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dc.contributor.authorReynoso Estévez, Alberto José ORCID
dc.contributor.authorAyastuy Arizti, José Luis ORCID
dc.contributor.authorIriarte Velasco, Unai
dc.contributor.authorGutiérrez Ortiz, Miguel Angel
dc.date.accessioned2023-12-29T11:51:45Z
dc.date.available2023-12-29T11:51:45Z
dc.date.issued2018-08-02
dc.identifier.citationApplied Catalysis B: Environmental 239 : 86-101(2018)es_ES
dc.identifier.issn0926-3373
dc.identifier.issn1873-3883 (electronic)
dc.identifier.urihttp://hdl.handle.net/10810/63725
dc.description.abstractCatalytic activity at mild (235 °C/3.5 MPa) and severe (260 °C/5.0 MPa) APR conditions was investigated over catalysts based on cobalt aluminate spinel synthetized by coprecipitation. Co/Al ratio was varied and physicochemical characteristics were assessed by N2 adsorption, H2 chemisorption, XRD, H2-TPR, DRS-UV, FTIR, CO2-TPD, NH3-TPD and XPS. Formation of cobalt aluminate produced strong Co-O-Al interaction in the catalyst precursor leading to improved Co dispersion upon activation. Co/Al ratio could be used to tune catalyst characteristics, thus selectivity towards the desired reaction pathway. Overall, Co/Al above the stoichiometric value produced smaller and more stable metallic Co, which allowed best APR performance. For instance, at 235 °C/3.5 MPa glycerol conversion and conversion to gas of 0.625CoAl (88% and 22%) were notably higher than those of bare Co3O4 (23% and 5%). At severe conditions, 0.625CoAl catalyst produced 231 μmolH2/gcat min (60% H2). Statistical analysis of data collected from long-term run was used to investigate reaction mechanism. Long-term run revealed that sintering and oxidation were main mechanisms for catalyst deactivation whereas some leaching of Co nanoparticles, and carbonaceous deposition was also detected.es_ES
dc.description.sponsorshipMinisterio de Economía y Competitividad, ENE2016-7450-Res_ES
dc.language.isoenges_ES
dc.publisherElsevieres_ES
dc.relationinfo:eu-repo/grantAgreement/MINECO/ENE2016-7450-Res_ES
dc.rightsinfo:eu-repo/semantics/openAccesses_ES
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es/*
dc.subjectcobalt aluminatees_ES
dc.subjectspineles_ES
dc.subjectaqueous phase reforminges_ES
dc.subjectglyceroles_ES
dc.subjecthydrogenes_ES
dc.titleCobalt aluminate spinel-derived catalysts for glycerol aqueous phase reforminges_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.rights.holderAtribución-NoComercial-SinDerivadas 3.0 Españaes_ES
dc.relation.publisherversionhttps://doi.org/10.1016/j.apcatb.2018.08.001es_ES
dc.identifier.doi10.1016/j.apcatb.2018.08.001
dc.departamentoesIngeniería químicaes_ES
dc.departamentoeuIngeniaritza kimikoaes_ES


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Atribución-NoComercial-SinDerivadas 3.0 España
Except where otherwise noted, this item's license is described as Atribución-NoComercial-SinDerivadas 3.0 España