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dc.creatorUriz, I.es
dc.creatorArzamendi, Gurutzees
dc.creatorDiéguez, P. M.es
dc.creatorLaguna Espitia, Oscar Hernandoes
dc.creatorCenteno Gallego, Miguel Ángeles
dc.creatorOdriozola Gordón, José Antonioes
dc.creatorGandía, L. M.es
dc.date.accessioned2018-02-19T14:51:16Z
dc.date.available2018-02-19T14:51:16Z
dc.date.issued2013
dc.identifier.citationUriz, I., Arzamendi, G., Diéguez, P.M., Laguna Espitia, O.H., Centeno Gallego, M.Á., Odriozola Gordón, J.A. y Gandía, L.M. (2013). Preferential oxidation of CO over Au/CuOx-CeO2 catalyst in microstructured reactors studied through CFD simulations. Catalysis Today, 216, 283-291.
dc.identifier.issn0920-5861es
dc.identifier.urihttps://hdl.handle.net/11441/70418
dc.description.abstractA computational fluid dynamics (CFD) simulation study of the preferential oxidation of CO (CO-PROX) in microstructured reactors consisting in square and semicircular microchannels coated with anAu/CuOx¿CeO2catalyst is presented. The CO content of the feed stream was set at 1 vol.%. A parametricsensitivity analysis has been performed under isothermal conditions revealing that an optimal reactiontemperature exists that leads to a minimum CO content at the microreactor exit. The influence of thespace velocity, CO2concentration and oxygen-to-CO molar ratio in the feed stream (), catalyst loading,and microchannel characteristic dimension (d) on the microreactor performance has been investigated.Under suitable conditions, the CO concentration can be reduced below 10 ppm at relatively low tem-peratures within the 155¿175¿C range. A negative effect of the increase of d from 0.35 mm to 2.8 mmon the CO removal efficiency has been found and attributed to a more detrimental effect of the masstransport limitations on the oxidation of CO than that of H2. Non-isothermal CFD simulations have beenperformed to investigate the cooling of the CO-PROX reactor with air or a fuel cell anode off gas surrogatein parallel microchannels. Due to the very rapid heat transfer allowed by the microreactor and the stronginfluence of the reaction temperature on the exit CO concentration, a careful control of the coolant flowrate and inlet temperature is required for proper reactor operation. The microreactor behavior is virtuallyisothermal.es
dc.description.sponsorshipMinisterio de Ciencia e Innovación ENE2009-14522-C04es
dc.description.sponsorshipMinisterio de Economía y Competitividad ENE2012-37431-C03es
dc.formatapplication/pdfes
dc.language.isoenges
dc.publisherElsevieres
dc.relation.ispartofCatalysis Today, 216, 283-291.
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internacional*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.subjectCatalytic wall reactores
dc.subjectCO preferential oxidation (CO-PROX)es
dc.subjectComputational fluid dynamics (CFD)es
dc.subjectMicroreactores
dc.subjectMicrostructured reactores
dc.titlePreferential oxidation of CO over Au/CuOx-CeO2 catalyst in microstructured reactors studied through CFD simulationses
dc.typeinfo:eu-repo/semantics/articlees
dcterms.identifierhttps://ror.org/03yxnpp24
dc.type.versioninfo:eu-repo/semantics/submittedVersiones
dc.rights.accessRightsinfo:eu-repo/semantics/openAccesses
dc.relation.projectIDENE2009-14522-C04es
dc.relation.projectIDENE2012-37431-C03es
dc.relation.publisherversionhttp://dx.doi.org/10.1016/j.cattod.2013.04.023es
dc.identifier.doi10.1016/j.cattod.2013.04.023es
idus.format.extent27 p.es
dc.journaltitleCatalysis Todayes
dc.publication.volumen216es
dc.publication.initialPage283es
dc.publication.endPage291es
dc.contributor.funderMinisterio de Ciencia e Innovación (MICIN). España
dc.contributor.funderMinisterio de Economía y Competitividad (MINECO). España

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