AIChE Symposium Series, Issue 323 |
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Page 296
... MINLP problem into two subproblems : the NLP subproblem where all binary variables are fixed to 0 or 1 values , and the master subproblem , where a linearization of the non- linear equations of the original MINLP is performed . These ...
... MINLP problem into two subproblems : the NLP subproblem where all binary variables are fixed to 0 or 1 values , and the master subproblem , where a linearization of the non- linear equations of the original MINLP is performed . These ...
Page 366
... MINLP optimisation approach , there is freedom to choose the level of abstraction . In other words , we can decide to use rigorous mathematical calculation procedures for each unit - operation of which the MINLP superstructure is build ...
... MINLP optimisation approach , there is freedom to choose the level of abstraction . In other words , we can decide to use rigorous mathematical calculation procedures for each unit - operation of which the MINLP superstructure is build ...
Page 392
... MINLP . Problem TAC with MINLP Optimum TAC target TAC achieved Approach to target Reduction cf MINLP ( $ / yr . ) ( $ / yr . ) ( $ / yr . ) ( % ) ( % ) Copper extraction 49.000 49 000 49 000 0.0 0 Coke - oven gas sweetening 918 000 413 ...
... MINLP . Problem TAC with MINLP Optimum TAC target TAC achieved Approach to target Reduction cf MINLP ( $ / yr . ) ( $ / yr . ) ( $ / yr . ) ( % ) ( % ) Copper extraction 49.000 49 000 49 000 0.0 0 Coke - oven gas sweetening 918 000 413 ...
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