AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 201
... solution ( see Floudas and Aggarwal , 1990 for a review of previous approaches and a decomposition strategy which alleviates but does not eliminate the multiplicity of local solutions problem ) . Ta- ble 1 presents results of local ...
... solution ( see Floudas and Aggarwal , 1990 for a review of previous approaches and a decomposition strategy which alleviates but does not eliminate the multiplicity of local solutions problem ) . Ta- ble 1 presents results of local ...
Page 210
... solution or are trapped to a local op- timum solution which may differ in value significantly form the global solution . Third , the global optimum solu- tion may have a very different physical interpretation when it is compared to ...
... solution or are trapped to a local op- timum solution which may differ in value significantly form the global solution . Third , the global optimum solu- tion may have a very different physical interpretation when it is compared to ...
Page 282
... solution , the DSP implies such a thread of control for which the multiple scheduling sub- problems must be solved before the next iteration can con- tinue . The DCABB system assumes full responsibility for conducting all branch and ...
... solution , the DSP implies such a thread of control for which the multiple scheduling sub- problems must be solved before the next iteration can con- tinue . The DCABB system assumes full responsibility for conducting all branch 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