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Distillation sequence superstructure optimization

Consider now ways in which the best arrangement of a distillation sequence can be determined more systematically. Given the possibilities for changing the sequence of simple columns or the introduction of prefractionators, side-strippers, side-rectifiers and fully thermally coupled arrangements, the problem is complex with many structural options. The problem can be addressed using the optimization of a superstructure. As discussed in Chapter 1, this approach starts by setting up a grand flowsheet in which all structural features for an optimal solution are embedded. [Pg.228]

HEAT-INTEGRATED DISTILLATION SEQUENCES BASED ON THE OPTIMIZATION OF A SUPERSTRUCTURE... [Pg.454]

Another class of separation problem attacked has been that of designing the most effective thermally coupled distillation column arrangement to separate a multicomponent mixture. Sargent and Gaxninibandara (1975) present a general column superstructure which they optimize. Imbedded in the superstructure are all the alternative thermally coupled and ordinary column sequences to be considered. The optimization eliminates those portions of the superstructure which are not economic leaving, hopefully, the optimal substructure. [Pg.71]


See other pages where Distillation sequence superstructure optimization is mentioned: [Pg.228]    [Pg.228]    [Pg.381]    [Pg.394]    [Pg.395]    [Pg.176]    [Pg.235]    [Pg.507]    [Pg.59]    [Pg.231]    [Pg.454]    [Pg.38]    [Pg.91]    [Pg.91]    [Pg.95]    [Pg.96]    [Pg.249]   
See also in sourсe #XX -- [ Pg.228 , Pg.229 ]




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