AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 25
... vapor phase include a term for mass trans- ferred from the vapor phase to each of the liquid phases . The material balances for each liquid phase includes a term for mass transfer from the vapor phase and a term for mass transfer ...
... vapor phase include a term for mass trans- ferred from the vapor phase to each of the liquid phases . The material balances for each liquid phase includes a term for mass transfer from the vapor phase and a term for mass transfer ...
Page 59
... vapor removal per unit vol- ume , Y is the mole fraction vector describing the vapor composition in equilibrium with the liquid of composition X and t is a scalar parameter . We will refer to S = ( X - Y ( X ) ) as the separation vector ...
... vapor removal per unit vol- ume , Y is the mole fraction vector describing the vapor composition in equilibrium with the liquid of composition X and t is a scalar parameter . We will refer to S = ( X - Y ( X ) ) as the separation vector ...
Page 191
... vapor , we cool the re- actor exit stream to 100 ° F ( cooling water temperature ) and then flash , filter and decant , depending on the phases obtained . Some- times both a high and a low pressure flash are desirable . 6. If the ...
... vapor , we cool the re- actor exit stream to 100 ° F ( cooling water temperature ) and then flash , filter and decant , depending on the phases obtained . Some- times both a high and a low pressure flash are desirable . 6. If 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