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Timestamp:
Feb 15, 2008, 1:00:49 PM (15 years ago)
Author:
Paula Bettio Staudt
Message:

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1 edited

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

    r458 r461  
    364364        rhoL as dens_mass;
    365365        rhoV as dens_mass;
    366         uL as velocity (Brief="volume flow rate of liquid, m^3/m^2/s", Default = 0.007);
    367         uV as velocity (Brief="volume flow rate of vapor, m^3/m^2/s", Default = 1.14);
     366        uL as velocity (Brief="volume flow rate of liquid, m^3/m^2/s", Lower=0, Default = 0.007);
     367        uV as velocity (Brief="volume flow rate of vapor, m^3/m^2/s", Lower=0, Default = 1.14);
    368368        dp as length (Brief="Particle diameter", Default=1e-3);
    369369        invK as Real (Brief="Wall factor");
     
    400400        "Reynolds number of the vapor stream"
    401401        Rev*invK = dp*uV*rhoV / (miV*(1-e));
    402        
    403         "Resistance Coefficient"
    404         Qsio = Cpo * (64/Rev + 1.8/Rev^0.08);
     402
     403        if Rev > 1e-4 then
     404                "Resistance Coefficient"       
     405                Qsio = 1;#Cpo * (64/Rev + 1.8/Rev^0.08);
     406        else
     407                Qsio = 1;
     408        end
    405409
    406410        "Pressure drop and Vapor flow"
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