AIChE Symposium Series, Issue 323 |
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Page 402
... 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 distributed feeds . This result is also known ...
... 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 distributed feeds . This result is also known ...
Page 404
... feed column with a reflux ratio of 1.99 , and 22 equilibrium stages of which 5 are in the rectifying section , and 17 stripping stages . This result is shown as the profiles in Figure 3 . With the addition of a second feed point on the ...
... feed column with a reflux ratio of 1.99 , and 22 equilibrium stages of which 5 are in the rectifying section , and 17 stripping stages . This result is shown as the profiles in Figure 3 . With the addition of a second feed point on the ...
Page 405
... feed flowrate selected , and the feed point , this can lead to either an increase or in some cases a decrease in the number of stages . On a fundamental level using only the number of stages as an indicator this would seem to have some ...
... feed flowrate selected , and the feed point , this can lead to either an increase or in some cases a decrease in the number of stages . On a fundamental level using only the number of stages as an indicator this would seem to have some ...
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