AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 17
... Column Composition Profile Figure 12. Liquid composition profile in the distillation column for Example 5 . As an alternative it may also be possible to feed the ex- tract phase to an extractive distillation column . This would require ...
... Column Composition Profile Figure 12. Liquid composition profile in the distillation column for Example 5 . As an alternative it may also be possible to feed the ex- tract phase to an extractive distillation column . This would require ...
Page 22
... distillation problems are , in one sense or another , extensions of meth ... column specifications and the presence of energy balances but only limited ... column specifi- cations . They also show which sets of column specifica- tions can ...
... distillation problems are , in one sense or another , extensions of meth ... column specifications and the presence of energy balances but only limited ... column specifi- cations . They also show which sets of column specifica- tions can ...
Page 287
... distillation column has been found to have three - phases ( one vapor and two liquid ) . Assuming that the MHV2 - model is more correct than the earlier GCEOS - model , it is likely that inconsistent energy costs have been reported by ...
... distillation column has been found to have three - phases ( one vapor and two liquid ) . Assuming that the MHV2 - model is more correct than the earlier GCEOS - model , it is likely that inconsistent energy costs have been reported by ...
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