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dc.contributor.authorJiménez-Gómez, Carmen Pilar
dc.contributor.authorCecilia-Buenestado, Juan Antonio 
dc.contributor.authorAlba Rubio, Ana Carolina
dc.contributor.authorCassidy, Andrea
dc.contributor.authorMoreno-Tost, Ramón 
dc.contributor.authorGarcía-Sancho, Cristina 
dc.contributor.authorMaireles-Torres, Pedro Jesús 
dc.date.accessioned2022-03-23T08:19:19Z
dc.date.available2022-03-23T08:19:19Z
dc.date.created2022
dc.date.issued2022
dc.identifier.citationJiménez-Gómez, C.P. et al. (2022) “Tailoring the selectivity of Cu-based catalysts in the furfural hydrogenation reaction: Influence of the morphology of the silica support,” Fuel, 319, p. 123827. doi:https://doi.org/10.1016/j.fuel.2022.123827.es_ES
dc.identifier.urihttps://hdl.handle.net/10630/23888
dc.description.abstractCu nanoparticles were incorporated on different porous silica supports (commercial silica, SBA-15 synthesized both at room temperature and under hydrothermal conditions, and mesocellular foam) by the strong electrostatic adsorption method and tested in the gas-phase furfural hydrogenation for the production of furfuryl alcohol and 2-methylfuran, being the latter a promising biofuel. The incorporated copper species provided metal particle sizes lower than 5 nm in all cases. However, different catalytic behaviors, both in terms of conversion and selectivity, were detected due to the morphology and textural properties of each support. Cu over commercial silica was more prone to suffer from deactivation, and it provided higher furfuryl alcohol yields, probably due to its higher acidity and lower metallic surface area. On the other hand, the agglomeration of Cu nanoparticles together with larger pore sizes complicated the access of furfural to the active sites using the hydrothermal SBA- 15 support, thus decreasing the activity. In contrast, the addition of fluoride in the synthesis of mesoporous silica, which shortened the length of the silica channels (mesocellular foam), facilitated the furfural access and provided both higher metallic surface area and lower acidity. This fact led to a more gradual deactivation, still attaining high values of furfural conversion and 2-methylfuran yield (95 and 76%, respectively) after 5 h at 190 ◦C. However, Cu over mesocellular foam changed its selectivity pattern along 48 h and after regeneration, increasing the furfuryl alcohol selectivity due to the decreased number of available active sites.es_ES
dc.language.isoenges_ES
dc.publisherElsevieres_ES
dc.rightsinfo:eu-repo/semantics/openAccesses_ES
dc.subjectCatalizadores metálicoses_ES
dc.subject.other2-Methylfuranes_ES
dc.subject.otherFurfurales_ES
dc.subject.otherHydrogenationes_ES
dc.subject.otherMesoporous silicaes_ES
dc.subject.otherCu-based catalystses_ES
dc.subject.otherStrong Electrostatic Adsorptiones_ES
dc.titleTailoring the selectivity of Cu-based catalysts in the furfural hydrogenation reaction: Influence of the morphology of the silica supportes_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.centroFacultad de Cienciases_ES
dc.identifier.doihttps://doi.org/10.1016/j.fuel.2022.123827
dc.type.hasVersioninfo:eu-repo/semantics/publishedVersiones_ES


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