AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 15
... azeotropes survive , but the other two are not present . The low - boiling binary azeotrope between MeOH and MeOAC is an unstable node and is connected to the intermediate- boiling saddle azeotrope between EtOH and EtOAc . This gives ...
... azeotropes survive , but the other two are not present . The low - boiling binary azeotrope between MeOH and MeOAC is an unstable node and is connected to the intermediate- boiling saddle azeotrope between EtOH and EtOAc . This gives ...
Page 230
... azeotrope , and the compositions of the two liquid phases into which the heterogeneous azeotrope sep- arates . Following the hierarchy to avoid the pinch critical fea- ture and to exploit the immiscibility region critical fea- ture , it ...
... azeotrope , and the compositions of the two liquid phases into which the heterogeneous azeotrope sep- arates . Following the hierarchy to avoid the pinch critical fea- ture and to exploit the immiscibility region critical fea- ture , it ...
Page 231
... azeotropic entrainer required by mass balance considerations ( so that the net feed is ex- actly collinear with acetic acid and the azeotrope ) is also the amount of reflux appropriate for the number of stages to produce the desired ...
... azeotropic entrainer required by mass balance considerations ( so that the net feed is ex- actly collinear with acetic acid and the azeotrope ) is also the amount of reflux appropriate for the number of stages to produce the desired ...
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