Ignore:
Timestamp:
Jul 26, 2008, 6:11:53 PM (15 years ago)
Author:
gerson bicca
Message:

more updates

File:
1 edited

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  • branches/gui/sample/costs/sample_distillation_kettle_cond_cost.mso

    r530 r581  
    6060       
    6161        SPECIFY
    62         feed.Outlet.F = 113.4 * 'kmol/h';
    63         feed.Outlet.T = 291 * 'K';
    64         feed.Outlet.P = 168.3 * 'kPa';
    65         feed.Outlet.z = 1/NComp;
     62        feed.F = 113.4 * 'kmol/h';
     63        feed.T = 291 * 'K';
     64        feed.P = 168.3 * 'kPa';
     65        feed.Composition = 1/NComp;
    6666       
    6767        zero.F = 0 * 'kmol/h';
     
    7676        col.sptop.frac = 0.444445;
    7777        col.cond.OutletV.F = 0 * 'kmol/h';
    78         Qr.OutletQ.Q = 3.7743e6 * 'kJ/h';
    79         Qc.OutletQ.Q = -3.71e6 * 'kJ/h';
     78        Qr.OutletQ = 3.7743e6 * 'kJ/h';
     79        Qc.OutletQ = -3.71e6 * 'kJ/h';
    8080        col.pump1.dP = 16 * 'kPa';
    8181        col.trays.Emv = 1;
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