AIChE Symposium Series, Issue 323 |
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Page 343
... column . For small values of the reflux above zero the distillates are aligned with the equilibrium vector y xB - XB starting from y XB when the reflux equals zero up to the point xD where the composition of the heaviest component ...
... column . For small values of the reflux above zero the distillates are aligned with the equilibrium vector y xB - XB starting from y XB when the reflux equals zero up to the point xD where the composition of the heaviest component ...
Page 402
... columns , there exists a single , optimal feed point . The feed location is known to be the point where the column composition is the same as that of the feed . In such systems it was shown that there is no advantage in the use of ...
... columns , there exists a single , optimal feed point . The feed location is known to be the point where the column composition is the same as that of the feed . In such systems it was shown that there is no advantage in the use of ...
Page 404
... column profile , which may have several benefits , as well as some not so desirable effects . However most columns ... column with a reflux ratio of 1.99 , and 22 equilibrium stages of which 5 are in the rectifying section , and 17 ...
... column profile , which may have several benefits , as well as some not so desirable effects . However most columns ... column with a reflux ratio of 1.99 , and 22 equilibrium stages of which 5 are in the rectifying section , and 17 ...
Contents
INVITED PAPERS | 1 |
RECENT DEVELOPMENTS | 21 |
The Web and Flow of Information in Pharmaceutical RD | 23 |
Copyright | |
45 other sections not shown
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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