AIChE Symposium Series, Issue 323 |
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Page 92
... solution of ( 13 ) inside some rectangular region is strictly positive , then the solution of ( 12 ) inside the same rectangular domain will also be strictly positive . A strictly positive solution for ( 12 ) implies that the slack ...
... solution of ( 13 ) inside some rectangular region is strictly positive , then the solution of ( 12 ) inside the same rectangular domain will also be strictly positive . A strictly positive solution for ( 12 ) implies that the slack ...
Page 317
... solution concentrated by evaporation to give solution of required strength Continuous solution polymerisation Continuous solution of melt batch dilution Load Temperature Low Medium High Conversion of the impurity I , Low 0,66 Medium 0 ...
... solution concentrated by evaporation to give solution of required strength Continuous solution polymerisation Continuous solution of melt batch dilution Load Temperature Low Medium High Conversion of the impurity I , Low 0,66 Medium 0 ...
Page 460
... solution of nonconvex MINLPs . METAMODELING - A NOVEL APPROACH FOR PHENOMENA - ORIENTED MODEL. Algorithms Algorithm 1 : Global solution of nonconvex MINLPS Initialize : Iteration counter k = 0 , 1 = 1 , 7 ° = Ø , S0 = Ø , V ° = Ø . 2 ...
... solution of nonconvex MINLPs . METAMODELING - A NOVEL APPROACH FOR PHENOMENA - ORIENTED MODEL. Algorithms Algorithm 1 : Global solution of nonconvex MINLPS Initialize : Iteration counter k = 0 , 1 = 1 , 7 ° = Ø , S0 = Ø , V ° = Ø . 2 ...
Contents
INVITED PAPERS | 1 |
RECENT DEVELOPMENTS | 21 |
The Web and Flow of Information in Pharmaceutical RD | 23 |
Copyright | |
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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