AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 74
... properties of the MSA are ( Hayes , 1988 ; Cohen , 1988 ) : • Partition coefficient of the solute among the MSA and the original solvent ( if the solvents are immiscible this information can be re- covered from the activity coefficients ...
... properties of the MSA are ( Hayes , 1988 ; Cohen , 1988 ) : • Partition coefficient of the solute among the MSA and the original solvent ( if the solvents are immiscible this information can be re- covered from the activity coefficients ...
Page 133
... properties be accurate over the entire range of possible ap- plication of the model . This can be a rather stringent re- quirement : for example , during plant startup and shutdown , or in batch processes , composition and condi- tion ...
... properties be accurate over the entire range of possible ap- plication of the model . This can be a rather stringent re- quirement : for example , during plant startup and shutdown , or in batch processes , composition and condi- tion ...
Page 148
American Institute of Chemical Engineers. Point Properties vs. Parametrized Properties The Physical Properties Model distinguishes between a point property and a parameterized property . Fig . 6 and Fig . 7 summarize the current PDXI ...
American Institute of Chemical Engineers. Point Properties vs. Parametrized Properties The Physical Properties Model distinguishes between a point property and a parameterized property . Fig . 6 and Fig . 7 summarize the current PDXI ...
Contents
Keynote Address | 1 |
Separation System Synthesis and Design | 7 |
Modeling and Analysis of Multicomponent Separation Processes | 19 |
Copyright | |
29 other sections not shown
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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