AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 14
... methanol to ethyl acetate in the reactor feed is kept above the ratio in the MeOH / EtOH bi- nary azeotrope , resulting in a product stream in distillation region 5 which yields product cuts consisting of the pure alcohols along with ...
... methanol to ethyl acetate in the reactor feed is kept above the ratio in the MeOH / EtOH bi- nary azeotrope , resulting in a product stream in distillation region 5 which yields product cuts consisting of the pure alcohols along with ...
Page 228
... methanol may be difficult because of homoge- neous azeotropes . Turning to the water destination , remov- al of both methyl acetate and methanol should be easy because of the large boiling point differences , but removal of the acetic ...
... methanol may be difficult because of homoge- neous azeotropes . Turning to the water destination , remov- al of both methyl acetate and methanol should be easy because of the large boiling point differences , but removal of the acetic ...
Page 229
... Methanol Acetic Acid Catalyst Methanol Reaction Task ( Removes Water ) Solvent - Enhanced Reaction Task E Distillative Separation Task G ( Removes Acetic Acid ) Distillative Separation Task J Methyl Acetate ( Eliminates Methanol ) ...
... Methanol Acetic Acid Catalyst Methanol Reaction Task ( Removes Water ) Solvent - Enhanced Reaction Task E Distillative Separation Task G ( Removes Acetic Acid ) Distillative Separation Task J Methyl Acetate ( Eliminates Methanol ) ...
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