AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 15
... example , if an equimolar mixture of methanol and ethyl acetate is fed to the reactor , the product may have a composition in a re- gion where a second extractive distillation is needed ( Ber- not et al . 1991 ) . Once again , we can ...
... example , if an equimolar mixture of methanol and ethyl acetate is fed to the reactor , the product may have a composition in a re- gion where a second extractive distillation is needed ( Ber- not et al . 1991 ) . Once again , we can ...
Page 44
... example will be ẞ - scission of a alkyl cation ( Fig . 1c ) : ( Label C1 + ( Find positive - carbon ) ) ( Label C2 ( Find carbon attached - to C1 + ) ) ( Label C3 ( Find carbon attached - to C2 ) ) ( Forbid ( Find aromatic - ring ...
... example will be ẞ - scission of a alkyl cation ( Fig . 1c ) : ( Label C1 + ( Find positive - carbon ) ) ( Label C2 ( Find carbon attached - to C1 + ) ) ( Label C3 ( Find carbon attached - to C2 ) ) ( Forbid ( Find aromatic - ring ...
Page 248
... Example 3. In Example 2 , decision - mapping d1 [ m1 ] is consistent ; however , decision - mapping d2 [ m2 ] = d1 [ m1 ] U { ( C , { ( { D , E } , { B , C } ) , ( { F } , { A , C } ) } ) } is inconsistent since d2 ( C ) N 82 ( A ) ...
... Example 3. In Example 2 , decision - mapping d1 [ m1 ] is consistent ; however , decision - mapping d2 [ m2 ] = d1 [ m1 ] U { ( C , { ( { D , E } , { B , C } ) , ( { F } , { A , C } ) } ) } is inconsistent since d2 ( C ) N 82 ( A ) ...
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