Ignore:
Timestamp:
Sep 30, 2008, 10:00:48 PM (14 years ago)
Author:
Argimiro Resende Secchi
Message:

Fixing convergence problems!

File:
1 edited

Legend:

Unmodified
Added
Removed
  • trunk/sample/costs/sample_distillation_kettle_cond_cost.mso

    r530 r650  
    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';
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