AIChE Symposium Series, Issue 323 |
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Page 321
... reaction rate vector . This average is a weighted sum of all the instantaneous reaction rates obtained because of the different operating conditions throughout the reactor network . There are two different ways that the average rate can ...
... reaction rate vector . This average is a weighted sum of all the instantaneous reaction rates obtained because of the different operating conditions throughout the reactor network . There are two different ways that the average rate can ...
Page 393
... reaction or reactions . The number of possible main reactions is relatively small and the plausible alternatives quite obvious . This suggests that applying automatic synthesis methods to discover main reactions is unlikely to be ...
... reaction or reactions . The number of possible main reactions is relatively small and the plausible alternatives quite obvious . This suggests that applying automatic synthesis methods to discover main reactions is unlikely to be ...
Page 398
... reaction distribution ( ( n ) ) and internal reflux ratio ( a ) has been set . The structural impact of simultaneous reaction and separation depends critically on the properties of the VLE separation vector field and its inverse ...
... reaction distribution ( ( n ) ) and internal reflux ratio ( a ) has been set . The structural impact of simultaneous reaction and separation depends critically on the properties of the VLE separation vector field and its inverse ...
Contents
INVITED PAPERS | 1 |
RECENT DEVELOPMENTS | 21 |
The Web and Flow of Information in Pharmaceutical RD | 23 |
Copyright | |
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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