Changeset 654 for branches/gui
- Timestamp:
- Oct 1, 2008, 5:51:36 PM (14 years ago)
- Location:
- branches/gui
- Files:
-
- 2 added
- 6 edited
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/stage_separators/column.mso
r649 r654 357 357 PARAMETERS 358 358 CondenserVapourFlow as Switcher (Valid = ["on", "off"], Default = "on",Hidden=true); 359 359 360 360 VARIABLES 361 361 CondenserUnity as condenser; … … 499 499 out HeatToTopVessel as power (Brief="Heat supplied to Top Vessel",Hidden=true); 500 500 501 out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.47); 502 in ConnectorSplitterTop as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true); 503 504 out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Bottom Splitter", PosX=1, PosY=1); 505 in ConnectorSplitterBottom as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true); 506 501 507 EQUATIONS 508 509 # Top Splitter Connector Equations 510 ConnectorSplitterTop.T = LiquidDistillate.T; 511 ConnectorSplitterTop.P = LiquidDistillate.P; 512 ConnectorSplitterTop.F = LiquidDistillate.F; 513 ConnectorSplitterTop.z = LiquidDistillate.z; 514 515 # Bottom Splitter Connector Equations 516 ConnectorSplitterBottom.T = BottomProduct.T; 517 ConnectorSplitterBottom.P = BottomProduct.P; 518 ConnectorSplitterBottom.F = BottomProduct.F; 519 ConnectorSplitterBottom.z = BottomProduct.z; 502 520 503 521 switch CondenserVapourFlow … … 533 551 HeatToBottomVessel to BottomVessel.InletQ; 534 552 HeatToTopVessel to TopVessel.InletQ; 553 TopSplitter.Outlet1 to ConnectorSplitterTop; 554 BottomSplitter.Outlet1 to ConnectorSplitterBottom; 535 555 536 556 end … … 548 568 * - a pump in reflux stream. 549 569 * 550 * ------------------------------------------------------------------* 551 Model Distillation_thermosyphon_cond Teste570 * ------------------------------------------------------------------*# 571 Model Distillation_thermosyphon_cond as Section_ColumnBasic 552 572 ATTRIBUTES 553 573 Pallete = true; … … 578 598 "; 579 599 580 PARAMETERS 581 outer PP as Plugin(Brief = "External Physical Properties", Type="PP"); 582 outer NComp as Integer; 583 NumberOfTrays as Integer(Brief="Number of trays", Default=2); 584 topdown as Integer(Brief="Trays counting (1=top-down, -1=bottom-up)", Default=1); 585 top as Integer(Brief="Number of top tray"); 586 bot as Integer(Brief="Number of bottom tray"); 587 VapourFlow as Switcher(Valid = ["on", "off"], Default = "on"); 588 589 SET 590 top = (NumberOfTrays-1)*(1-topdown)/2+1; 591 bot = NumberOfTrays/top; 592 593 VARIABLES 594 trays(NumberOfTrays) as trayTeste; 595 cond as condenser; 596 reb as reboilerSteady; 597 tbottom as tank; 598 spbottom as splitter; 599 sptop as splitter; 600 pump1 as pump; 601 alfaTopo as Real; 602 603 EQUATIONS 604 switch VapourFlow 600 PARAMETERS 601 CondenserVapourFlow as Switcher (Valid = ["on", "off"], Default = "on",Hidden=true); 602 603 VARIABLES 604 605 CondenserUnity as condenser; 606 SplitterTop as splitter; 607 PumpUnity as pump; 608 BottomVessel as tank; 609 SplitterBottom as splitter; 610 ReboilerUnity as reboilerSteady; 611 alfaTopo as Real; 612 613 out HeatToCondenser as power (Brief="Heat supplied to Condenser",Hidden=true); 614 out HeatToReboiler as power (Brief="Heat supplied to Reboiler",Hidden=true); 615 out HeatToBottomVessel as power (Brief="Heat supplied to Bottom Vessel",Hidden=true); 616 617 out VapourDistillate as vapour_stream (Brief="Vapour outlet stream From Top Condenser", PosX=0.73, PosY=0); 618 in ConnectorCondenserVout as stream (Brief="Connector for Vapour outlet stream From Top Condenser", Hidden=true); 619 620 out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.45); 621 in ConnectorSplitterTop as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true); 622 623 out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Bottom Splitter", PosX=1, PosY=1); 624 in ConnectorSplitterBottom as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true); 625 626 EQUATIONS 627 628 # Condenser Connector Equations 629 ConnectorCondenserVout.T = VapourDistillate.T; 630 ConnectorCondenserVout.P = VapourDistillate.P; 631 ConnectorCondenserVout.F = VapourDistillate.F; 632 ConnectorCondenserVout.z = VapourDistillate.z; 633 634 # Top Splitter Connector Equations 635 ConnectorSplitterTop.T = LiquidDistillate.T; 636 ConnectorSplitterTop.P = LiquidDistillate.P; 637 ConnectorSplitterTop.F = LiquidDistillate.F; 638 ConnectorSplitterTop.z = LiquidDistillate.z; 639 640 # Bottom Splitter Connector Equations 641 ConnectorSplitterBottom.T = BottomProduct.T; 642 ConnectorSplitterBottom.P = BottomProduct.P; 643 ConnectorSplitterBottom.F = BottomProduct.F; 644 ConnectorSplitterBottom.z = BottomProduct.z; 645 646 switch CondenserVapourFlow 605 647 case "on": 606 cond.InletV.F*trays(top).vV = alfaTopo * trays(top).Ah * sqrt(2*(trays(top).OutletV.P -607 cond.OutletL.P + 1e-8 * 'atm') / (trays(top).alfa*trays(top).rhoV));608 when cond.InletV.F < 1e-6 * 'kmol/h' switchto "off";648 CondenserUnity.InletV.F*trays(1).vV = alfaTopo * Ah * sqrt(2*(trays(1).OutletV.P - 649 CondenserUnity.OutletL.P + 1e-8 * 'atm') / (alfa*trays(1).rhoV)); 650 when CondenserUnity.InletV.F < 1e-6 * 'kmol/h' switchto "off"; 609 651 610 652 case "off": 611 cond.InletV.F = 0 * 'mol/s'; 612 when trays(top).OutletV.P > cond.OutletL.P + 1e-1 * 'atm' switchto "on"; 613 end 614 615 CONNECTIONS 616 #vapor 617 reb.OutletV to trays(bot).InletV; 618 trays([top+topdown:topdown:bot]).OutletV to trays([top:topdown:bot-topdown]).InletV; 619 trays(top).OutletV to cond.InletV; 620 621 #liquid 622 cond.OutletL to sptop.Inlet; 623 sptop.Outlet2 to pump1.Inlet; 624 pump1.Outlet to trays(top).InletL; 625 trays([top:topdown:bot-topdown]).OutletL to trays([top+topdown:topdown:bot]).InletL; 626 trays(bot).OutletL to tbottom.Inlet; 627 tbottom.Outlet to spbottom.Inlet; 628 spbottom.Outlet2 to reb.InletL; 653 CondenserUnity.InletV.F = 0 * 'mol/s'; 654 when trays(1).OutletV.P > CondenserUnity.OutletL.P + 1e-1 * 'atm' switchto "on"; 655 end 656 657 CONNECTIONS 658 #vapor 659 ReboilerUnity.OutletV to trays(NumberOfTrays).InletV; 660 trays(1).OutletV to CondenserUnity.InletV; 661 662 #liquid 663 CondenserUnity.OutletL to SplitterTop.Inlet; 664 SplitterTop.Outlet2 to PumpUnity.Inlet; 665 PumpUnity.Outlet to trays(1).InletL; 666 trays(NumberOfTrays).OutletL to BottomVessel.Inlet; 667 BottomVessel.Outlet to SplitterBottom.Inlet; 668 SplitterBottom.Outlet2 to ReboilerUnity.InletL; 669 670 #Connectors 671 HeatToCondenser to CondenserUnity.InletQ; 672 HeatToReboiler to ReboilerUnity.InletQ; 673 HeatToBottomVessel to BottomVessel.InletQ; 674 CondenserUnity.OutletV to ConnectorCondenserVout; 675 SplitterTop.Outlet1 to ConnectorSplitterTop; 676 SplitterBottom.Outlet1 to ConnectorSplitterBottom; 677 629 678 end 630 679 … … 639 688 * - a pump in reflux stream. 640 689 * 641 * ------------------------------------------------------------------* 642 Model Distillation_kettle_subcoolingTeste 643 ATTRIBUTES 690 * ------------------------------------------------------------------*# 691 Model Distillation_kettle_subcooling as Section_ColumnBasic 692 693 ATTRIBUTES 644 694 Pallete = true; 645 695 Icon = "icon/DistillationKettleSubcooling"; 646 Brief 696 Brief = "Model of a distillation column with steady condenser and dynamic reboiler."; 647 697 Info = 648 698 "== Specify == … … 670 720 "; 671 721 672 PARAMETERS 673 outer PP as Plugin(Brief = "External Physical Properties", Type="PP"); 674 outer NComp as Integer; 675 NumberOfTrays as Integer(Brief="Number of trays", Default=2); 676 topdown as Integer(Brief="Trays counting (1=top-down, -1=bottom-up)", Default=1); 677 top as Integer(Brief="Number of top tray"); 678 bot as Integer(Brief="Number of bottom tray"); 679 VapourFlow as Switcher(Valid = ["on", "off"], Default = "on"); 680 681 SET 682 top = (NumberOfTrays-1)*(1-topdown)/2+1; 683 bot = NumberOfTrays/top; 684 685 VARIABLES 686 trays(NumberOfTrays) as trayTeste; 687 cond as condenserSteady; 688 reb as reboiler; 689 ttop as tank_cylindrical; 690 sptop as splitter; 691 pump1 as pump; 722 PARAMETERS 723 VapourFlow as Switcher(Valid = ["on", "off"], Default = "on",Hidden=true); 724 725 VARIABLES 726 CondenserUnity as condenserSteady; 727 TopVessel as tank_cylindrical; 728 SplitterTop as splitter; 729 PumpUnity as pump; 730 ReboilerUnity as reboiler; 692 731 alfaTopo as Real; 693 732 694 EQUATIONS 733 out HeatToCondenser as power (Brief="Heat supplied to Condenser",Hidden=true); 734 out HeatToReboiler as power (Brief="Heat supplied to Reboiler",Hidden=true); 735 out HeatToTopVessel as power (Brief="Heat supplied to Top Vessel",Hidden=true); 736 737 out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.47); 738 in ConnectorSplitterOut as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true); 739 740 out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Reboiler", PosX=1, PosY=1); 741 in ConnectorReboilerLout as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true); 742 743 RebNoFlow as sourceNoFlow (Brief="No Inlet Flow to Reboiler",Hidden=true); 744 745 EQUATIONS 746 747 # Splitter Connector Equations 748 ConnectorSplitterOut.T = LiquidDistillate.T; 749 ConnectorSplitterOut.P = LiquidDistillate.P; 750 ConnectorSplitterOut.F = LiquidDistillate.F; 751 ConnectorSplitterOut.z = LiquidDistillate.z; 752 753 # Reboiler Connector Equations 754 ConnectorReboilerLout.T = BottomProduct.T; 755 ConnectorReboilerLout.P = BottomProduct.P; 756 ConnectorReboilerLout.F = BottomProduct.F; 757 ConnectorReboilerLout.z = BottomProduct.z; 758 695 759 switch VapourFlow 696 760 case "on": 697 cond.InletV.F*trays(top).vV = alfaTopo * trays(top).Ah * sqrt(2*(trays(top).OutletV.P -698 cond.OutletL.P + 1e-8 * 'atm') / (trays(top).alfa*trays(top).rhoV));699 when cond.InletV.F < 1e-6 * 'kmol/h' switchto "off";761 CondenserUnity.InletV.F*trays(1).vV = alfaTopo * Ah * sqrt(2*(trays(1).OutletV.P - 762 CondenserUnity.OutletL.P + 1e-8 * 'atm') / (alfa*trays(1).rhoV)); 763 when CondenserUnity.InletV.F < 1e-6 * 'kmol/h' switchto "off"; 700 764 701 765 case "off": 702 cond.InletV.F = 0 * 'mol/s'; 703 when trays(top).OutletV.P > cond.OutletL.P + 1e-1 * 'atm' switchto "on"; 704 end 705 706 CONNECTIONS 707 #vapor 708 reb.OutletV to trays(bot).InletV; 709 trays([top+topdown:topdown:bot]).OutletV to trays([top:topdown:bot-topdown]).InletV; 710 trays(top).OutletV to cond.InletV; 711 712 #liquid 713 cond.OutletL to ttop.Inlet; 714 ttop.Outlet to sptop.Inlet; 715 sptop.Outlet2 to pump1.Inlet; 716 pump1.Outlet to trays(top).InletL; 717 trays([top:topdown:bot-topdown]).OutletL to trays([top+topdown:topdown:bot]).InletL; 718 trays(bot).OutletL to reb.InletL; 766 CondenserUnity.InletV.F = 0 * 'mol/s'; 767 when trays(1).OutletV.P > CondenserUnity.OutletL.P + 1e-1 * 'atm' switchto "on"; 768 end 769 770 CONNECTIONS 771 #vapor 772 ReboilerUnity.OutletV to trays(NumberOfTrays).InletV; 773 trays(1).OutletV to CondenserUnity.InletV; 774 775 #liquid 776 CondenserUnity.OutletL to TopVessel.Inlet; 777 TopVessel.Outlet to SplitterTop.Inlet; 778 SplitterTop.Outlet2 to PumpUnity.Inlet; 779 PumpUnity.Outlet to trays(1).InletL; 780 trays(NumberOfTrays).OutletL to ReboilerUnity.InletL; 781 782 #Connectors 783 HeatToCondenser to CondenserUnity.InletQ; 784 HeatToReboiler to ReboilerUnity.InletQ; 785 HeatToTopVessel to TopVessel.InletQ; 786 RebNoFlow.Outlet to ReboilerUnity.Inlet; 787 788 SplitterTop.Outlet1 to ConnectorSplitterOut; 789 ReboilerUnity.OutletL to ConnectorReboilerLout; 790 719 791 end 720 792 -
branches/gui/eml/stage_separators/icon/DistillationThermosyphonSubcooling.svg
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branches/gui/sample/stage_separators/Column_Distillation_Kettle_Diagram.pfd
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branches/gui/sample/stage_separators/Column_teste_Diagram.pfd
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1127 1816 <Status>0</Status> 1128 1817 </Parameters> 1818 <Parameters> 1819 <Desc>NComp</Desc> 1820 <Index>0</Index> 1821 <Values>5</Values> 1822 <Status>0</Status> 1823 </Parameters> 1824 <Variables> 1825 <Desc>M</Desc> 1826 <Index>0</Index> 1827 <Values>0.0938137</Values> 1828 <Status>0</Status> 1829 <Unit>kmol</Unit> 1830 <Index>1</Index> 1831 <Values>0.00876344</Values> 1832 <Status>0</Status> 1833 <Unit>kmol</Unit> 1834 <Index>2</Index> 1835 <Values>0.00216424</Values> 1836 <Status>0</Status> 1837 <Unit>kmol</Unit> 1838 <Index>3</Index> 1839 <Values>0.00172747</Values> 1840 <Status>0</Status> 1841 <Unit>kmol</Unit> 1842 <Index>4</Index> 1843 <Values>0.0799025</Values> 1844 <Status>0</Status> 1845 <Unit>kmol</Unit> 1846 </Variables> 1847 <Variables> 1848 <Desc>ML</Desc> 1849 <Index>0</Index> 1850 <Values>0.171533</Values> 1851 <Status>0</Status> 1852 <Unit>kmol</Unit> 1853 </Variables> 1854 <Variables> 1855 <Desc>MV</Desc> 1856 <Index>0</Index> 1857 <Values>0.014838</Values> 1858 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