AIChE Symposium Series, Issue 323 |
From inside the book
Results 1-3 of 40
Page 387
... reactive distillation is worse than a simple combination of reaction and distillation . 1.00 D 0.75 To apply the rule , it is only necessary to know the composition of the feed at chemical equilibrium and the vapor composition arising ...
... reactive distillation is worse than a simple combination of reaction and distillation . 1.00 D 0.75 To apply the rule , it is only necessary to know the composition of the feed at chemical equilibrium and the vapor composition arising ...
Page 399
... reactive rectifying section . a sample composition profile with artificial VLE closely resembles the profiles known from ideal mixtures . With the non - reactive composition profile fixed with an arbitrary orientation compared to the ...
... reactive rectifying section . a sample composition profile with artificial VLE closely resembles the profiles known from ideal mixtures . With the non - reactive composition profile fixed with an arbitrary orientation compared to the ...
Page 401
... reactive case , but with different amounts and distribution of forward and backward chemical reaction . In Fig . 7b the actual compositions are marked with filled circles and we also note that the non - reactive profile encounters a ...
... reactive case , but with different amounts and distribution of forward and backward chemical reaction . In Fig . 7b the actual compositions are marked with filled circles and we also note that the non - reactive profile encounters a ...
Contents
INVITED PAPERS | 1 |
RECENT DEVELOPMENTS | 21 |
The Web and Flow of Information in Pharmaceutical RD | 23 |
Copyright | |
45 other sections not shown
Common terms and phrases
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