AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 19
... Equilibrium stage model , Nonequilibrium models , Rate - based models , Separation process modeling . Introduction The equilibrium stage model has been with us for almost exactly 100 years . It is the standard model for simulating ...
... Equilibrium stage model , Nonequilibrium models , Rate - based models , Separation process modeling . Introduction The equilibrium stage model has been with us for almost exactly 100 years . It is the standard model for simulating ...
Page 24
... equilibrium equations are used in the two types of model . In equilibrium stage mod- els the balance equations are written around the stage as a whole and the composition of the leaving streams related through an assumption that they ...
... equilibrium equations are used in the two types of model . In equilibrium stage mod- els the balance equations are written around the stage as a whole and the composition of the leaving streams related through an assumption that they ...
Page 33
... equilibrium , so kinetic and equilibrium effects are closely coupled . Dynamic Models for a PSA Process The basic differential equations governing the perfor- mance of a PSA process come from transient differential mass , momentum and ...
... equilibrium , so kinetic and equilibrium effects are closely coupled . Dynamic Models for a PSA Process The basic differential equations governing the perfor- mance of a PSA process come from transient differential mass , momentum 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