AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 116
... strategy design but also the integration of these two functions . This has caused the relationship between pro- cess design and control strategy design to change as the need for better integration has increased . There is move- ment ...
... strategy design but also the integration of these two functions . This has caused the relationship between pro- cess design and control strategy design to change as the need for better integration has increased . There is move- ment ...
Page 119
... strategy , safety interlock strategy , major equipment specifications , equipment layout , environmental and regulatory specifica- tions , etc. This package is then used as the basis for the de- tailed design and construction of the ...
... strategy , safety interlock strategy , major equipment specifications , equipment layout , environmental and regulatory specifica- tions , etc. This package is then used as the basis for the de- tailed design and construction of the ...
Page 120
... strategy for each unit operation must be developed within the framework of the overall component inventory control strategy . Each component , whether important or insignifi- cant , must have a mechanism by which its inventory is ...
... strategy for each unit operation must be developed within the framework of the overall component inventory control strategy . Each component , whether important or insignifi- cant , must have a mechanism by which its inventory is ...
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