- Timestamp:
- Jul 26, 2008, 6:11:53 PM (15 years ago)
- File:
-
- 1 edited
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branches/gui/sample/costs/sample_distillation_kettle_cond_cost.mso
r530 r581 60 60 61 61 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; 66 66 67 67 zero.F = 0 * 'kmol/h'; … … 76 76 col.sptop.frac = 0.444445; 77 77 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'; 80 80 col.pump1.dP = 16 * 'kPa'; 81 81 col.trays.Emv = 1;
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