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
AIChE algorithm analysis application azeotropic batch process behavior Biegler branch and bound CAPE-OPEN Chem Chem Eng Chemical Engineering chemical process chemical process modeling column Comp Chem components composition computational computational chemistry concepts constraints cost crystallisation distillation dynamic energy equations equipment evaluation example exergy feed Figure Floudas flow flowsheet formulation function global optimization Grossmann implementation industry information model integration interactions interface iteration J.D. Perkins kinetic lifecycle linear linear programming material mathematical methods microfabricated Microreaction Technology microreactor MINLP molecular molecular dynamics networks nonconvex nonlinear programming optimisation optimization problems Pantelides parameters particle performance phase Pistikopoulos plant process design process development process engineering process modeling process optimization process synthesis process systems properties reaction reactive distillation reactor recycle selection simulation solution solved solvents solver specific stage Stephanopoulos strategy structure techniques temperature thermodynamic unit operations