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dc.creatorMuñoz Murillo, Araes
dc.creatorMartínez Tejada, Leidy Marcelaes
dc.creatorDomínguez Leal, María Isabeles
dc.creatorOdriozola Gordón, José Antonioes
dc.creatorCenteno Gallego, Miguel Ángeles
dc.date.accessioned2023-04-14T08:33:06Z
dc.date.available2023-04-14T08:33:06Z
dc.date.issued218
dc.identifier.citationMuñoz Murillo, A., Martínez Tejada, L.M., Domínguez Leal, M.I., Odriozola Gordón, J.A. y Centeno Gallego, M.Á. (218). Selective CO methanation with structured RuO2/Al2O3 catalysts. Applied Catalysis B: Environmental, 236, 420-427. https://doi.org/10.1016/j.apcatb.2018.05.020.
dc.identifier.issn0926-3373es
dc.identifier.issn1873-3883es
dc.identifier.urihttps://hdl.handle.net/11441/144357
dc.description.abstractActive and selective structured RuO2/Al2O3 catalysts for CO methanation using a flow simulating CO2-rich reformate gases from WGS and PROX units (H2 excess, CO2 presence and 300 ppm CO concentration) were prepared. Both, the RuO2/Al2O3 powder and the slurry prepared from it for its structuration by washcoating of the metallic micromonolithic structure, were also active and selective. Both the slurry (S-RuAl) and micro- monoliths (M-RuAl) were able to completely and selectively methanate CO at much lower temperatures than the parent RuAl powder. The optimal working temperature in which the CO conversion is maximum and the CO2 conversion is minimized was determined to be from 149 °C to 239 °C for S-RuAl and from 165 °C to 232 °C for M- RuAl, whilst it was from 217 °C to 226 °C for RuAl powder. TPR, XRD and TEM measurements confirmed that the changes in the activity and selectivity for CO methanation among the considered catalysts can be related with modifications in the surface particle size of ruthenium and its reducibility. These were ascribed to the metallic substrate, the presence of PVA and colloidal alumina in the slurry preparation, the aqueous and acidic media and the thermal treatment used, resulting in a more active and selective catalysts than the parent powder.es
dc.description.sponsorshipMinisterio de Economía y Competitividad de España y fondos europeos FEDER-ENE2012- 37431-C03-03es
dc.description.sponsorshipJunta de Andalucía-TEP-8196es
dc.formatapplication/mswordes
dc.format.extent8 p.es
dc.language.isoenges
dc.publisherElsevieres
dc.relation.ispartofApplied Catalysis B: Environmental, 236, 420-427.
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internacional*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.subjectRuO2/Al2O3es
dc.subjectFecralloy micromonolithes
dc.subjectCO and CO2 methanationes
dc.titleSelective CO methanation with structured RuO2/Al2O3 catalystses
dc.typeinfo:eu-repo/semantics/articlees
dcterms.identifierhttps://ror.org/03yxnpp24
dc.type.versioninfo:eu-repo/semantics/acceptedVersiones
dc.rights.accessRightsinfo:eu-repo/semantics/openAccesses
dc.contributor.affiliationUniversidad de Sevilla. Departamento de Química Inorgánicaes
dc.relation.projectIDENE2012- 37431-C03-03es
dc.relation.projectIDTEP-8196es
dc.relation.publisherversionhttps://doi.org/10.1016/j.apcatb.2018.05.020es
dc.identifier.doi10.1016/j.apcatb.2018.05.020es
dc.journaltitleApplied Catalysis B: Environmentales
dc.publication.volumen236es
dc.publication.initialPage420es
dc.publication.endPage427es
dc.contributor.funderMinisterio de Economía y Competitividad (MINECO). Españaes
dc.contributor.funderEuropean Commission (EC). Fondo Europeo de Desarrollo Regional (FEDER)es
dc.contributor.funderJunta de Andalucíaes

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