AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 210
... Floudas and Visweswaran 1990 , 1993 ; Ben - Tal et al . 1994 ) , ( g ) Reformulation - Lineariza- tion methods ( e.g. Sherali and Alameddine , 1992 ; Sherali and Tuncbilek 1992 ) , and ( h ) Interval methods ( e.g. Hans- en 1979 ) . The ...
... Floudas and Visweswaran 1990 , 1993 ; Ben - Tal et al . 1994 ) , ( g ) Reformulation - Lineariza- tion methods ( e.g. Sherali and Alameddine , 1992 ; Sherali and Tuncbilek 1992 ) , and ( h ) Interval methods ( e.g. Hans- en 1979 ) . The ...
Page 215
... Floudas and Visweswaran ( 1990 ) and Visweswaran and Floudas ( 1993 ) . The fourth and fifth pooling problems are described in Ben - Tal et al . ( 1994 ) . The first two heat exchanger problems are taken from Floudas and Ciric ( 1989 ) ...
... Floudas and Visweswaran ( 1990 ) and Visweswaran and Floudas ( 1993 ) . The fourth and fifth pooling problems are described in Ben - Tal et al . ( 1994 ) . The first two heat exchanger problems are taken from Floudas and Ciric ( 1989 ) ...
Page 220
... Floudas ( 1994 ) . Stability in Optimal De- sign : Synthesis of Complex Reactor Networks . AIChE J. , 40 ( 5 ) , 849-861 . Lien , K. M. And Wahl , P. E. ( 1991 ) . If you can't beat them , join them . Combine Artificial Intelligence and ...
... Floudas ( 1994 ) . Stability in Optimal De- sign : Synthesis of Complex Reactor Networks . AIChE J. , 40 ( 5 ) , 849-861 . Lien , K. M. And Wahl , P. E. ( 1991 ) . If you can't beat them , join them . Combine Artificial Intelligence and ...
Contents
Keynote Address | 1 |
Separation System Synthesis and Design | 7 |
Modeling and Analysis of Multicomponent Separation Processes | 19 |
Copyright | |
29 other sections not shown
Common terms and phrases
acetic acid activities AIChE algorithm alternatives analysis application approach attainable region azeotrope azeotropic distillation batch branch and bound calculations cess Chem Chemical Engineering chemical process complex components composition concepts constraints cost CSTR data models decision-mapping defined described developed distillation column dynamic energy Engng environment equations equilibrium equipment example feed Figure Floudas flow flowsheet formulation function global optimization Grossmann hierarchical implementation industrial integration interface linear liquid logic mass material mathematical methanol methods methyl acetate MILP MINLP mixture n-dim network synthesis Newton's method nonlinear nonlinear programming paper parameters phase pinch plant pressure problem procedure process design process modelling process synthesis programming properties reac reaction reactive distillation reactor network recycle Seider separation system SimRefinery simulation solution solvent solving specific stage strategy stream structure target task techniques temperature tion unit operations values vapor variables