AIChE Symposium Series, Issue 323 |
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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 ... Reactive Distillation 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 ... Reactive Distillation 387.
Page 401
... reactive case , but with different amounts and distribution of forward and backward chemical reaction . In Fig . 7b ... Distillation Systems . PhD thesis , Norwegian University of Science and Technology . Dr.ing Dissertation No. 1998 : 121 .
... reactive case , but with different amounts and distribution of forward and backward chemical reaction . In Fig . 7b ... Distillation Systems . PhD thesis , Norwegian University of Science and Technology . Dr.ing Dissertation No. 1998 : 121 .
Page 501
... reactive distillation process is used , as an example , to demonstrate the feasibility and advantages of the proposed method . Reactive distillation was selected as example because it combines two processes of fairly high level of ...
... reactive distillation process is used , as an example , to demonstrate the feasibility and advantages of the proposed method . Reactive distillation was selected as example because it combines two processes of fairly high level of ...
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