AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 14
... acetate in the reactor feed is kept above the ratio in the MeOH / EtOH bi ... methyl formate is used as an entrainer for batch extractive distilla- tion ... acetate and a significant amount of the methanol is left for recycle . We know of ...
... acetate in the reactor feed is kept above the ratio in the MeOH / EtOH bi ... methyl formate is used as an entrainer for batch extractive distilla- tion ... acetate and a significant amount of the methanol is left for recycle . We know of ...
Page 228
... methyl acetate and byproduct water destinations , two sets of differences are detected . For the methyl acetate destination , acetic ac- id , water , and methanol must all be essentially completely removed . For the water destination , ...
... methyl acetate and byproduct water destinations , two sets of differences are detected . For the methyl acetate destination , acetic ac- id , water , and methanol must all be essentially completely removed . For the water destination , ...
Page 229
... methyl acetate - water azeotrope ( Task G ) , and conventional distil- lative separation might be used to separate both methyl ac- etate ( Task H ) and methanol ( Task I ) from water , and acetic acid from methyl acetate ( Task J ) ...
... methyl acetate - water azeotrope ( Task G ) , and conventional distil- lative separation might be used to separate both methyl ac- etate ( Task H ) and methanol ( Task I ) from water , and acetic acid from methyl acetate ( Task J ) ...
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