AIChE Symposium Series, Issue 323 |
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Page 345
... distillation regions divide the concentration simplex as was noted by Van Dongen and Doherty ( 1985 ) . Each one of the distillation regions has one unstable node , one or more saddle nodes and one stable node . As in the previous ...
... distillation regions divide the concentration simplex as was noted by Van Dongen and Doherty ( 1985 ) . Each one of the distillation regions has one unstable node , one or more saddle nodes and one stable node . As in the previous ...
Page 381
... distillation schemes by using a computer program to calculate the efficiencies of various possible configurations for ternary distillation . Ternary distillation , Thermally coupled columns , Thermodynamic efficiency , Minimum energy ...
... distillation schemes by using a computer program to calculate the efficiencies of various possible configurations for ternary distillation . Ternary distillation , Thermally coupled columns , Thermodynamic efficiency , Minimum energy ...
Page 387
... distillation is worse than a simple combination of reaction and distillation . 1.00 D 0.75 To apply the rule , it is only necessary to know the composition of the feed at chemical equilibrium and the vapor composition arising from that ...
... distillation is worse than a simple combination of reaction and distillation . 1.00 D 0.75 To apply the rule , it is only necessary to know the composition of the feed at chemical equilibrium and the vapor composition arising from that ...
Contents
INVITED PAPERS | 1 |
RECENT DEVELOPMENTS | 21 |
The Web and Flow of Information in Pharmaceutical RD | 23 |
Copyright | |
45 other sections not shown
Common terms and phrases
activities addition AIChE algorithm allow alternatives analysis application approach batch bound calculations changes Chem chemical codes column Comp complex components composition computational concepts considered constraints continuous cost defined described detailed determine distillation dynamic economic effect efficient energy engineering equations equipment et al evaluation example experiments feed Figure Floudas flow flowsheet formulation function given global optimization Grossmann heat important improve increase industry integration involved lifecycle linear material mathematical methods molecular networks nonlinear objective obtained operating parameters particle performance phase plant possible predict presented problem procedure process design process modeling programming properties proposed reaction reactor reduced selection separation shown shows simulation solution solved specific stage step strategy structure synthesis techniques temperature types unit variables