AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 244
... CSTR in the cascade processes a single or a two - phase stream , a synthesis structure based upon the above set of structural parameters is incomplete and em- beds a number of unrealistic scenarios ( i.e. settlers pro- cessing single ...
... CSTR in the cascade processes a single or a two - phase stream , a synthesis structure based upon the above set of structural parameters is incomplete and em- beds a number of unrealistic scenarios ( i.e. settlers pro- cessing single ...
Page 310
... CSTR locus . If this is also not con- vex , then continue with a new temperature optimized PFR trajectory starting at the point on the CSTR locus where the overall selectivity is highest . In the latter case , the opti- mal system will ...
... CSTR locus . If this is also not con- vex , then continue with a new temperature optimized PFR trajectory starting at the point on the CSTR locus where the overall selectivity is highest . In the latter case , the opti- mal system will ...
Page 311
... CSTR followed by a PFR . Figure 5. Temperature optimized reactor tra- jectories . ( PFR : _._ . CSTR : --- ) Fig . 6 displays the corresponding temperature profiles for the optimized reactor trajectories . It is seen that the re- actors ...
... CSTR followed by a PFR . Figure 5. Temperature optimized reactor tra- jectories . ( PFR : _._ . CSTR : --- ) Fig . 6 displays the corresponding temperature profiles for the optimized reactor trajectories . It is seen that the re- actors ...
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