AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 61
... attainable region ( but not the entire region itself ) has been found . Here we modify the AR description slightly and first consider ARs in segregated flow , rather than sim- ple PFRS . For isothermal problems , the segregated flow or ...
... attainable region ( but not the entire region itself ) has been found . Here we modify the AR description slightly and first consider ARs in segregated flow , rather than sim- ple PFRS . For isothermal problems , the segregated flow or ...
Page 309
... Attainable Region concept to cater for temperature pro- file optimization in cases where the reaction mixture composition is uniquely described by less than three independent composition variables . The method may be extended to also ...
... Attainable Region concept to cater for temperature pro- file optimization in cases where the reaction mixture composition is uniquely described by less than three independent composition variables . The method may be extended to also ...
Page 310
... attainable in practice . The scope of the method is further limited to 2 - dimensional composition problems , i.e. the composition of the reaction mixture is assumed to be uniquely defined in a plane . If the Attainable Region for an ...
... attainable in practice . The scope of the method is further limited to 2 - dimensional composition problems , i.e. the composition of the reaction mixture is assumed to be uniquely defined in a plane . If the Attainable Region for an ...
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