AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 52
... approach . The targeting approach is based on geometric interpretations of reaction and mixing . It uses a constructive approach to find the attainable region ; that is , it effectively captures all possible reactor structures and finds ...
... approach . The targeting approach is based on geometric interpretations of reaction and mixing . It uses a constructive approach to find the attainable region ; that is , it effectively captures all possible reactor structures and finds ...
Page 66
American Institute of Chemical Engineers. Furthermore as the approach effectively finds all possible outputs from all possible reactor networks , and then searches over this set of solutions for the optimal one , it is not a feasible ...
American Institute of Chemical Engineers. Furthermore as the approach effectively finds all possible outputs from all possible reactor networks , and then searches over this set of solutions for the optimal one , it is not a feasible ...
Page 270
... approach has been shown to be quite promising in handling these difficulties . In this paper , we re- view some recent results using this approach for the design of polymers and refrigerants . Computer - aided molecular design ...
... approach has been shown to be quite promising in handling these difficulties . In this paper , we re- view some recent results using this approach for the design of polymers and refrigerants . Computer - aided molecular design ...
Contents
Keynote Address | 1 |
Separation System Synthesis and Design | 7 |
Modeling and Analysis of Multicomponent Separation Processes | 19 |
Copyright | |
29 other sections not shown
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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