Changeset 672 for branches/gui/eml


Ignore:
Timestamp:
Oct 26, 2008, 5:57:21 PM (14 years ago)
Author:
gerson bicca
Message:

improved column model (testing)

Location:
branches/gui/eml
Files:
2 added
7 edited

Legend:

Unmodified
Added
Removed
  • branches/gui/eml/icon/SourceNoFlow.svg

    r641 r672  
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  • branches/gui/eml/stage_separators/column.mso

    r666 r672  
    6969        outer NComp                                                             as Integer                      (Brief="Number of components");
    7070        NumberOfTrays                                                           as Integer                      (Brief="Number of trays", Default=8);
    71         SpecialTrayIndex(NumberOfTrays)         as Integer                      (Brief="Number of trays", Default=0,Hidden=true);
     71        FeedTrayIndex(NumberOfTrays)    as Integer                      (Brief="Number of trays", Default=0,Hidden=true);
     72        LiqSideTrayIndex(NumberOfTrays)         as Integer                      (Brief="Number of trays", Default=0,Hidden=true);
     73        VapSideTrayIndex(NumberOfTrays)         as Integer                      (Brief="Number of trays", Default=0,Hidden=true);
    7274        FeedTrayLocation                                                        as Integer                      (Brief="Feed tray Location", Default=2);
     75        LiquidSideStreamLocation                                                        as Integer                      (Brief="Liquid Side Stream Location", Default=2);
     76        VapourSideStreamLocation                                                        as Integer                      (Brief="Vapour Side Stream Location", Default=2);
    7377        g                                                                                                       as acceleration         (Brief="Gravity Acceleration",Default=9.81,Hidden=true);
    7478        Mw(NComp)                                                                       as molweight    (Brief="Component Mol Weight",Hidden=true);
     
    114118
    115119SET
    116         SpecialTrayIndex(FeedTrayLocation) =1;
     120        FeedTrayIndex(FeedTrayLocation) =1;
     121        VapSideTrayIndex(FeedTrayLocation) =1;
     122        LiqSideTrayIndex(FeedTrayLocation) =1;
    117123        Mw = PP.MolecularWeight();
    118124
     
    134140        trays(NumberOfTrays) as tray                    (Brief="Number of trays");
    135141
     142                VapourDrawOffFlow  as flow_mol                  (Brief = "Stream Molar Flow Rate");
     143                LiquidDrawOffFlow   as flow_mol                         (Brief = "Stream Molar Flow Rate");
     144
    136145        MurphreeEff                             as Real         (Brief = "Murphree efficiency");
    137146
     
    144153EQUATIONS
    145154# Connecting Trays
    146         FeedTray.F*SpecialTrayIndex= trays.Inlet.F;
     155        FeedTray.F*FeedTrayIndex= trays.Inlet.F;
    147156        FeedTray.T = trays.Inlet.T;
    148157        FeedTray.P = trays.Inlet.P;
     
    276285VARIABLES
    277286
     287        out     VapourDrawOff   as vapour_stream                (Brief="Vapour Outlet in the section", PosX=1, PosY=0.35,Protected = true);
     288        out     LiquidDrawOff           as liquid_stream                        (Brief="Liquid Outlet in the section", PosX=1, PosY=0.65,Protected = true);
     289       
    278290        in              LiquidInlet             as      stream                          (Brief="Liquid Inlet in the section", PosX=0.80, PosY=0);
    279291        out     VapourOutlet            as vapour_stream        (Brief="Vapour Outlet in the section", PosX=0.30, PosY=0);
     
    315327        VapourOutlet.P = trays(1).OutletV.P;
    316328        VapourOutlet.z = trays(1).OutletV.z;
     329
     330        VapourDrawOff.F*VapSideTrayIndex= trays.VapourSideStream.F;
     331        VapourDrawOff.T = trays(VapourSideStreamLocation).VapourSideStream.T;
     332        VapourDrawOff.P = trays(VapourSideStreamLocation).VapourSideStream.P;
     333        VapourDrawOff.z = trays(VapourSideStreamLocation).VapourSideStream.z;
     334
     335        LiquidDrawOff.F*LiqSideTrayIndex= trays.LiquidSideStream.F;
     336        LiquidDrawOff.T = trays(LiquidSideStreamLocation).LiquidSideStream.T;
     337        LiquidDrawOff.P = trays(LiquidSideStreamLocation).LiquidSideStream.P;
     338        LiquidDrawOff.z = trays(LiquidSideStreamLocation).LiquidSideStream.z;
     339
     340        VapourDrawOffFlow = VapourDrawOff.F;
     341        LiquidDrawOffFlow = LiquidDrawOff.F;
    317342
    318343end
     
    359384
    360385VARIABLES
     386        out     VapourDrawOff   as vapour_stream                (Brief="Vapour Outlet in the section", PosX=0.25, PosY=0.45,Protected = true);
     387        out     LiquidDrawOff           as liquid_stream                        (Brief="Liquid Outlet in the section", PosX=0.25, PosY=0.65,Protected = true);
     388       
    361389        CondenserUnity  as condenser;
    362390        ReboilerUnity           as reboiler;
     
    370398RebNoFlow       as sourceNoFlow (Brief="No Inlet Flow to Reboiler",Hidden=true);
    371399
    372 out     VapourDistillate                                as vapour_stream        (Brief="Vapour outlet stream From Top Condenser", PosX=0.72, PosY=0);
     400out     VapourDistillate                                as vapour_stream        (Brief="Vapour outlet stream From Top Condenser", PosX=0.68, PosY=0);
    373401in              ConnectorCondenserVout  as stream       (Brief="Connector for Vapour outlet stream From Top Condenser", Hidden=true);
    374402
    375 out     LiquidDistillate                                as liquid_stream        (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.47);
     403out     LiquidDistillate                                as liquid_stream        (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.30);
    376404in              ConnectorSplitterOut    as stream       (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true);
    377405
     
    412440        ConnectorReboilerLout.z = BottomProduct.z;
    413441
     442VapourDrawOff.F*VapSideTrayIndex= trays.VapourSideStream.F;
     443        VapourDrawOff.T = trays(VapourSideStreamLocation).VapourSideStream.T;
     444        VapourDrawOff.P = trays(VapourSideStreamLocation).VapourSideStream.P;
     445        VapourDrawOff.z = trays(VapourSideStreamLocation).VapourSideStream.z;
     446
     447        LiquidDrawOff.F*LiqSideTrayIndex= trays.LiquidSideStream.F;
     448        LiquidDrawOff.T = trays(LiquidSideStreamLocation).LiquidSideStream.T;
     449        LiquidDrawOff.P = trays(LiquidSideStreamLocation).LiquidSideStream.P;
     450        LiquidDrawOff.z = trays(LiquidSideStreamLocation).LiquidSideStream.z;
     451
     452        VapourDrawOffFlow = VapourDrawOff.F;
     453        LiquidDrawOffFlow = LiquidDrawOff.F;
     454       
    414455CONNECTIONS
    415456#vapor
  • branches/gui/eml/stage_separators/icon/DistillationKettleCond.svg

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  • branches/gui/eml/stage_separators/tray.mso

    r648 r672  
    4444
    4545        Inlet                   as stream                               (Brief="Feed stream", PosX=0, PosY=0.4932, Symbol="_{in}");
     46        LiquidSideStream        as liquid_stream        (Brief="liquid Sidestream", Hidden=true, Symbol="_{outL}");
     47        VapourSideStream        as vapour_stream        (Brief="vapour Sidestream", Hidden=true, Symbol="_{outV}");
     48       
    4649in      InletL                  as stream                               (Brief="Inlet liquid stream", PosX=0.5195, PosY=0, Symbol="_{inL}");
    4750in      InletV                  as stream                               (Brief="Inlet vapour stream", PosX=0.4994, PosY=1, Symbol="_{inV}");
    4851out     OutletL         as liquid_stream        (Brief="Outlet liquid stream", PosX=0.8277, PosY=1, Symbol="_{outL}");
    4952out     OutletV         as vapour_stream        (Brief="Outlet vapour stream", PosX=0.8043, PosY=0, Symbol="_{outV}");
     53
    5054
    5155        M(NComp)                        as mol                          (Brief="Molar Holdup in the tray");
     
    6064       
    6165EQUATIONS
    62         "Component Molar Balance"
    63         diff(M)=Inlet.F*Inlet.z + InletL.F*InletL.z + InletV.F*InletV.z- OutletL.F*OutletL.z - OutletV.F*OutletV.z;
     66"Component Molar Balance"
     67        diff(M)=Inlet.F*Inlet.z + InletL.F*InletL.z + InletV.F*InletV.z- OutletL.F*OutletL.z - OutletV.F*OutletV.z-
     68        LiquidSideStream.F*LiquidSideStream.z-VapourSideStream.F*VapourSideStream.z;
    6469
    6570"Molar Holdup"
     
    8489"Mechanical Equilibrium"
    8590        OutletV.P = OutletL.P;
     91       
     92"Thermal Equilibrium Vapour Side Stream"
     93        OutletV.T = VapourSideStream.T;
     94
     95"Thermal Equilibrium Liquid Side Stream"
     96        OutletL.T = LiquidSideStream.T;
     97
     98"Mechanical Equilibrium Vapour Side Stream"
     99        OutletV.P= VapourSideStream.P;
     100
     101"Mechanical Equilibrium Liquid Side Stream"
     102        OutletL.P = LiquidSideStream.P;
     103
     104"Composition Liquid Side Stream"
     105        OutletL.z= LiquidSideStream.z;
     106       
     107"Composition Vapour Side Stream"
     108        OutletV.z= VapourSideStream.z;
    86109
    87110end
  • branches/gui/eml/streams.mso

    r641 r672  
    673673
    674674end
     675
     676Model sinkNoFlow
     677        ATTRIBUTES
     678        Pallete = true;
     679        Icon = "icon/sinkNoFlow";
     680        Brief = "Simple material stream sink";
     681        Info = "
     682        This model should be used for seal an outlet material stream port.
     683        ";
     684       
     685        VARIABLES
     686        in Inlet                as stream       (Brief = "Inlet Stream", PosX=0, PosY=0.5308, Protected=true,Symbol="_{in}");
     687
     688EQUATIONS
     689"Stream Molar Flow"
     690        Inlet.F = 0 * 'kmol/h';
     691       
     692end
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