AIChE Symposium Series, Issue 323 |
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Page 183
... equations are Let ас ас дп + ¢ V + ( 1 - p ) at дх at n = f ( c ) = o ( c ) = 2/4 ( = ac 1 + Kc 1+ 1 - Φ Φ n α = 0 , = 1 + ( 1 + Kc ) 2 and transform the equations to ас ас σ ( c ) + V Ət = 0 дх 1 - $ df dc This equation underlies ...
... equations are Let ас ас дп + ¢ V + ( 1 - p ) at дх at n = f ( c ) = o ( c ) = 2/4 ( = ac 1 + Kc 1+ 1 - Φ Φ n α = 0 , = 1 + ( 1 + Kc ) 2 and transform the equations to ас ас σ ( c ) + V Ət = 0 дх 1 - $ df dc This equation underlies ...
Page 184
... equations ) . Textbooks usually treat only simple systems such as batch , CSTR , or plug flow reactors , usually for only a few components . The inclusion of the above effects are time- consuming to include , and hence are seldom ...
... equations ) . Textbooks usually treat only simple systems such as batch , CSTR , or plug flow reactors , usually for only a few components . The inclusion of the above effects are time- consuming to include , and hence are seldom ...
Page 225
... equations . Typically , an equation - orientated PME will assemble the sets of equations from the various units in the process into one large set ; it will extend this set with equations reflecting unit connectivity and , potentially ...
... equations . Typically , an equation - orientated PME will assemble the sets of equations from the various units in the process into one large set ; it will extend this set with equations reflecting unit connectivity and , potentially ...
Contents
INVITED PAPERS | 1 |
RECENT DEVELOPMENTS | 21 |
The Web and Flow of Information in Pharmaceutical RD | 23 |
Copyright | |
45 other sections not shown
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activities addition AIChE algorithm allow alternatives analysis application approach batch bound calculations changes Chem chemical codes column Comp complex components composition computational concepts considered constraints continuous cost defined described detailed determine distillation dynamic economic effect efficient energy engineering equations equipment et al evaluation example experiments feed Figure Floudas flow flowsheet formulation function given global optimization Grossmann heat important improve increase industry integration involved lifecycle linear material mathematical methods molecular networks nonlinear objective obtained operating parameters particle performance phase plant possible predict presented problem procedure process design process modeling programming properties proposed reaction reactor reduced selection separation shown shows simulation solution solved specific stage step strategy structure synthesis techniques temperature types unit variables