AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 43
... specific target products from specific raw materials . Suppose , for example , that the objective is to in- crease the octane number of the product of fluid catalytic cracking . We have a general idea for what products lead to higher ...
... specific target products from specific raw materials . Suppose , for example , that the objective is to in- crease the octane number of the product of fluid catalytic cracking . We have a general idea for what products lead to higher ...
Page 190
... specific separation subsystems , in a loose hierarchy of design sub - levels ( Douglas , 1992 ) , as follows : General separation structure ; identi- fication of specific separation sub- systems . Vapor recovery system ; to recover ...
... specific separation subsystems , in a loose hierarchy of design sub - levels ( Douglas , 1992 ) , as follows : General separation structure ; identi- fication of specific separation sub- systems . Vapor recovery system ; to recover ...
Page 194
... specific knowledge to do the following ; acquire necessary data , reason with a specific set of rules , execute a design algo- rithm , carry out an optimization procedure , update the state of the evolving design , etc. To represent the ...
... specific knowledge to do the following ; acquire necessary data , reason with a specific set of rules , execute a design algo- rithm , carry out an optimization procedure , update the state of the evolving design , etc. To represent the ...
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