AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 57
... structure . Generally , the maximum number of parallel branches needed in the structure is related to the dimensionality of the problem . A point in the interior of A can be achieved by infinitely many different reactor structures ; we ...
... structure . Generally , the maximum number of parallel branches needed in the structure is related to the dimensionality of the problem . A point in the interior of A can be achieved by infinitely many different reactor structures ; we ...
Page 111
... structure . A disturbance regime is defined , and an optimal control structure is sought which minimises the sum of the economic giveaway implied by the ball - size analysis ( Fig . 1 ) and the costs of instrumentation associat- ed with ...
... structure . A disturbance regime is defined , and an optimal control structure is sought which minimises the sum of the economic giveaway implied by the ball - size analysis ( Fig . 1 ) and the costs of instrumentation associat- ed with ...
Page 291
... structures of the HDA process and the process with a heat pump are summarized in Table 2. It is evident that the pro- cess structure , obtained with the NLP method , gives the lowest total annual costs when observing Example 1 . Structures ...
... structures of the HDA process and the process with a heat pump are summarized in Table 2. It is evident that the pro- cess structure , obtained with the NLP method , gives the lowest total annual costs when observing Example 1 . Structures ...
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