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dc.contributor.authorCarranza Abaid, Andres
dc.contributor.authorGonzalez-Garcia, Raul
dc.date.accessioned2021-09-01T07:16:33Z
dc.date.available2021-09-01T07:16:33Z
dc.date.created2021-01-03T18:17:26Z
dc.date.issued2020
dc.identifier.issn0255-2701
dc.identifier.urihttps://hdl.handle.net/11250/2772098
dc.description.abstractThermally coupled distillation columns (TCDC) have proven to be a superior and feasible alternative compared to conventional distillation. However, their inherent system complexity presents optimization and operational challenges. In this work, we analyzed these problems from a different perspective: understanding the steady-state behavior by the means of a steady state and bifurcation analysis. This approach used a dynamic model programmed in Matlab 2019b and validated with Aspen Plus v8.8. The analysis demonstrated that the steady-state multiplicity is triggered by the magnitude of the internal flows and that the interlinking trays may develop isolated bifurcation branches. Moreover, it is shown that the “operational holes” or intermittent discontinuities in the TCDC steady states are formed by saddle-node bifurcations. This suggests that a non-smooth optimization algorithm is more suitable for TCDC design.en_US
dc.language.isoengen_US
dc.publisherElsevieren_US
dc.titleA Petlyuk distillation column dynamic analysis: Hysteresis and bifurcationsen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.source.volume149en_US
dc.source.journalChemical Engineering and Processingen_US
dc.identifier.doihttps://doi.org/10.1016/j.cep.2020.107843
dc.identifier.cristin1864440
dc.description.localcodeThis article will not be available due to copyright restrictions (c) 2020 by Elsevieren_US
cristin.ispublishedfalse
cristin.fulltextpreprint
cristin.qualitycode1


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