Changeset 645 for branches/gui
- Timestamp:
- Sep 30, 2008, 3:29:17 PM (14 years ago)
- Location:
- branches/gui
- Files:
-
- 2 edited
-
eml/stage_separators/columnTeste.mso (modified) (4 diffs)
-
sample/stage_separators/Column_Distillation_Kettle_Diagram.pfd (modified) (97 diffs)
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/stage_separators/columnTeste.mso
r644 r645 322 322 * - NumberOfTrays like tray; 323 323 * - a kettle reboiler; 324 * - dy mamic condenser;324 * - dynamic condenser; 325 325 * - a splitter which separate reflux and distillate; 326 326 * - a pump in reflux stream; … … 370 370 RebNoFlow as sourceNoFlow (Brief="No Inlet Flow to Reboiler",Hidden=true); 371 371 372 out VapourDistillate as vapour_stream (Brief="Vapour outlet stream From Top Condenser", PosX=0.72, PosY=0); 373 in ConnectorCondenserVout as stream (Brief="Connector for Vapour outlet stream From Top Condenser", Hidden=true); 374 375 out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.47); 376 in ConnectorSplitterOut as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true); 377 378 out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Reboiler", PosX=1, PosY=1); 379 in ConnectorReboilerLout as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true); 380 372 381 EQUATIONS 373 382 … … 384 393 385 394 end 395 396 # Condenser Connector Equations 397 ConnectorCondenserVout.T = VapourDistillate.T; 398 ConnectorCondenserVout.P = VapourDistillate.P; 399 ConnectorCondenserVout.F = VapourDistillate.F; 400 ConnectorCondenserVout.z = VapourDistillate.z; 401 402 # Splitter Connector Equations 403 ConnectorSplitterOut.T = LiquidDistillate.T; 404 ConnectorSplitterOut.P = LiquidDistillate.P; 405 ConnectorSplitterOut.F = LiquidDistillate.F; 406 ConnectorSplitterOut.z = LiquidDistillate.z; 407 408 # Reboiler Connector Equations 409 ConnectorReboilerLout.T = BottomProduct.T; 410 ConnectorReboilerLout.P = BottomProduct.P; 411 ConnectorReboilerLout.F = BottomProduct.F; 412 ConnectorReboilerLout.z = BottomProduct.z; 386 413 387 414 CONNECTIONS … … 400 427 HeatToCondenser to CondenserUnity.InletQ; 401 428 RebNoFlow.Outlet to ReboilerUnity.Inlet; 429 430 CondenserUnity.OutletV to ConnectorCondenserVout; 431 SplitterTop.Outlet1 to ConnectorSplitterOut; 432 ReboilerUnity.OutletL to ConnectorReboilerLout; 402 433 403 434 end -
branches/gui/sample/stage_separators/Column_Distillation_Kettle_Diagram.pfd
r644 r645 78 78 <Desc>NComp</Desc> 79 79 <Index>0</Index> 80 <Values> 2</Values>80 <Values>5</Values> 81 81 <Status>0</Status> 82 82 </Parameters> … … 105 105 <Desc>h</Desc> 106 106 <Index>0</Index> 107 <Values>- 27164.3</Values>107 <Values>-15790.9</Values> 108 108 <Status>0</Status> 109 109 <Unit>kJ/kmol</Unit> … … 112 112 <Desc>v</Desc> 113 113 <Index>0</Index> 114 <Values>0 </Values>114 <Values>0.429005</Values> 115 115 <Status>0</Status> 116 116 </Variables> … … 118 118 <Desc>z</Desc> 119 119 <Index>0</Index> 120 <Values>0. 5</Values>120 <Values>0.2</Values> 121 121 <Status>0</Status> 122 122 <Index>1</Index> 123 <Values>0.5</Values> 123 <Values>0.2</Values> 124 <Status>0</Status> 125 <Index>2</Index> 126 <Values>0.2</Values> 127 <Status>0</Status> 128 <Index>3</Index> 129 <Values>0.2</Values> 130 <Status>0</Status> 131 <Index>4</Index> 132 <Values>0.2</Values> 124 133 <Status>0</Status> 125 134 </Variables> … … 137 146 <Desc>NComp</Desc> 138 147 <Index>0</Index> 139 <Values> 2</Values>148 <Values>5</Values> 140 149 <Status>0</Status> 141 150 </Parameters> … … 147 156 <Unit>kg/kmol</Unit> 148 157 <Index>1</Index> 158 <Values>72.1498</Values> 159 <Status>0</Status> 160 <Unit>kg/kmol</Unit> 161 <Index>2</Index> 162 <Values>42.0804</Values> 163 <Status>0</Status> 164 <Unit>kg/kmol</Unit> 165 <Index>3</Index> 149 166 <Values>78.1134</Values> 167 <Status>0</Status> 168 <Unit>kg/kmol</Unit> 169 <Index>4</Index> 170 <Values>56.1072</Values> 150 171 <Status>0</Status> 151 172 <Unit>kg/kmol</Unit> … … 207 228 <Block> 208 229 <Type>Distillation_kettle_condTeste</Type> 209 <Id_String>Distillation_kettle_cond Teste_1</Id_String>230 <Id_String>Distillation_kettle_cond</Id_String> 210 231 <Image_File_Name>D:\Apps\repositorio\branches\gui\eml\stage_separators\icon/DistillationKettleCond.png</Image_File_Name> 211 <X> 348</X>212 <Y>13 0</Y>232 <X>293</X> 233 <Y>131</Y> 213 234 <Z>0</Z> 214 235 <Width>270</Width> … … 237 258 <Model_Name>stream</Model_Name> 238 259 <T_Connection>1</T_Connection> 260 <Parameters> 261 <Desc>NComp</Desc> 262 <Index>0</Index> 263 <Values>5</Values> 264 <Status>0</Status> 265 </Parameters> 266 <Variables> 267 <Desc>F</Desc> 268 <Index>0</Index> 269 <Values>113.4</Values> 270 <Status>0</Status> 271 <Unit>kmol/h</Unit> 272 </Variables> 273 <Variables> 274 <Desc>T</Desc> 275 <Index>0</Index> 276 <Values>291</Values> 277 <Status>0</Status> 278 <Unit>K</Unit> 279 </Variables> 280 <Variables> 281 <Desc>P</Desc> 282 <Index>0</Index> 283 <Values>1.66099</Values> 284 <Status>0</Status> 285 <Unit>atm</Unit> 286 </Variables> 287 <Variables> 288 <Desc>h</Desc> 289 <Index>0</Index> 290 <Values>-15790.9</Values> 291 <Status>0</Status> 292 <Unit>kJ/kmol</Unit> 293 </Variables> 294 <Variables> 295 <Desc>v</Desc> 296 <Index>0</Index> 297 <Values>0.429005</Values> 298 <Status>0</Status> 299 </Variables> 300 <Variables> 301 <Desc>z</Desc> 302 <Index>0</Index> 303 <Values>0.2</Values> 304 <Status>0</Status> 305 <Index>1</Index> 306 <Values>0.2</Values> 307 <Status>0</Status> 308 <Index>2</Index> 309 <Values>0.2</Values> 310 <Status>0</Status> 311 <Index>3</Index> 312 <Values>0.2</Values> 313 <Status>0</Status> 314 <Index>4</Index> 315 <Values>0.2</Values> 316 <Status>0</Status> 317 </Variables> 239 318 </Block_Properties> 240 319 </Base_Models> … … 271 350 <Model_Name>stream</Model_Name> 272 351 <T_Connection>0</T_Connection> 352 <Parameters> 353 <Desc>NComp</Desc> 354 <Index>0</Index> 355 <Values>5</Values> 356 <Status>0</Status> 357 </Parameters> 358 <Variables> 359 <Desc>F</Desc> 360 <Index>0</Index> 361 <Values>0</Values> 362 <Status>0</Status> 363 <Unit>kmol/h</Unit> 364 </Variables> 365 <Variables> 366 <Desc>T</Desc> 367 <Index>0</Index> 368 <Values>291</Values> 369 <Status>0</Status> 370 <Unit>K</Unit> 371 </Variables> 372 <Variables> 373 <Desc>P</Desc> 374 <Index>0</Index> 375 <Values>1.66099</Values> 376 <Status>0</Status> 377 <Unit>atm</Unit> 378 </Variables> 379 <Variables> 380 <Desc>h</Desc> 381 <Index>0</Index> 382 <Values>-15790.9</Values> 383 <Status>0</Status> 384 <Unit>kJ/kmol</Unit> 385 </Variables> 386 <Variables> 387 <Desc>v</Desc> 388 <Index>0</Index> 389 <Values>0.429005</Values> 390 <Status>0</Status> 391 </Variables> 392 <Variables> 393 <Desc>z</Desc> 394 <Index>0</Index> 395 <Values>0.2</Values> 396 <Status>0</Status> 397 <Index>1</Index> 398 <Values>0.2</Values> 399 <Status>0</Status> 400 <Index>2</Index> 401 <Values>0.2</Values> 402 <Status>0</Status> 403 <Index>3</Index> 404 <Values>0.2</Values> 405 <Status>0</Status> 406 <Index>4</Index> 407 <Values>0.2</Values> 408 <Status>0</Status> 409 </Variables> 273 410 </Block_Properties> 274 411 </Base_Models> … … 287 424 <Model_Name>stream</Model_Name> 288 425 <T_Connection>1</T_Connection> 426 <Parameters> 427 <Desc>NComp</Desc> 428 <Index>0</Index> 429 <Values>5</Values> 430 <Status>0</Status> 431 </Parameters> 432 <Variables> 433 <Desc>F</Desc> 434 <Index>0</Index> 435 <Values>85</Values> 436 <Status>0</Status> 437 <Unit>kmol/h</Unit> 438 </Variables> 439 <Variables> 440 <Desc>T</Desc> 441 <Index>0</Index> 442 <Values>298.181</Values> 443 <Status>0</Status> 444 <Unit>K</Unit> 445 </Variables> 446 <Variables> 447 <Desc>P</Desc> 448 <Index>0</Index> 449 <Values>3.85346</Values> 450 <Status>0</Status> 451 <Unit>atm</Unit> 452 </Variables> 453 <Variables> 454 <Desc>h</Desc> 455 <Index>0</Index> 456 <Values>-20407.2</Values> 457 <Status>0</Status> 458 <Unit>kJ/kmol</Unit> 459 </Variables> 460 <Variables> 461 <Desc>v</Desc> 462 <Index>0</Index> 463 <Values>0</Values> 464 <Status>0</Status> 465 </Variables> 466 <Variables> 467 <Desc>z</Desc> 468 <Index>0</Index> 469 <Values>0.537546</Values> 470 <Status>0</Status> 471 <Index>1</Index> 472 <Values>0.051044</Values> 473 <Status>0</Status> 474 <Index>2</Index> 475 <Values>0.0796779</Values> 476 <Status>0</Status> 477 <Index>3</Index> 478 <Values>0.00455204</Values> 479 <Status>0</Status> 480 <Index>4</Index> 481 <Values>0.32718</Values> 482 <Status>0</Status> 483 </Variables> 289 484 </Block_Properties> 290 485 </Base_Models> … … 303 498 <Model_Name>stream</Model_Name> 304 499 <T_Connection>1</T_Connection> 500 <Parameters> 501 <Desc>NComp</Desc> 502 <Index>0</Index> 503 <Values>5</Values> 504 <Status>0</Status> 505 </Parameters> 506 <Variables> 507 <Desc>F</Desc> 508 <Index>0</Index> 509 <Values>199.919</Values> 510 <Status>0</Status> 511 <Unit>kmol/h</Unit> 512 </Variables> 513 <Variables> 514 <Desc>T</Desc> 515 <Index>0</Index> 516 <Values>303.096</Values> 517 <Status>0</Status> 518 <Unit>K</Unit> 519 </Variables> 520 <Variables> 521 <Desc>P</Desc> 522 <Index>0</Index> 523 <Values>3.73012</Values> 524 <Status>0</Status> 525 <Unit>atm</Unit> 526 </Variables> 527 <Variables> 528 <Desc>h</Desc> 529 <Index>0</Index> 530 <Values>-353.222</Values> 531 <Status>0</Status> 532 <Unit>kJ/kmol</Unit> 533 </Variables> 534 <Variables> 535 <Desc>v</Desc> 536 <Index>0</Index> 537 <Values>1</Values> 538 <Status>0</Status> 539 </Variables> 540 <Variables> 541 <Desc>z</Desc> 542 <Index>0</Index> 543 <Values>0.472221</Values> 544 <Status>0</Status> 545 <Index>1</Index> 546 <Values>0.0280774</Values> 547 <Status>0</Status> 548 <Index>2</Index> 549 <Values>0.135698</Values> 550 <Status>0</Status> 551 <Index>3</Index> 552 <Values>0.000602071</Values> 553 <Status>0</Status> 554 <Index>4</Index> 555 <Values>0.363402</Values> 556 <Status>0</Status> 557 </Variables> 305 558 </Block_Properties> 306 559 </Base_Models> … … 325 578 <Model_Name>stream</Model_Name> 326 579 <T_Connection>2</T_Connection> 580 <Parameters> 581 <Desc>NComp</Desc> 582 <Index>0</Index> 583 <Values>5</Values> 584 <Status>0</Status> 585 </Parameters> 586 <Variables> 587 <Desc>F</Desc> 588 <Index>0</Index> 589 <Values>83.7692</Values> 590 <Status>0</Status> 591 <Unit>kmol/h</Unit> 592 </Variables> 593 <Variables> 594 <Desc>T</Desc> 595 <Index>0</Index> 596 <Values>301.121</Values> 597 <Status>0</Status> 598 <Unit>K</Unit> 599 </Variables> 600 <Variables> 601 <Desc>P</Desc> 602 <Index>0</Index> 603 <Values>3.69943</Values> 604 <Status>0</Status> 605 <Unit>atm</Unit> 606 </Variables> 607 <Variables> 608 <Desc>h</Desc> 609 <Index>0</Index> 610 <Values>-20350.4</Values> 611 <Status>0</Status> 612 <Unit>kJ/kmol</Unit> 613 </Variables> 614 <Variables> 615 <Desc>v</Desc> 616 <Index>0</Index> 617 <Values>0</Values> 618 <Status>0</Status> 619 </Variables> 620 <Variables> 621 <Desc>z</Desc> 622 <Index>0</Index> 623 <Values>0.487751</Values> 624 <Status>0</Status> 625 <Index>1</Index> 626 <Values>0.0754466</Values> 627 <Status>0</Status> 628 <Index>2</Index> 629 <Values>0.0519748</Values> 630 <Status>0</Status> 631 <Index>3</Index> 632 <Values>0.00520137</Values> 633 <Status>0</Status> 634 <Index>4</Index> 635 <Values>0.379626</Values> 636 <Status>0</Status> 637 </Variables> 327 638 </Block_Properties> 328 639 </Base_Models> … … 355 666 <Model_Name>stream</Model_Name> 356 667 <T_Connection>2</T_Connection> 668 <Parameters> 669 <Desc>NComp</Desc> 670 <Index>0</Index> 671 <Values>5</Values> 672 <Status>0</Status> 673 </Parameters> 674 <Variables> 675 <Desc>F</Desc> 676 <Index>0</Index> 677 <Values>201.164</Values> 678 <Status>0</Status> 679 <Unit>kmol/h</Unit> 680 </Variables> 681 <Variables> 682 <Desc>T</Desc> 683 <Index>0</Index> 684 <Values>301.121</Values> 685 <Status>0</Status> 686 <Unit>K</Unit> 687 </Variables> 688 <Variables> 689 <Desc>P</Desc> 690 <Index>0</Index> 691 <Values>3.69943</Values> 692 <Status>0</Status> 693 <Unit>atm</Unit> 694 </Variables> 695 <Variables> 696 <Desc>h</Desc> 697 <Index>0</Index> 698 <Values>-527.825</Values> 699 <Status>0</Status> 700 <Unit>kJ/kmol</Unit> 701 </Variables> 702 <Variables> 703 <Desc>v</Desc> 704 <Index>0</Index> 705 <Values>1</Values> 706 <Status>0</Status> 707 </Variables> 708 <Variables> 709 <Desc>z</Desc> 710 <Index>0</Index> 711 <Values>0.493821</Values> 712 <Status>0</Status> 713 <Index>1</Index> 714 <Values>0.0177539</Values> 715 <Status>0</Status> 716 <Index>2</Index> 717 <Values>0.146696</Values> 718 <Status>0</Status> 719 <Index>3</Index> 720 <Values>0.000399049</Values> 721 <Status>0</Status> 722 <Index>4</Index> 723 <Values>0.34133</Values> 724 <Status>0</Status> 725 </Variables> 357 726 </Block_Properties> 358 727 </Base_Models> … … 373 742 <Status>0</Status> 374 743 </Parameters> 744 <Parameters> 745 <Desc>NComp</Desc> 746 <Index>0</Index> 747 <Values>5</Values> 748 <Status>0</Status> 749 </Parameters> 750 <Variables> 751 <Desc>M</Desc> 752 <Index>0</Index> 753 <Values>0.1025</Values> 754 <Status>0</Status> 755 <Unit>kmol</Unit> 756 <Index>1</Index> 757 <Values>0.0149425</Values> 758 <Status>0</Status> 759 <Unit>kmol</Unit> 760 <Index>2</Index> 761 <Values>0.0123865</Values> 762 <Status>0</Status> 763 <Unit>kmol</Unit> 764 <Index>3</Index> 765 <Values>0.00101732</Values> 766 <Status>0</Status> 767 <Unit>kmol</Unit> 768 <Index>4</Index> 769 <Values>0.0791085</Values> 770 <Status>0</Status> 771 <Unit>kmol</Unit> 772 </Variables> 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<Index>0</Index> 892 <Values>5</Values> 893 <Status>0</Status> 894 </Parameters> 895 <Variables> 896 <Desc>F</Desc> 897 <Index>0</Index> 898 <Values>0</Values> 899 <Status>0</Status> 900 <Unit>kmol/h</Unit> 901 </Variables> 902 <Variables> 903 <Desc>T</Desc> 904 <Index>0</Index> 905 <Values>291</Values> 906 <Status>0</Status> 907 <Unit>K</Unit> 908 </Variables> 909 <Variables> 910 <Desc>P</Desc> 911 <Index>0</Index> 912 <Values>1.66099</Values> 913 <Status>0</Status> 914 <Unit>atm</Unit> 915 </Variables> 916 <Variables> 917 <Desc>h</Desc> 918 <Index>0</Index> 919 <Values>-15790.9</Values> 920 <Status>0</Status> 921 <Unit>kJ/kmol</Unit> 922 </Variables> 923 <Variables> 924 <Desc>v</Desc> 925 <Index>0</Index> 926 <Values>0.429005</Values> 927 <Status>0</Status> 928 </Variables> 929 <Variables> 930 <Desc>z</Desc> 931 <Index>0</Index> 932 <Values>0.2</Values> 933 <Status>0</Status> 934 <Index>1</Index> 935 <Values>0.2</Values> 936 <Status>0</Status> 937 <Index>2</Index> 938 <Values>0.2</Values> 939 <Status>0</Status> 940 <Index>3</Index> 941 <Values>0.2</Values> 942 <Status>0</Status> 943 <Index>4</Index> 944 <Values>0.2</Values> 945 <Status>0</Status> 946 </Variables> 411 947 </Block_Properties> 412 948 </Base_Models> … … 425 961 <Model_Name>stream</Model_Name> 426 962 <T_Connection>1</T_Connection> 963 <Parameters> 964 <Desc>NComp</Desc> 965 <Index>0</Index> 966 <Values>5</Values> 967 <Status>0</Status> 968 </Parameters> 969 <Variables> 970 <Desc>F</Desc> 971 <Index>0</Index> 972 <Values>83.7692</Values> 973 <Status>0</Status> 974 <Unit>kmol/h</Unit> 975 </Variables> 976 <Variables> 977 <Desc>T</Desc> 978 <Index>0</Index> 979 <Values>301.121</Values> 980 <Status>0</Status> 981 <Unit>K</Unit> 982 </Variables> 983 <Variables> 984 <Desc>P</Desc> 985 <Index>0</Index> 986 <Values>3.69943</Values> 987 <Status>0</Status> 988 <Unit>atm</Unit> 989 </Variables> 990 <Variables> 991 <Desc>h</Desc> 992 <Index>0</Index> 993 <Values>-20350.4</Values> 994 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<Status>0</Status> 1048 <Unit>kmol/h</Unit> 1049 </Variables> 1050 <Variables> 1051 <Desc>T</Desc> 1052 <Index>0</Index> 1053 <Values>305.573</Values> 1054 <Status>0</Status> 1055 <Unit>K</Unit> 1056 </Variables> 1057 <Variables> 1058 <Desc>P</Desc> 1059 <Index>0</Index> 1060 <Values>3.76017</Values> 1061 <Status>0</Status> 1062 <Unit>atm</Unit> 1063 </Variables> 1064 <Variables> 1065 <Desc>h</Desc> 1066 <Index>0</Index> 1067 <Values>-127.572</Values> 1068 <Status>0</Status> 1069 <Unit>kJ/kmol</Unit> 1070 </Variables> 1071 <Variables> 1072 <Desc>v</Desc> 1073 <Index>0</Index> 1074 <Values>1</Values> 1075 <Status>0</Status> 1076 </Variables> 1077 <Variables> 1078 <Desc>z</Desc> 1079 <Index>0</Index> 1080 <Values>0.454216</Values> 1081 <Status>0</Status> 1082 <Index>1</Index> 1083 <Values>0.0441664</Values> 1084 <Status>0</Status> 1085 <Index>2</Index> 1086 <Values>0.134379</Values> 1087 <Status>0</Status> 1088 <Index>3</Index> 1089 <Values>0.00145199</Values> 1090 <Status>0</Status> 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