Global Optimization of Ideal Multi-component Distillation Columns

dc.contributor.authorMertens, Nick
dc.contributor.authorKunde, Christian
dc.contributor.authorKienle, Achim
dc.contributor.authorMichaels, Dennis
dc.date.accessioned2017-05-23T13:30:35Z
dc.date.available2017-05-23T13:30:35Z
dc.date.issued2017-05
dc.description.abstractThis paper addresses the problem of determining cost-minimal process designs for ideal multi-component distillation columns. The special case of binary distillation was considered in former work. Therein, a problem-specific bound-tightening strategy based on monotonic mole fraction profiles of single components was developed to solve the corresponding MINLPs, globally. In the multi-component setting, the mole fraction profiles of single components may not be monotonic, which is why the bound-tightening strategy from the binary case cannot be applied. In this follow-up paper, a model reformulation for ideal multi-component distillation columns is presented. The reformulation is achieved by suitable aggregations of the involved components. Proofs are given showing that mole fraction profiles of aggregated components are monotonic. This property is then used to adapt the bound-tightening strategy from the two-component case to the proposed model reformulation. Computational results are provided that indicate the usefulness of both the model reformulation and the adapted bound tightening technique for deterministic global optimization of ideal multi-component distillation column designs.en
dc.identifier.issn2190-1767
dc.identifier.urihttp://hdl.handle.net/2003/35965
dc.identifier.urihttp://dx.doi.org/10.17877/DE290R-17988
dc.language.isoen
dc.relation.ispartofseriesErgebnisberichte des Instituts für Angewandte Mathematik;567de
dc.subject.ddc610
dc.titleGlobal Optimization of Ideal Multi-component Distillation Columnsen
dc.typeText
dc.type.publicationtypepreprint
dcterms.accessRightsopen access

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