Changeset 930 for branches/gui
 Timestamp:
 Apr 23, 2011, 8:08:41 PM (11 years ago)
 File:

 1 edited
Legend:
 Unmodified
 Added
 Removed

branches/gui/eml/stage_separators/condenser.mso
r929 r930 427 427 428 428 429 Model condenser2 430 431 ATTRIBUTES 432 Pallete = true; 433 Icon = "icon/Condenser"; 434 Brief = "Model of a dynamic condenser with control."; 435 Info = 436 "== ASSUMPTIONS == 437 * perfect mixing of both phases; 438 * thermodynamics equilibrium. 439 440 == SPECIFY == 441 * the InletVapour stream; 442 * the outlet flows: Product.F and Reflux.F; 443 * the InletQ (the model requires an energy stream, also you can use a controller for setting the heat duty using the heat_flow model). 444 445 == OPTIONAL == 446 * the condenser model has three control ports 447 ** TI OutletLiquid Temperature Indicator; 448 ** PI OutletLiquid Pressure Indicator; 449 ** LI Level Indicator of Condenser; 450 451 == INITIAL CONDITIONS == 452 * Initial_Temperature : the condenser temperature (OutletLiquid.T); 453 * Levelpercent_Initial : the condenser liquid level in percent (LI); 454 * Initial_Composition : (NoComps) OutletLiquid compositions. 455 "; 456 457 PARAMETERS 458 outer PP as Plugin (Brief = "External Physical Properties", Type="PP"); 459 outer NComp as Integer (Brief="Number of Components"); 460 461 Mw(NComp) as molweight (Brief = "Component Mol Weight",Hidden=true); 462 low_flow as flow_mol (Brief = "Low Flow",Default = 1E6, Hidden=true); 463 zero_flow as flow_mol (Brief = "No Flow",Default = 0, Hidden=true); 464 465 CondenserType as Switcher (Brief="Condenser type", Valid = ["partial", "total"], Default = "partial"); 466 VapourFlow as Switcher (Brief="Vapour Flow", Valid = ["on", "off"], Default = "on",Hidden=true); 467 468 Kfactor as positive (Brief="K factor for pressure drop", Lower = 1E8, Default = 1E3); 469 470 Levelpercent_Initial as positive (Brief="Initial liquid height in Percent", Default = 0.70); 471 Initial_Temperature as temperature (Brief="Initial Temperature of Condenser"); 472 Initial_Composition(NComp) as positive (Brief="Initial Liquid Composition", Lower=1E6); 473 474 VARIABLES 475 476 Geometry as VesselVolume (Brief="Vessel Geometry", Symbol=" "); 477 478 in InletVapour as stream (Brief="Vapour inlet stream", PosX=0.13, PosY=0, Symbol="_{in}^{Vapour}"); 479 out OutletLiquid as liquid_stream (Brief="Liquid outlet stream", PosX=0.35, PosY=1, Symbol="_{out}^{Liquid}"); 480 Vapour as vapour_stream (Brief="Vapour outlet stream", Hidden=true, Symbol="_{out}^{Vapour}"); 481 out Product as stream (Brief="Vapour or Liquid product stream", PosX=0.54, PosY=0, Symbol="_{out}^{Vapour}"); 482 in InletQ as power (Brief="Heat supplied", Protected = true, PosX=1, PosY=0.08, Symbol="Q_{in}"); 483 484 RefluxRatio as positive (Brief = "Reflux Ratio", Default=10, Lower = 0.05); 485 486 out TI as control_signal (Brief="Temperature Indicator of Condenser", Protected = true, PosX=0.33, PosY=0); 487 out LI as control_signal (Brief="Level Indicator of Condenser", Protected = true, PosX=0.43, PosY=0); 488 out PI as control_signal (Brief="Pressure Indicator of Condenser", Protected = true, PosX=0.25, PosY=0); 489 490 M(NComp) as mol (Brief="Molar Holdup in the tray", Protected = true); 491 ML as mol (Brief="Molar liquid holdup", Protected = true); 492 MV as mol (Brief="Molar vapour holdup", Protected = true); 493 E as energy (Brief="Total Energy Holdup on tray", Protected = true); 494 vL as volume_mol (Brief="Liquid Molar Volume", Protected = true); 495 vV as volume_mol (Brief="Vapour Molar volume", Protected = true); 496 rho as dens_mass (Brief ="Inlet Vapour Mass Density",Hidden=true, Symbol ="\rho"); 497 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P", Protected=true); 498 499 SET 500 Mw = PP.MolecularWeight(); 501 low_flow = 1E6 * 'kmol/h'; 502 zero_flow = 0 * 'kmol/h'; 503 504 INITIAL 505 506 "Initial level Percent" 507 LI = Levelpercent_Initial; 508 509 "Initial Temperature" 510 OutletLiquid.T = Initial_Temperature; 511 512 "Initial Composition" 513 OutletLiquid.z(1:NComp1) = Initial_Composition(1:NComp1)/sum(Initial_Composition); 514 515 EQUATIONS 516 517 518 Vapour.F = zero_flow; 519 "Reflux ratio" 520 RefluxRatio*Product.F = OutletLiquid.F; 521 522 switch CondenserType 523 524 case "partial": 525 Product.v = Vapour.v; 526 Product.h = Vapour.h; 527 Product.z = Vapour.z; 528 529 case "total": 530 Product.v = OutletLiquid.v; 531 Product.h = OutletLiquid.h; 532 Product.z = OutletLiquid.z; 533 end 534 535 536 switch VapourFlow 537 538 case "on": 539 InletVapour.F*vV = Kfactor *sqrt(Pdrop/rho)*'m^2'; 540 541 when InletVapour.F < low_flow switchto "off"; 542 543 case "off": 544 InletVapour.F = zero_flow; 545 546 when InletVapour.P > OutletLiquid.P switchto "on"; 547 548 end 549 550 "Component Molar Balance" 551 diff(M) = InletVapour.F*InletVapour.z  OutletLiquid.F*OutletLiquid.z Product.F*Product.z; 552 553 "Energy Balance" 554 diff(E) = InletVapour.F*InletVapour.h  OutletLiquid.F*OutletLiquid.h Product.F*Product.h + InletQ; 555 556 "Molar Holdup" 557 M = ML*OutletLiquid.z + MV*Vapour.z; 558 559 "Energy Holdup" 560 E = ML*OutletLiquid.h + MV*Vapour.h  Vapour.P*Geometry.Vtotal; 561 562 "Mol fraction normalisation" 563 sum(OutletLiquid.z)=1.0; 564 565 "Mol fraction Constraint" 566 sum(OutletLiquid.z)=sum(Vapour.z); 567 568 "Liquid Volume" 569 vL = PP.LiquidVolume(OutletLiquid.T, OutletLiquid.P, OutletLiquid.z); 570 571 "Vapour Volume" 572 vV = PP.VapourVolume(Vapour.T, Vapour.P, Vapour.z); 573 574 "Inlet Vapour Density" 575 rho = PP.VapourDensity(InletVapour.T, InletVapour.P, InletVapour.z); 576 577 "Chemical Equilibrium" 578 PP.LiquidFugacityCoefficient(OutletLiquid.T, OutletLiquid.P, OutletLiquid.z)*OutletLiquid.z = 579 PP.VapourFugacityCoefficient(Vapour.T, Vapour.P, Vapour.z)*Vapour.z; 580 581 "Thermal Equilibrium" 582 OutletLiquid.T = Vapour.T; 583 OutletLiquid.T = Product.T; 584 585 "Mechanical Equilibrium" 586 Vapour.P = OutletLiquid.P; 587 Vapour.P = Product.P; 588 589 "Pressure Drop" 590 OutletLiquid.P = InletVapour.P  Pdrop; 591 592 "Geometry Constraint" 593 Geometry.Vtotal = ML*vL + MV*vV; 594 595 "Liquid Level" 596 ML * vL = Geometry.Vfilled; 597 598 "Temperature indicator" 599 TI * 'K' = OutletLiquid.T; 600 601 "Pressure indicator" 602 PI * 'atm' = OutletLiquid.P; 603 604 "Level indicator" 605 LI*Geometry.Vtotal= Geometry.Vfilled; 606 607 end 608 609 429 610 Model condenserSubcooled 430 611
Note: See TracChangeset
for help on using the changeset viewer.