/[ascend]/trunk/models/when_demo.a4c
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revision 108 by aw0a, Fri Oct 29 20:54:12 2004 UTC revision 109 by johnpye, Wed Dec 14 00:34:09 2005 UTC
# Line 734  MODEL test_flowsheet REFINES flowsheet; Line 734  MODEL test_flowsheet REFINES flowsheet;
734      f1.stream.state.Cpi['D'] := 0.055 {BTU/mole/K};      f1.stream.state.Cpi['D'] := 0.055 {BTU/mole/K};
735    
736  (* Feed 1 *)  (* Feed 1 *)
737      f1.cost_factor := 0.026 {dollar/kg_mole};      f1.cost_factor := 0.026 {USD/kg_mole};
738    
739  (* Feed 2 *)  (* Feed 2 *)
740      f2.cost_factor := 0.033 {dollar/kg_mole};      f2.cost_factor := 0.033 {USD/kg_mole};
741    
742  (* Cooler 1 *)  (* Cooler 1 *)
743      co1.cost_factor  := 0.7e-06 {dollar/kJ};      co1.cost_factor  := 0.7e-06 {USD/kJ};
744      co1.heat_removed := 100 {BTU/s};      co1.heat_removed := 100 {BTU/s};
745    
746  (* Cooler 2 *)  (* Cooler 2 *)
747      co2.heat_removed := 150 {BTU/s};      co2.heat_removed := 150 {BTU/s};
748      co2.cost_factor  := 0.7e-06 {dollar/kJ};      co2.cost_factor  := 0.7e-06 {USD/kJ};
749    
750  (* Heater 1 *)  (* Heater 1 *)
751      h1.heat_supplied := 200 {BTU/s};      h1.heat_supplied := 200 {BTU/s};
752      h1.cost_factor  := 8e-06 {dollar/kJ};      h1.cost_factor  := 8e-06 {USD/kJ};
753    
754  (* Heater 2 *)  (* Heater 2 *)
755      h2.heat_supplied := 180 {BTU/s};      h2.heat_supplied := 180 {BTU/s};
756      h2.cost_factor  := 8e-06 {dollar/kJ};      h2.cost_factor  := 8e-06 {USD/kJ};
757    
758  (* Heater 3 *)  (* Heater 3 *)
759      h3.heat_supplied := 190 {BTU/s};      h3.heat_supplied := 190 {BTU/s};
760      h3.cost_factor  := 8e-06 {dollar/kJ};      h3.cost_factor  := 8e-06 {USD/kJ};
761    
762  (* Flash *)  (* Flash *)
763      fl1.alpha['A'] := 12.0;      fl1.alpha['A'] := 12.0;
# Line 773  MODEL test_flowsheet REFINES flowsheet; Line 773  MODEL test_flowsheet REFINES flowsheet;
773      m1.To := 298 {K};      m1.To := 298 {K};
774    
775  (* Single Compressor 1 *)  (* Single Compressor 1 *)
776      c1.cost_factor := 8.33333e-06 {dollar/kJ};      c1.cost_factor := 8.33333e-06 {USD/kJ};
777      c1.pressure_rate := 2.5;      c1.pressure_rate := 2.5;
778    
779  (* Single Compressor 2 *)  (* Single Compressor 2 *)
780      c2.cost_factor := 8.33333e-06 {dollar/kJ};      c2.cost_factor := 8.33333e-06 {USD/kJ};
781      c2.pressure_rate := 1.5;      c2.pressure_rate := 1.5;
782    
783  (* Staged Compressor 1 *)  (* Staged Compressor 1 *)
784      s1.cost_factor_work := 8.33333e-06 {dollar/kJ};      s1.cost_factor_work := 8.33333e-06 {USD/kJ};
785      s1.cost_factor_heat := 0.7e-06 {dollar/kJ};      s1.cost_factor_heat := 0.7e-06 {USD/kJ};
786      s1.pressure_rate := 2.5;      s1.pressure_rate := 2.5;
787          s1.n_stages := 2.0;          s1.n_stages := 2.0;
788    
789  (* Staged Compressor 2 *)  (* Staged Compressor 2 *)
790      s2.cost_factor_work := 8.33333e-06 {dollar/kJ};      s2.cost_factor_work := 8.33333e-06 {USD/kJ};
791      s2.cost_factor_heat := 0.7e-06 {dollar/kJ};      s2.cost_factor_heat := 0.7e-06 {USD/kJ};
792      s2.pressure_rate := 1.5;      s2.pressure_rate := 1.5;
793          s2.n_stages := 2.0;          s2.n_stages := 2.0;
794    
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john.pye@anu.edu.au
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