/[ascend]/trunk/models/reactor.a4l
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revision 576 by johnpye, Tue May 9 03:42:08 2006 UTC revision 821 by johnpye, Thu Aug 17 11:57:54 2006 UTC
# Line 581  MODEL test_single_phase_cstr() REFINES c Line 581  MODEL test_single_phase_cstr() REFINES c
581      END scale_all;      END scale_all;
582    
583      METHOD values;      METHOD values;
584          input.f['n_butane'] :=100 {kmol/hr};          input.f['n_butane'] :=100 {kmol/h};
585          input.f['butene_1'] :=100 {kmol/hr};          input.f['butene_1'] :=100 {kmol/h};
586          input.f['n_octane'] :=1e-11 {kmol/hr};          input.f['n_octane'] :=1e-11 {kmol/h};
587          input.T :=300 {K};          input.T :=300 {K};
588          input.P :=1 {atm};          input.P :=1 {atm};
589          reactor.state.T :=320 {K};          reactor.state.T :=320 {K};
# Line 672  MODEL test_multiple_phase_cstr() REFINES Line 672  MODEL test_multiple_phase_cstr() REFINES
672      END scale_all;      END scale_all;
673    
674      METHOD values;      METHOD values;
675          vapin.f['n_butane'] :=100 {kmol/hr};          vapin.f['n_butane'] :=100 {kmol/h};
676          vapin.f['butene_1'] :=100 {kmol/hr};          vapin.f['butene_1'] :=100 {kmol/h};
677          vapin.f['n_octane'] :=1e-10 {kmol/hr};          vapin.f['n_octane'] :=1e-10 {kmol/h};
678          vapin.T :=300 {K};          vapin.T :=300 {K};
679          vapin.P :=1 {atm};          vapin.P :=1 {atm};
680          liqin.f['n_butane'] :=100 {kmol/hr};          liqin.f['n_butane'] :=100 {kmol/h};
681          liqin.f['butene_1'] :=100 {kmol/hr};          liqin.f['butene_1'] :=100 {kmol/h};
682          liqin.f['n_octane'] :=1e-10 {kmol/hr};          liqin.f['n_octane'] :=1e-10 {kmol/h};
683          liqin.T :=300 {K};          liqin.T :=300 {K};
684          liqin.P :=1 {atm};          liqin.P :=1 {atm};
685          reactor.state.T :=320 {K};          reactor.state.T :=320 {K};

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john.pye@anu.edu.au
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