Changeset 387 for trunk/eml


Ignore:
Timestamp:
Oct 11, 2007, 5:45:24 PM (15 years ago)
Author:
gerson bicca
Message:

added PHE diagram and updated Heat Exchangers models, icon

Location:
trunk/eml/heat_exchangers
Files:
4 edited

Legend:

Unmodified
Added
Removed
  • trunk/eml/heat_exchangers/HEX_Engine.mso

    r386 r387  
    410410Gchannel        as flux_mass                            (Brief ="Channel Mass Flux", Default=1, Lower=1e-6, Symbol ="G^{channel}");
    411411Gports          as flux_mass                            (Brief ="Ports Mass Flux", Default=1, Lower=1e-6, Symbol ="G^{ports}");
    412 Phi                     as positive                                     (Brief="Viscosity Correction",Default=1,Lower=1e-3, Symbol="\phi");
     412Phi                     as positive                                     (Brief="Viscosity Correction",Default=1,Lower=1e-6, Symbol="\phi");
    413413
    414414end
  • trunk/eml/heat_exchangers/PHE.mso

    r386 r387  
    7171outer NComp             as Integer      (Brief="Number of Chemical Components");
    7272        Pi                              as constant     (Brief="Pi Number",Default=3.14159265, Symbol = "\pi");
    73         N1                      as Integer      (Brief="Auxiliar Constant");
    74         N2                      as Integer      (Brief="Auxiliar Constant");
     73        N1                      as Integer      (Brief="Auxiliar Constant",Default = 15);
     74        N2                      as Integer      (Brief="Auxiliar Constant",Default = 14);
    7575        Kp1(N1)                 as constant     (Brief="First constant in Kumar calculation for Pressure Drop");
    7676        Kp2(N1)                 as constant     (Brief="Second constant in Kumar calculation for Pressure Drop");
     
    7979        M(NComp)                as molweight    (Brief="Component Mol Weight");
    8080       
    81         ChevronAngle    as Switcher             (Brief="Chevron Corrugation Inclination Angle in Degrees ",Valid=["30 Deg","45 Deg","50 Deg","60 Deg","65 Deg"],Default="30 Deg");
     81        ChevronAngle    as Switcher             (Brief="Chevron Corrugation Inclination Angle in Degrees ",Valid=["A30_Deg","A45_Deg","A50_Deg","A60_Deg","A65_Deg"],Default="A30_Deg");
    8282        SideOne                 as Switcher             (Brief="Fluid Alocation in the Side I - (The odd channels)",Valid=["hot","cold"],Default="hot");
    8383        Nchannels               as Integer              (Brief="Total Number of Channels in The Whole Heat Exchanger");
     
    105105 VARIABLES
    106106
    107 in  InletHot        as stream           (Brief="Inlet Hot Stream", PosX=0, PosY=0.7156, Symbol="^{inHot}");     
    108 in  InletCold       as stream           (Brief="Inlet Cold Stream", PosX=1, PosY=0.7156, Symbol="^{inCold}");
    109 out OutletHot           as streamPH     (Brief="Outlet Hot Stream", PosX=0, PosY=0.2793, Symbol="^{outHot}");
    110 out OutletCold          as streamPH     (Brief="Outlet Cold Stream", PosX=1, PosY=0.2793, Symbol="^{outCold}");
     107in  InletHot        as stream           (Brief="Inlet Hot Stream", PosX=0, PosY=0.75, Symbol="^{inHot}");       
     108in  InletCold       as stream           (Brief="Inlet Cold Stream", PosX=0, PosY=0.25, Symbol="^{inCold}");
     109out OutletHot           as streamPH     (Brief="Outlet Hot Stream", PosX=1, PosY=0.25, Symbol="^{outHot}");
     110out OutletCold          as streamPH     (Brief="Outlet Cold Stream", PosX=1, PosY=0.75, Symbol="^{outCold}");
    111111
    112112        HotSide                 as Main_PHE             (Brief="Plate Heat Exchanger Hot Side", Symbol="_{hot}");
     
    447447 switch ChevronAngle #Pressure Drop Friction Factor According to kumar's (1984)
    448448       
    449         case "30 Deg": #        ChevronAngle <= 30
     449        case "A30_Deg": #       ChevronAngle <= 30
    450450       
    451451        if      HotSide.HeatTransfer.Re < 10
     
    465465        end     
    466466
    467         case "45 Deg":
     467        case "A45_Deg":
    468468       
    469469        if      HotSide.HeatTransfer.Re < 15
     
    483483        end     
    484484
    485         case "50 Deg":
     485        case "A50_Deg":
    486486       
    487487        if      HotSide.HeatTransfer.Re < 20
     
    501501        end
    502502       
    503         case "60 Deg":
     503        case "A60_Deg":
    504504       
    505505        if      HotSide.HeatTransfer.Re < 40
     
    519519        end
    520520       
    521         case "65 Deg": #        ChevronAngle >= 65
     521        case "A65_Deg": #       ChevronAngle >= 65
    522522       
    523523        if      HotSide.HeatTransfer.Re < 50
     
    541541 switch ChevronAngle # Heat Transfer Coefficient According to kumar's (1984)
    542542
    543         case "30 Deg": #        ChevronAngle <= 30
     543        case "A30_Deg": #       ChevronAngle <= 30
    544544       
    545545        if      HotSide.HeatTransfer.Re < 10
     
    552552        end     
    553553       
    554         case "45 Deg":
     554        case "A45_Deg":
    555555       
    556556        if      HotSide.HeatTransfer.Re < 10
     
    569569        end
    570570
    571         case "50 Deg":
     571        case "A50_Deg":
    572572       
    573573        if      HotSide.HeatTransfer.Re < 20
     
    586586        end
    587587
    588         case "60 Deg":
     588        case "A60_Deg":
    589589       
    590590        if      HotSide.HeatTransfer.Re < 20
     
    603603        end
    604604       
    605         case "65 Deg": #        ChevronAngle >= 65
     605        case "A65_Deg": #       ChevronAngle >= 65
    606606       
    607607        if      HotSide.HeatTransfer.Re < 20
     
    691691        ColdSide.HeatTransfer.NTU*ColdSide.HeatTransfer.WCp = Thermal.Ud*Atotal;
    692692
    693 if Thermal.Cr equal 1 # To be Fixed: Effectiveness in true counter flow !
     693if  Thermal.Eft >= 1  #To be Fixed: Effectiveness in true counter flow !
    694694       
    695695        then
    696696"Effectiveness in Counter Flow"
    697         Thermal.Eft*(1+Thermal.NTU) = Thermal.NTU;
    698        
     697        Thermal.Eft = 1;
    699698        else
    700699"Effectiveness in Counter Flow"
    701         Thermal.NTU = (1/(Thermal.Cr-1))*ln(abs((Thermal.Eft-1)/(Thermal.Cr*Thermal.Eft-1)));
     700        Thermal.NTU*(Thermal.Cr-1.00001) = ln(abs((Thermal.Eft-1.00001))) - ln(abs((Thermal.Cr*Thermal.Eft-1.00001)));
    702701
    703702end
  • trunk/eml/heat_exchangers/icon/phe.svg

    r282 r387  
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