AIChE Symposium Series, Issue 323 |
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Results 1-3 of 79
Page 251
... procedure . It is our opinion that such a design procedure is not available yet , although some very relevant work has been done in both the fields of process design and crystallisation . Based on the pioneering work of Douglas ( 1985 ) ...
... procedure . It is our opinion that such a design procedure is not available yet , although some very relevant work has been done in both the fields of process design and crystallisation . Based on the pioneering work of Douglas ( 1985 ) ...
Page 262
... procedure , i.e. better designs in less time , cannot be guaranteed until the procedure as a whole is validated by means of industrial case studies . Main achievements so far are improved understanding of the design process and ...
... procedure , i.e. better designs in less time , cannot be guaranteed until the procedure as a whole is validated by means of industrial case studies . Main achievements so far are improved understanding of the design process and ...
Page 447
... procedure for identifying the optimal separation sequence using a dynamic programming method . This procedure was automated by Johns & Romero ( 1979 ) by introducing discrete programming techniques . Fraga & McKinnon ( 1994 ) extended ...
... procedure for identifying the optimal separation sequence using a dynamic programming method . This procedure was automated by Johns & Romero ( 1979 ) by introducing discrete programming techniques . Fraga & McKinnon ( 1994 ) extended ...
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