = 0*'s'; 209 PID21.Parameters.tauSet = 0*'s'; 210 PID21.Parameters.alpha = 0.3; 211 PID21.Parameters.bias = 0.0; 212 PID21.Parameters.gamma = 1; 213 PID21.Parameters.beta = 1; 214 PID21.Options.action = 1; 215 PID21.Options.clip = 1; 216 PID21.Options.autoMan = 0; 217 PID21.Parameters.intTime = 100*'s'; 218 PID21.Parameters.gain = 0.5; 219 PID21.Parameters.derivTime = 0*'s'; 220 PID21.Ports.setPoint = xtop_sp; 221 PID21.Ports.input = xtop; 222 223 PID22.Parameters.tau = 0*'s'; 224 PID22.Parameters.tauSet = 0*'s'; 225 PID22.Parameters.alpha = 0.3; 226 PID22.Parameters.bias = 0.5; 227 PID22.Parameters.gamma = 1; 228 PID22.Parameters.beta = 1; 229 PID22.Options.action = -1; 230 PID22.Options.clip = 1; 231 PID22.Options.autoMan = 0; 232 PID22.Parameters.intTime = 60*'s'; 233 PID22.Parameters.gain = 0.6; 234 PID22.Parameters.derivTime = 0*'s'; 235 PID22.Ports.setPoint = xbot_sp; 236 PID22.Ports.input = xbot; 237 238 Qr.OutletQ.Q = Qrmin + (Qrmax-Qrmin) * (PID21.Ports.output + PID22.Ports.output); 239 240 RR * (col.cond.OutletV.F + col.sptop.Outlet1.F) = col.sptop.Outlet2.F; 241 xtop = col.cond.OutletL.z(4); # benzene 242 xbot = col.reb.OutletL.z(3); # propylene 243 244 if time < 1 * 'h' then 245 feed.Outlet.F = 113.4 * 'kmol/h'; 246 else 247 feed.Outlet.F = 120 * 'kmol/h'; 248 end 249 250 SPECIFY 251 feed.Outlet.T = 290 * 'K'; 252 feed.Outlet.P = 6 * 'bar'; 253 feed.Outlet.z = 1/NComp; 254 255 zero.F = 0 * 'kmol/h'; 256 zero.T = 300 * 'K'; 257 zero.P = 1 * 'atm'; 258 zero.z = 1/NComp; 259 zero.v = 0; 260 zero.h = 0 * 'J/mol'; 261 262 # Qr.OutletQ.Q = 3e6 * 'kJ/h'; 263 col.pump1.dP = 16 * 'kPa'; 264 col.trays.Emv = 1; 265 # col.sptop.Outlet2.F = 75 * 'kmol/h'; # reflux 266 col.alfaTopo = 2; 142 # Qr.OutletQ = 3e6 * 'kJ/h'; 143 pump1.Pincrease = 16 * 'kPa'; 144 # sptop.Reflux.F = 75 * 'kmol/h'; # reflux 145 col.VapourDrawOffFlow = 0 * 'kmol/h' ; 146 col.LiquidDrawOffFlow = 0 * 'kmol/h' ; 267 147 268 148 xtop_sp = 1e-3; # benzene 269 xbot_sp = 5e-5; # propylene270 P_sp = 5.0*'bar';149 xbot_sp = 1e-5; # propylene 150 P_sp = 4.0*'bar'; 271 151 T_sp = (15+273.15) * 'K'; 272 LC_sp = 1.0 * 'm';273 LR_sp = 1.0 * 'm';152 LC_sp = 0.5; 153 LR_sp = 0.5; 274 154 275 155 SET 276 col.NTrays = 8; 277 col.cond.V = 2 * 'm^3'; 278 col.cond.Across = 1 * 'm^2'; 279 col.trays.V = 4 * 'ft^3'; 280 col.trays.Ah = 0.394 * 'ft^2'; 281 col.trays.lw = 20.94 * 'in'; 282 col.trays.hw = 0.125 * 'ft'; 283 col.trays.Q = 0 * 'kW'; 284 col.trays.beta = 0.6; 285 col.trays.alfa = 4; 286 col.trays.Ap = 3.94 * 'ft^2'; 287 col.reb.V = 2 * 'm^3'; 288 col.reb.Across = 1 * 'm^2'; 156 col.FeedTrayLocation(1) = 5; 157 col.NumberOfTrays = 8; 158 col.LiquidSideStreamLocation = 2; 159 col.VapourSideStreamLocation = 2; 160 col.WeirLength = 20.94 * 'in'; 161 col.WeirHeight = 0.125 * 'ft'; 162 col.TrayLiquidPasses = 1; 163 col.HeatSupply = 0 * 'kW' ; 164 col.AerationFraction = 0.6; 165 col.DryPdropCoeff = 4; 166 col.MurphreeEff = 1; 167 168 cond.Geometry.Lenght = 1 * 'm'; 169 cond.Geometry.Diameter = 1 * 'm'; 170 reb.Geometry.Lenght = 2 * 'm'; 171 reb.Geometry.Diameter = 1 * 'm'; 289 172 290 173 # Controllers type … … 298 181 PID22.PID_Select = "Ideal_AW"; 299 182 183 # Temperature Controller 184 TCcond.tau = 1*'s'; 185 TCcond.tauSet = 1*'s'; 186 TCcond.alpha = 0.1; 187 TCcond.bias = 0.5; 188 TCcond.gamma = 1; 189 TCcond.beta = 1; 190 TCcond.Action = "Reverse"; 191 TCcond.Clip = "Clipped"; 192 TCcond.Mode = "Automatic"; 193 TCcond.intTime = 60*'s'; 194 TCcond.gain = 0.6; 195 TCcond.derivTime = 1*'s'; 196 197 # Pressure Controller 198 PC.tau = 1*'s'; 199 PC.tauSet = 1*'s'; 200 PC.alpha = 0.1; 201 PC.bias = 0; 202 PC.gamma = 1; 203 PC.beta = 1; 204 PC.Action = "Direct"; 205 PC.Clip = "Clipped"; 206 PC.Mode = "Automatic"; 207 PC.intTime = 50*'s'; 208 PC.gain = 0.5; 209 PC.derivTime = 1*'s'; 210 211 # Ttop Level Controller 212 LCtop.tau = 1*'s'; 213 LCtop.tauSet = 1*'s'; 214 LCtop.alpha = 0.1; 215 LCtop.bias = 0.5; 216 LCtop.gamma = 1; 217 LCtop.beta = 1; 218 LCtop.Action = "Direct"; 219 LCtop.Clip = "Clipped"; 220 LCtop.Mode = "Automatic"; 221 LCtop.intTime = 20*'s'; 222 LCtop.gain = 1; 223 LCtop.derivTime = 0*'s'; 224 225 # Tbottom Level Controller 226 LCbot.tau = 1*'s'; 227 LCbot.tauSet = 1*'s'; 228 LCbot.alpha = 0.1; 229 LCbot.bias = 0.5; 230 LCbot.gamma = 1; 231 LCbot.beta = 1; 232 LCbot.Action = "Direct"; 233 LCbot.Clip = "Clipped"; 234 LCbot.Mode = "Automatic"; 235 LCbot.intTime = 100*'s'; 236 LCbot.gain = 1.5; 237 LCbot.derivTime = 0*'s'; 238 239 # MIMO PID Controller 240 PID11.tau = 1*'s'; 241 PID11.tauSet = 1*'s'; 242 PID11.alpha = 0.1; 243 PID11.bias = 0.1; 244 PID11.gamma = 1; 245 PID11.beta = 1; 246 PID11.Action = "Direct"; 247 PID11.Clip = "Clipped"; 248 PID11.Mode = "Automatic"; 249 PID11.intTime = 60*'s'; 250 PID11.gain = 0.6; 251 PID11.derivTime = 0*'s'; 252 253 PID12.tau = 1*'s'; 254 PID12.tauSet = 1*'s'; 255 PID12.alpha = 0.1; 256 PID12.bias = 0.0; 257 PID12.gamma = 1; 258 PID12.beta = 1; 259 PID12.Action = "Direct"; 260 PID12.Clip = "Clipped"; 261 PID12.Mode = "Automatic"; 262 PID12.intTime = 100*'s'; 263 PID12.gain = 0.5; 264 PID12.derivTime = 0*'s'; 265 266 PID21.tau = 1*'s'; 267 PID21.tauSet = 1*'s'; 268 PID21.alpha = 0.1; 269 PID21.bias = 0.0; 270 PID21.gamma = 1; 271 PID21.beta = 1; 272 PID21.Action = "Reverse"; 273 PID21.Clip = "Clipped"; 274 PID21.Mode = "Automatic"; 275 PID21.intTime = 100*'s'; 276 PID21.gain = 0.5; 277 PID21.derivTime = 0*'s'; 278 279 PID22.tau = 1*'s'; 280 PID22.tauSet = 1*'s'; 281 PID22.alpha = 0.1; 282 PID22.bias = 0.5; 283 PID22.gamma = 1; 284 PID22.beta = 1; 285 PID22.Action = "Direct"; 286 PID22.Clip = "Clipped"; 287 PID22.Mode = "Automatic"; 288 PID22.intTime = 60*'s'; 289 PID22.gain = 0.6; 290 PID22.derivTime = 0*'s'; 291 292 PC.MinOutput = 0; 293 PC.MaxOutput = 120; 294 PC.MinInput = 0.5; 295 PC.MaxInput = 10; 296 LCtop.MinInput = 0; 297 LCtop.MaxInput = 1; 298 LCtop.MinOutput = 0; 299 LCtop.MaxOutput = 120; 300 LCbot.MinInput = 0; 301 LCbot.MaxInput = 1; 302 LCbot.MinOutput = 0; 303 LCbot.MaxOutput = 60; 304 TCcond.MaxOutput = -5e5; 305 TCcond.MinOutput = -5e6; 306 TCcond.MaxInput = (30+273.15); 307 TCcond.MinInput = (-20+273.15); 308 PID11.MinInput = 0; 309 PID12.MinInput = 0; 310 PID21.MinInput = 0; 311 PID22.MinInput = 0; 312 PID11.MaxInput = 1; 313 PID12.MaxInput = 1; 314 PID21.MaxInput = 1; 315 PID22.MaxInput = 1; 316 RRmax = 5; 317 RRmin = 0.1; 300 318 Qrmax = 5e6 * 'kJ/h'; 301 319 Qrmin = 1e6 * 'kJ/h'; 302 Frmin = 0 * 'kmol/h'; 303 Frmax = 60 * 'kmol/h'; 304 Fcmin = 0 * 'kmol/h'; 305 Fcmax = 120 * 'kmol/h'; 306 Hmint = 0 * 'm'; 307 Hmaxt = 2 * 'm'; 308 Hminb = 0 * 'm'; 309 Hmaxb = 2 * 'm'; 310 Pmin = 0.5 * 'bar'; 311 Pmax = 10 * 'bar'; 312 Qcmax = -5e5 * 'kJ/h'; 313 Qcmin = -5e6 * 'kJ/h'; 314 Tmax = (30+273.15) * 'K'; 315 Tmin = (-20+273.15) * 'K'; 316 RRmax = 5; 317 RRmin = 0.1; 318 319 INITIAL 320 321 # Initial condition 320 322 # condenser 321 co l.cond.OutletL.T = 260 *'K';322 co l.cond.Level = 1 * 'm';323 co l.cond.OutletL.z([1:4]) = [0.2, 0.2, 0.4, 0.05];323 cond.Levelpercent_Initial = 0.5; 324 cond.Initial_Temperature = 260 *'K'; 325 cond.Initial_Composition = [0.2, 0.2, 0.4, 0.05, 0.15]; 324 326 325 327 # reboiler 326 col.reb.OutletL.T = 350 *'K';327 col.reb.Level = 1 * 'm';328 col.reb.OutletL.z([1:4]) = [0.1, 0.4, 0.1, 0.3];328 reb.Levelpercent_Initial = 0.5; 329 reb.Initial_Temperature = 350 *'K'; 330 reb.Initial_Composition = [0.1, 0.4, 0.1, 0.3, 0.1]; 329 331 330 332 # column trays 331 col.trays.OutletL.T = [290:(330-290)/(col.NTrays-1):330] * 'K'; 332 col.trays.Level = 1.2 * col.trays.hw; 333 col.trays.OutletL.z([1:4]) = [0.15, 0.3, 0.25, 0.2]; 333 col.INITIALIZATION.TopTemperature = 290 * 'K'; 334 col.INITIALIZATION.BottomTemperature = 330 * 'K'; 335 col.INITIALIZATION.LevelFraction = 0.1; 336 col.INITIALIZATION.TopComposition = [0.2, 0.2, 0.4, 0.05, 0.15]; 337 col.INITIALIZATION.BottomComposition = [0.1, 0.4, 0.1, 0.3, 0.1]; 334 338 335 339 OPTIONS 336 340 TimeStep = 0.1; 337 TimeEnd = 6;341 TimeEnd = 5; 338 342 TimeUnit = 'h'; 339 343 InitialFile = "Column_MPID.rlt"; … … 342 346 #Dynamic = false; 343 347 end 344 *# 348 -
branches/gui/sample/controllers/sample_PID_MIMO.mso
r735 r910 24 24 * Author: Argimiro R. Secchi 25 25 * $Id: sample_PID_MIMO.mso 313 2007-07-14 16:45:55Z arge $ 26 *-------------------------------------------------------------------- #26 *--------------------------------------------------------------------*# 27 27 28 28 using "stage_separators/column"; … … 41 41 NComp as Integer; 42 42 43 Qcmin as heat_rate (Brief="Minimum Condenser Heat supplied");44 Qcmax as heat_rate (Brief="Maximum Condenser Heat supplied");45 43 Qrmin as heat_rate (Brief="Minimum Reboiler Heat supplied"); 46 44 Qrmax as heat_rate (Brief="Maximum Reboiler Heat supplied"); 47 Frmin as flow_mol (Brief="Minimum bottom flow rate");48 Frmax as flow_mol (Brief="Maximum bottom flow rate");49 Fcmin as flow_mol (Brief="Minimum reflux flow rate");50 Fcmax as flow_mol (Brief="Maximum reflux flow rate");51 Hmint as length (Brief="Minimum liquid level in top tank");52 Hmaxt as length (Brief="Maximum liquid level in top tank");53 Hminb as length (Brief="Minimum liquid level in reboiler");54 Hmaxb as length (Brief="Maximum liquid level in reboiler");55 Pmax as pressure (Brief="Maximum column pressure");56 Pmin as pressure (Brief="Minimum column pressure");57 Tmax as temperature (Brief="Maximum column temperature");58 Tmin as temperature (Brief="Minimum column temperature");59 45 RRmax as positive (Brief="Maximum reflux ratio"); 60 46 RRmin as positive (Brief="Minimum reflux ratio"); … … 63 49 Qc as energy_source (Brief="Heat rate removed from condenser"); 64 50 Qr as energy_source (Brief="Heat rate supplied to reboiler"); 65 Had_top as Real (Brief="Dimensionless condenser level");66 Had_bot as Real (Brief="Dimensionless reboiler level");67 Pad as Real (Brief="Dimensionless pressure");68 51 P_sp as pressure (Brief="Pressure setpoint"); 69 Tad as Real (Brief="Dimensionless temperature");70 52 T_sp as temperature (Brief="Condenser temperature setpoint"); 71 53 RR as positive (Brief="Reflux ratio"); 72 LC_sp as length(Brief="Condenser level setpoint");73 LR_sp as length(Brief="Reboiler level setpoint");74 xtop as fraction (Brief="Controlled top composition");75 xbot as fraction (Brief="Controlled bottom composition");54 LC_sp as fraction (Brief="Condenser level setpoint"); 55 LR_sp as fraction (Brief="Reboiler level setpoint"); 56 out xtop as fraction (Brief="Controlled top composition"); 57 out xbot as fraction (Brief="Controlled bottom composition"); 76 58 xtop_sp as fraction (Brief="Controlled top composition setpoint"); 77 59 xbot_sp as fraction (Brief="Controlled bottom composition setpoint"); … … 81 63 82 64 DEVICES 83 col as Distillation_kettle_cond; 65 col as Section_Column; 66 cond as condenser; 67 reb as reboiler; 68 sptop as splitter_column; 69 pump1 as pump; 70 # Valve_Distillate as valve_flow; 71 # Valve_Bottom as valve_flow; 84 72 feed as source; 85 zero as stream;86 73 TCcond as PIDIncr; 87 74 LCtop as PIDIncr; … … 94 81 95 82 CONNECTIONS 96 feed.Outlet to col.trays(5).Inlet; 97 zero to col.reb.Inlet; 98 zero to col.trays([1:4]).Inlet; 99 zero to col.trays([6:col.NTrays]).Inlet; 100 Qc.OutletQ to col.cond.InletQ; 101 Qr.OutletQ to col.reb.InletQ; 83 feed.Outlet to col.FeedTray; 84 Qc.OutletQ to cond.InletQ; 85 Qr.OutletQ to reb.InletQ; 86 # sptop.Distillate to Valve_Distillate.Inlet; 87 sptop.Reflux to pump1.Inlet; 88 pump1.Outlet to col.LiquidInlet; 89 col.VapourOutlet to cond.InletVapour; 90 cond.OutletLiquid to sptop.Inlet; 91 col.LiquidOutlet to reb.InletLiquid; 92 reb.OutletVapour to col.VapourInlet; 93 # reb.OutletLiquid to Valve_Bottom.Inlet; 94 cond.TI to TCcond.Input; 95 cond.PI to PC.Input; 96 cond.LI to LCtop.Input; 97 reb.LI to LCbot.Input; 98 xtop to PID11.Input; 99 xbot to PID12.Input; 100 xtop to PID21.Input; 101 xbot to PID22.Input; 102 102 103 103 EQUATIONS 104 "Temperature Controller" 105 TCcond.Parameters.tau = 0*'s'; 106 TCcond.Parameters.tauSet = 0*'s'; 107 TCcond.Parameters.alpha = 0.3; 108 TCcond.Parameters.bias = 0.5; 109 TCcond.Parameters.gamma = 1; 110 TCcond.Parameters.beta = 1; 111 TCcond.Options.action = 1; 112 TCcond.Options.clip = 1; 113 TCcond.Options.autoMan = 0; 114 TCcond.Parameters.intTime = 60*'s'; 115 TCcond.Parameters.gain = 0.6; 116 TCcond.Parameters.derivTime = 1*'s'; 117 TCcond.Ports.setPoint = (T_sp - Tmin)/(Tmax-Tmin); 118 TCcond.Ports.input = Tad; 119 Tad = (col.cond.OutletL.T-Tmin)/(Tmax-Tmin); 120 Qc.OutletQ.Q = Qcmin+(Qcmax-Qcmin)*TCcond.Ports.output; 121 122 "Pressure Controller" 123 PC.Parameters.tau = 0*'s'; 124 PC.Parameters.tauSet = 0*'s'; 125 PC.Parameters.alpha = 0.3; 126 PC.Parameters.bias = 0; 127 PC.Parameters.gamma = 1; 128 PC.Parameters.beta = 1; 129 PC.Options.action = -1; 130 PC.Options.clip = 1; 131 PC.Options.autoMan = 0; 132 PC.Parameters.intTime = 50*'s'; 133 PC.Parameters.gain = 0.5; 134 PC.Parameters.derivTime = 1*'s'; 135 PC.Ports.setPoint = (P_sp-Pmin)/(Pmax-Pmin); 136 PC.Ports.input = Pad; 137 Pad = (col.cond.OutletV.P-Pmin)/(Pmax-Pmin); 138 col.cond.OutletV.F = (Fcmin+(Fcmax-Fcmin)*PC.Ports.output); 104 105 TCcond.SetPoint * 'K' = T_sp; 106 Qc.OutletQ = TCcond.Output * 'kJ/h'; 107 108 PC.SetPoint * 'bar' = P_sp; 109 cond.OutletVapour.F = PC.Output * 'kmol/h'; 110 111 LCtop.SetPoint = LC_sp; 112 sptop.Distillate.F = LCtop.Output * 'kmol/h'; 113 114 LCbot.SetPoint = LR_sp; 115 reb.OutletLiquid.F = LCbot.Output * 'kmol/h'; 116 117 "MIMO PID Controller" 118 PID11.SetPoint = xtop_sp; 119 PID12.SetPoint = xbot_sp; 120 121 RR = RRmin + (RRmax-RRmin) * (PID11.Output + PID12.Output); 122 123 PID21.SetPoint = xtop_sp; 124 PID22.SetPoint = xbot_sp; 125 126 Qr.OutletQ = Qrmin + (Qrmax-Qrmin) * (PID21.Output + PID22.Output); 127 128 RR * (cond.OutletVapour.F + sptop.Distillate.F) = sptop.Reflux.F; 129 xtop = cond.OutletLiquid.z(4); # benzene 130 xbot = reb.OutletLiquid.z(3); # propylene 131 132 if time < 1 * 'h' then 133 feed.F = 113.4 * 'kmol/h'; 134 else 135 feed.F = 120 * 'kmol/h'; 136 end 137 138 SPECIFY 139 feed.T = 291 * 'K'; 140 feed.P = 568.3 * 'kPa'; 141 feed.Composition = 1/NComp; 139 142 140 "Ttop Level Controller" 141 LCtop.Parameters.tau = 0*'s'; 142 LCtop.Parameters.tauSet = 0*'s'; 143 LCtop.Parameters.alpha = 0.3; 144 LCtop.Parameters.bias = 0.5; 145 LCtop.Parameters.gamma = 1; 146 LCtop.Parameters.beta = 1; 147 LCtop.Options.action = -1; 148 LCtop.Options.clip = 1; 149 LCtop.Options.autoMan = 0; 150 LCtop.Parameters.intTime = 20*'s'; 151 LCtop.Parameters.gain = 1; 152 LCtop.Parameters.derivTime = 0*'s'; 153 LCtop.Ports.setPoint = (LC_sp - Hmint)/(Hmaxt-Hmint); 154 LCtop.Ports.input = Had_top; 155 Had_top = (col.cond.Level-Hmint)/(Hmaxt-Hmint); 156 col.sptop.Outlet1.F = Fcmin + (Fcmax-Fcmin) * LCtop.Ports.output; 157 158 "Tbottom Level Controller" 159 LCbot.Parameters.tau = 0*'s'; 160 LCbot.Parameters.tauSet = 0*'s'; 161 LCbot.Parameters.alpha = 0.3; 162 LCbot.Parameters.bias = 0.5; 163 LCbot.Parameters.gamma = 1; 164 LCbot.Parameters.beta = 1; 165 LCbot.Options.action = -1; 166 LCbot.Options.clip = 1; 167 LCbot.Options.autoMan = 0; 168 LCbot.Parameters.intTime = 100*'s'; 169 LCbot.Parameters.gain = 1; 170 LCbot.Parameters.derivTime = 0*'s'; 171 LCbot.Ports.setPoint = (LR_sp - Hminb)/(Hmaxb-Hminb); 172 LCbot.Ports.input = Had_bot; 173 Had_bot = (col.reb.Level-Hminb)/(Hmaxb-Hminb); 174 col.reb.OutletL.F = Frmin + (Frmax-Frmin) * LCbot.Ports.output; 175 176 "MIMO PID Controller" 177 PID11.Parameters.tau = 0*'s'; 178 PID11.Parameters.tauSet = 0*'s'; 179 PID11.Parameters.alpha = 0.3; 180 PID11.Parameters.bias = 0.1; 181 PID11.Parameters.gamma = 1; 182 PID11.Parameters.beta = 1; 183 PID11.Options.action = -1; 184 PID11.Options.clip = 1; 185 PID11.Options.autoMan = 0; 186 PID11.Parameters.intTime = 60*'s'; 187 PID11.Parameters.gain = 0.6; 188 PID11.Parameters.derivTime = 0*'s'; 189 PID11.Ports.setPoint = xtop_sp; 190 PID11.Ports.input = xtop; 191 192 PID12.Parameters.tau = 0*'s'; 193 PID12.Parameters.tauSet = 0*'s'; 194 PID12.Parameters.alpha = 0.3; 195 PID12.Parameters.bias = 0.0; 196 PID12.Parameters.gamma = 1; 197 PID12.Parameters.beta = 1; 198 PID12.Options.action = -1; 199 PID12.Options.clip = 1; 200 PID12.Options.autoMan = 0; 201 PID12.Parameters.intTime = 100*'s'; 202 PID12.Parameters.gain = 0.5; 203 PID12.Parameters.derivTime = 0*'s'; 204 PID12.Ports.setPoint = xbot_sp; 205 PID12.Ports.input = xbot; 206 207 RR = RRmin + (RRmax-RRmin) * (PID11.Ports.output + PID12.Ports.output); 208 209 PID21.Parameters.tau = 0*'s'; 210 PID21.Parameters.tauSet = 0*'s'; 211 PID21.Parameters.alpha = 0.3; 212 PID21.Parameters.bias = 0.0; 213 PID21.Parameters.gamma = 1; 214 PID21.Parameters.beta = 1; 215 PID21.Options.action = 1; 216 PID21.Options.clip = 1; 217 PID21.Options.autoMan = 0; 218 PID21.Parameters.intTime = 100*'s'; 219 PID21.Parameters.gain = 0.5; 220 PID21.Parameters.derivTime = 0*'s'; 221 PID21.Ports.setPoint = xtop_sp; 222 PID21.Ports.input = xtop; 223 224 PID22.Parameters.tau = 0*'s'; 225 PID22.Parameters.tauSet = 0*'s'; 226 PID22.Parameters.alpha = 0.3; 227 PID22.Parameters.bias = 0.5; 228 PID22.Parameters.gamma = 1; 229 PID22.Parameters.beta = 1; 230 PID22.Options.action = -1; 231 PID22.Options.clip = 1; 232 PID22.Options.autoMan = 0; 233 PID22.Parameters.intTime = 60*'s'; 234 PID22.Parameters.gain = 0.6; 235 PID22.Parameters.derivTime = 0*'s'; 236 PID22.Ports.setPoint = xbot_sp; 237 PID22.Ports.input = xbot; 238 239 Qr.OutletQ.Q = Qrmin + (Qrmax-Qrmin) * (PID21.Ports.output + PID22.Ports.output); 240 241 RR * (col.cond.OutletV.F + col.sptop.Outlet1.F) = col.sptop.Outlet2.F; 242 xtop = col.cond.OutletL.z(4); # benzene 243 xbot = col.reb.OutletL.z(3); # propylene 244 245 if time < 1 * 'h' then 246 feed.Outlet.F = 113.4 * 'kmol/h'; 247 else 248 feed.Outlet.F = 120 * 'kmol/h'; 249 end 250 251 SPECIFY 252 feed.Outlet.T = 291 * 'K'; 253 feed.Outlet.P = 568.3 * 'kPa'; 254 feed.Outlet.z = 1/NComp; 255 256 zero.F = 0 * 'kmol/h'; 257 zero.T = 300 * 'K'; 258 zero.P = 1 * 'atm'; 259 zero.z = 1/NComp; 260 zero.v = 0; 261 zero.h = 0 * 'J/mol'; 262 263 # Qr.OutletQ.Q = 3e6 * 'kJ/h'; 264 col.pump1.dP = 16 * 'kPa'; 265 col.trays.Emv = 1; 266 # col.sptop.Outlet2.F = 75 * 'kmol/h'; # reflux 267 col.alfaTopo = 2; 143 # Qr.OutletQ = 3e6 * 'kJ/h'; 144 pump1.Pincrease = 16 * 'kPa'; 145 # sptop.Reflux.F = 75 * 'kmol/h'; # reflux 146 col.VapourDrawOffFlow = 0 * 'kmol/h' ; 147 col.LiquidDrawOffFlow = 0 * 'kmol/h' ; 268 148 269 149 xtop_sp = 1e-3; # benzene … … 271 151 P_sp = 4.0*'bar'; 272 152 T_sp = (15+273.15) * 'K'; 273 LC_sp = 1.0 * 'm';274 LR_sp = 1.0 * 'm';153 LC_sp = 0.5; 154 LR_sp = 0.5; 275 155 276 156 SET 277 col.NTrays = 8; 278 col.cond.V = 2 * 'm^3'; 279 col.cond.Across = 1 * 'm^2'; 280 col.trays.V = 4 * 'ft^3'; 281 col.trays.Ah = 0.394 * 'ft^2'; 282 col.trays.lw = 20.94 * 'in'; 283 col.trays.hw = 0.125 * 'ft'; 284 col.trays.Q = 0 * 'kW'; 285 col.trays.beta = 0.6; 286 col.trays.alfa = 4; 287 col.trays.Ap = 3.94 * 'ft^2'; 288 col.reb.V = 2 * 'm^3'; 289 col.reb.Across = 1 * 'm^2'; 157 col.FeedTrayLocation(1) = 5; 158 col.NumberOfTrays = 8; 159 col.LiquidSideStreamLocation = 2; 160 col.VapourSideStreamLocation = 2; 161 col.WeirLength = 20.94 * 'in'; 162 col.WeirHeight = 0.125 * 'ft'; 163 col.TrayLiquidPasses = 1; 164 col.HeatSupply = 0 * 'kW' ; 165 col.AerationFraction = 0.6; 166 col.DryPdropCoeff = 4; 167 col.MurphreeEff = 1; 168 169 cond.Geometry.Lenght = 1 * 'm'; 170 cond.Geometry.Diameter = 1 * 'm'; 171 reb.Geometry.Lenght = 2 * 'm'; 172 reb.Geometry.Diameter = 1 * 'm'; 290 173 291 174 # Controllers type … … 299 182 PID22.PID_Select = "Ideal_AW"; 300 183 184 # Temperature Controller 185 TCcond.tau = 1*'s'; 186 TCcond.tauSet = 1*'s'; 187 TCcond.alpha = 0.1; 188 TCcond.bias = 0.5; 189 TCcond.gamma = 1; 190 TCcond.beta = 1; 191 TCcond.Action = "Reverse"; 192 TCcond.Clip = "Clipped"; 193 TCcond.Mode = "Automatic"; 194 TCcond.intTime = 60*'s'; 195 TCcond.gain = 0.6; 196 TCcond.derivTime = 1*'s'; 197 198 # Pressure Controller 199 PC.tau = 1*'s'; 200 PC.tauSet = 1*'s'; 201 PC.alpha = 0.1; 202 PC.bias = 0; 203 PC.gamma = 1; 204 PC.beta = 1; 205 PC.Action = "Direct"; 206 PC.Clip = "Clipped"; 207 PC.Mode = "Automatic"; 208 PC.intTime = 50*'s'; 209 PC.gain = 0.5; 210 PC.derivTime = 1*'s'; 211 212 # Ttop Level Controller 213 LCtop.tau = 1*'s'; 214 LCtop.tauSet = 1*'s'; 215 LCtop.alpha = 0.1; 216 LCtop.bias = 0.5; 217 LCtop.gamma = 1; 218 LCtop.beta = 1; 219 LCtop.Action = "Direct"; 220 LCtop.Clip = "Clipped"; 221 LCtop.Mode = "Automatic"; 222 LCtop.intTime = 20*'s'; 223 LCtop.gain = 1; 224 LCtop.derivTime = 0*'s'; 225 226 # Tbottom Level Controller 227 LCbot.tau = 1*'s'; 228 LCbot.tauSet = 1*'s'; 229 LCbot.alpha = 0.1; 230 LCbot.bias = 0.5; 231 LCbot.gamma = 1; 232 LCbot.beta = 1; 233 LCbot.Action = "Direct"; 234 LCbot.Clip = "Clipped"; 235 LCbot.Mode = "Automatic"; 236 LCbot.intTime = 100*'s'; 237 LCbot.gain = 1.5; 238 LCbot.derivTime = 0*'s'; 239 240 # MIMO PID Controller 241 PID11.tau = 1*'s'; 242 PID11.tauSet = 1*'s'; 243 PID11.alpha = 0.1; 244 PID11.bias = 0.1; 245 PID11.gamma = 1; 246 PID11.beta = 1; 247 PID11.Action = "Direct"; 248 PID11.Clip = "Clipped"; 249 PID11.Mode = "Automatic"; 250 PID11.intTime = 60*'s'; 251 PID11.gain = 0.6; 252 PID11.derivTime = 0*'s'; 253 254 PID12.tau = 1*'s'; 255 PID12.tauSet = 1*'s'; 256 PID12.alpha = 0.1; 257 PID12.bias = 0.0; 258 PID12.gamma = 1; 259 PID12.beta = 1; 260 PID12.Action = "Direct"; 261 PID12.Clip = "Clipped"; 262 PID12.Mode = "Automatic"; 263 PID12.intTime = 100*'s'; 264 PID12.gain = 0.5; 265 PID12.derivTime = 0*'s'; 266 267 PID21.tau = 1*'s'; 268 PID21.tauSet = 1*'s'; 269 PID21.alpha = 0.1; 270 PID21.bias = 0.0; 271 PID21.gamma = 1; 272 PID21.beta = 1; 273 PID21.Action = "Reverse"; 274 PID21.Clip = "Clipped"; 275 PID21.Mode = "Automatic"; 276 PID21.intTime = 100*'s'; 277 PID21.gain = 0.5; 278 PID21.derivTime = 0*'s'; 279 280 PID22.tau = 1*'s'; 281 PID22.tauSet = 1*'s'; 282 PID22.alpha = 0.1; 283 PID22.bias = 0.5; 284 PID22.gamma = 1; 285 PID22.beta = 1; 286 PID22.Action = "Direct"; 287 PID22.Clip = "Clipped"; 288 PID22.Mode = "Automatic"; 289 PID22.intTime = 60*'s'; 290 PID22.gain = 0.6; 291 PID22.derivTime = 0*'s'; 292 293 PC.MinOutput = 0; 294 PC.MaxOutput = 120; 295 PC.MinInput = 0.5; 296 PC.MaxInput = 10; 297 LCtop.MinInput = 0; 298 LCtop.MaxInput = 1; 299 LCtop.MinOutput = 0; 300 LCtop.MaxOutput = 120; 301 LCbot.MinInput = 0; 302 LCbot.MaxInput = 1; 303 LCbot.MinOutput = 0; 304 LCbot.MaxOutput = 60; 305 TCcond.MaxOutput = -5e5; 306 TCcond.MinOutput = -5e6; 307 TCcond.MaxInput = (30+273.15); 308 TCcond.MinInput = (-20+273.15); 309 PID11.MinInput = 0; 310 PID12.MinInput = 0; 311 PID21.MinInput = 0; 312 PID22.MinInput = 0; 313 PID11.MaxInput = 1; 314 PID12.MaxInput = 1; 315 PID21.MaxInput = 1; 316 PID22.MaxInput = 1; 317 RRmax = 5; 318 RRmin = 0.1; 301 319 Qrmax = 5e6 * 'kJ/h'; 302 320 Qrmin = 1e6 * 'kJ/h'; 303 Frmin = 0 * 'kmol/h'; 304 Frmax = 60 * 'kmol/h'; 305 Fcmin = 0 * 'kmol/h'; 306 Fcmax = 120 * 'kmol/h'; 307 Hmint = 0 * 'm'; 308 Hmaxt = 2 * 'm'; 309 Hminb = 0 * 'm'; 310 Hmaxb = 2 * 'm'; 311 Pmin = 0.5 * 'bar'; 312 Pmax = 10 * 'bar'; 313 Qcmax = -5e5 * 'kJ/h'; 314 Qcmin = -5e6 * 'kJ/h'; 315 Tmax = (30+273.15) * 'K'; 316 Tmin = (-20+273.15) * 'K'; 317 RRmax = 5; 318 RRmin = 0.1; 319 320 INITIAL 321 322 # Initial condition 321 323 # condenser 322 co l.cond.OutletL.T = 260 *'K';323 co l.cond.Level = 1 * 'm';324 co l.cond.OutletL.z([1:4]) = [0.2, 0.2, 0.4, 0.05];324 cond.Levelpercent_Initial = 0.5; 325 cond.Initial_Temperature = 260 *'K'; 326 cond.Initial_Composition = [0.2, 0.2, 0.4, 0.05, 0.15]; 325 327 326 328 # reboiler 327 col.reb.OutletL.T = 350 *'K';328 col.reb.Level = 1 * 'm';329 col.reb.OutletL.z([1:4]) = [0.1, 0.4, 0.1, 0.3];329 reb.Levelpercent_Initial = 0.5; 330 reb.Initial_Temperature = 350 *'K'; 331 reb.Initial_Composition = [0.1, 0.4, 0.1, 0.3, 0.1]; 330 332 331 333 # column trays 332 col.trays.OutletL.T = [290:(330-290)/(col.NTrays-1):330] * 'K'; 333 col.trays.Level = 1.2 * col.trays.hw; 334 col.trays.OutletL.z([1:4]) = [0.15, 0.3, 0.25, 0.2]; 334 col.INITIALIZATION.TopTemperature = 290 * 'K'; 335 col.INITIALIZATION.BottomTemperature = 330 * 'K'; 336 col.INITIALIZATION.LevelFraction = 0.1; 337 col.INITIALIZATION.TopComposition = [0.2, 0.2, 0.4, 0.05, 0.15]; 338 col.INITIALIZATION.BottomComposition = [0.1, 0.4, 0.1, 0.3, 0.1]; 335 339 336 340 OPTIONS … … 338 342 TimeEnd = 5; 339 343 TimeUnit = 'h'; 340 InitialFile = "Column_ ctrl.rlt";344 InitialFile = "Column_MPID.rlt"; 341 345 DAESolver(File="dassl"); 342 #GuessFile = "Column_ ctrl.rlt";346 #GuessFile = "Column_MPID.rlt"; 343 347 #Dynamic = false; 344 348 end -
branches/gui/sample/controllers/sample_tanks_pid.mso
r735 r910 20 20 * Author: Tiago Osório 21 21 * $Id$ 22 *----------------------------------------------------------------- #22 *-----------------------------------------------------------------*# 23 23 24 24 using "tanksmodel"; … … 32 32 PIDc as PIDIncr; 33 33 34 PARAMETERS35 h_max as Real (Brief="Altura máxima do nível do tanque", Unit='m');36 h_min as Real (Brief="Altura mínima do nível do tanque", Unit='m');37 38 34 VARIABLES 39 h_ad as Real (Brief="Altura adimensional do nível do tanque", Lower=0,Upper=1);35 out LI as control_signal (Brief="Level Indicator"); 40 36 41 37 CONNECTIONS 38 LI to PIDc.Input; 42 39 43 40 SET 44 41 Tanque1.A = 8 * 'm^2'; 45 h_max = 2 * 'm';46 h_min = 0 * 'm';42 PIDc.MaxInput = 2; 43 PIDc.MinInput = 0; 47 44 PIDc.PID_Select = "Ideal_AWBT"; 48 45 … … 62 59 EQUATIONS 63 60 64 PIDc.Ports.input = h_ad; 65 h_ad = (Tanque1.h-h_min)/(h_max-h_min); 66 Tanque1.k = 8*'m^2.5/h'*PIDc.Ports.output; 61 Tanque1.k = 8*'m^2.5/h'*PIDc.Output; 67 62 68 #Perturbação servo 69 #Nível desejado=1*'m' 70 PIDc.Ports.setPoint=0.5; 63 "Level sensor" 64 LI * 'm' = Tanque1.h; 71 65 72 #Perturbação regulatória 66 #Setpoint tracking 67 PIDc.SetPoint=1; 68 69 #Disturbance rejection 73 70 if time<10*'h' then 74 71 Tanque1.Fin= 3*'m^3/h'; … … 92 89 PIDx as PID; 93 90 94 PARAMETERS95 h_max as Real (Brief="Altura máxima do nível do tanque", Unit='m');96 h_min as Real (Brief="Altura mínima do nível do tanque", Unit='m');97 98 91 VARIABLES 99 h_ad as Real (Brief="Altura adimensional do nível do tanque", Lower=0,Upper=1);92 out LI as control_signal (Brief="Level Indicator"); 100 93 101 94 CONNECTIONS 95 LI to PIDx.Input; 102 96 103 97 SET 104 98 Tanque1.A = 8 * 'm^2'; 105 h_max = 2 * 'm';106 h_min = 0 * 'm';99 PIDx.MaxInput = 2; 100 PIDx.MinInput = 0; 107 101 PIDx.PID_Select = "Ideal_AWBT"; 108 102 … … 122 116 EQUATIONS 123 117 124 PIDx.Ports.input = h_ad; 125 h_ad = (Tanque1.h-h_min)/(h_max-h_min); 126 Tanque1.k = 8*'m^2.5/h'*PIDx.Ports.output; 118 Tanque1.k = 8*'m^2.5/h'*PIDx.Output; 127 119 128 #Perturbação servo 129 #Nível desejado=1*'m' 130 PIDx.Ports.setPoint=0.5; 120 "Level sensor" 121 LI * 'm' = Tanque1.h; 131 122 132 #Perturbação regulatória 123 #Setpoint tracking 124 PIDx.SetPoint=1; 125 126 #Disturbance rejection 133 127 if time<10*'h' then 134 128 Tanque1.Fin= 3*'m^3/h';
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