AIChE Symposium Series, Issue 323 |
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Page 334
... exergy used to create that driving force . The cost of the energy conversion equipment is also often a monotone function of the consumption of that type of exergy , although the operating condition may have a significant effect , too ...
... exergy used to create that driving force . The cost of the energy conversion equipment is also often a monotone function of the consumption of that type of exergy , although the operating condition may have a significant effect , too ...
Page 335
... exergy consumption is proportional to the driving force . These cases are , however , much less frequently encountered in the process industry . Heat Transfer Except in the cases in which radiation plays an important role , such as in ...
... exergy consumption is proportional to the driving force . These cases are , however , much less frequently encountered in the process industry . Heat Transfer Except in the cases in which radiation plays an important role , such as in ...
Page 382
... Exergy loss is calculated by balancing the exergies of all the material streams entering and leaving the distillation column system , excluding the reboilers and condensers . It was shown by Agrawal and Herron ( 1997 ) that it is ...
... Exergy loss is calculated by balancing the exergies of all the material streams entering and leaving the distillation column system , excluding the reboilers and condensers . It was shown by Agrawal and Herron ( 1997 ) that it is ...
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