Simulation of an industrial adiabatic multi-bed catalytic reactor for sulfur dioxide oxidation using the Maxwell-Stefan model

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dc.citation.journalTitleCHEMICAL ENGINEERING JOURNAL
dc.contributor.authorGomez-Garcia, Miguel-Angel
dc.contributor.authorDobrosz-Gomez, Izabela
dc.contributor.authorGil Pavas, E.
dc.contributor.authorRynkowski, Jacek
dc.contributor.departmentUniversidad EAFIT. Departamento de Ingeniería de Procesosspa
dc.contributor.researchgroupProcesos Ambientales (GIPAB)spa
dc.creatorGomez-Garcia, Miguel-Angel
dc.creatorDobrosz-Gomez, Izabela
dc.creatorGil Pavas, E.
dc.creatorRynkowski, Jacek
dc.date.accessioned2021-04-16T20:27:36Z
dc.date.available2021-04-16T20:27:36Z
dc.date.issued2015-12-15
dc.description.abstractIn this work, a rigorous heterogeneous model for the analysis of an industrial adiabatic multi-bed catalytic reactor for sulfur dioxide oxidation was developed. It was based on the Maxwell-Stefan diffusional model, which was selected from the analysis of the Maxwell-Stefan diffusivity and the thermodynamic correction factor matrix. The reactor model, implemented in MatLab, allowed evaluating truthfully the behavior of each catalytic bed (e.g., concentration, conversion, pressure and temperature profiles) with errors lower than 3%. Additionally, the effectiveness factor variation along the reactor was estimated. Thus, a better understanding of the effect of diffusional resistances on reactor performance was possible. (C) 2015 Elsevier B.V. All rights reserved.eng
dc.identifierhttps://eafit.fundanetsuite.com/Publicaciones/ProdCientif/PublicacionFrw.aspx?id=1635
dc.identifier.doi10.1016/j.cej.2015.02.013
dc.identifier.issn13858947
dc.identifier.issn18733212
dc.identifier.otherWOS;000362860100012
dc.identifier.otherSCOPUS;2-s2.0-84924169399
dc.identifier.urihttp://hdl.handle.net/10784/29369
dc.language.isoeng
dc.publisherELSEVIER SCIENCE SA
dc.relation.urihttps://www.scopus.com/inward/record.uri?eid=2-s2.0-84924169399&doi=10.1016%2fj.cej.2015.02.013&partnerID=40&md5=8908900075c4362b928bce017b4ef2a8
dc.rightshttps://v2.sherpa.ac.uk/id/publication/issn/1385-8947
dc.sourceCHEMICAL ENGINEERING JOURNAL
dc.subjectSO2 oxidationeng
dc.subjectAdiabatic reactoreng
dc.subjectMaxwell-Stefan diffusion modeleng
dc.subjectIndustrial reactoreng
dc.titleSimulation of an industrial adiabatic multi-bed catalytic reactor for sulfur dioxide oxidation using the Maxwell-Stefan modeleng
dc.typeinfo:eu-repo/semantics/articleeng
dc.typearticleeng
dc.typeinfo:eu-repo/semantics/publishedVersioneng
dc.typepublishedVersioneng
dc.type.localArtículospa

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