Modification of Sepiolite for Its Catalytic Upgrading in the Hydrogenation of Furfural
| dc.centro | Facultad de Ciencias | es_ES |
| dc.contributor.author | Guerrero-Torres, Antonio | |
| dc.contributor.author | Maderuelo-Solera, Rocío | |
| dc.contributor.author | García-Sancho, Cristina | |
| dc.contributor.author | Quirante-Sánchez, José Joaquín | |
| dc.contributor.author | Moreno-Tost, Ramón | |
| dc.contributor.author | Maireles-Torres, Pedro Jesús | |
| dc.contributor.author | Cecilia-Buenestado, Juan Antonio | |
| dc.date.accessioned | 2025-10-17T10:44:00Z | |
| dc.date.available | 2025-10-17T10:44:00Z | |
| dc.date.issued | 2025 | |
| dc.departamento | Química Física | es_ES |
| dc.departamento | Química Inorgánica, Cristalografía y Mineralografía | es_ES |
| dc.description.abstract | In this work, a new methodology for dispersing metal particles supported in clay has been described. For this purpose, a sepiolite has been modified by a microwave-assisted treatment to increase the surface area and pore volume due to the progressive leaching of the Mg2+-species located in the octahedral sheet. These materials have been used as support to incorporate Cu species on the surface by a precipitation-deposition process from the thermal decomposition of urea at 95 °C. Once calcined and reduced, the Cu-based catalysts showed a Cu0-particle size lower than 5 nm in the case of catalysts whose support is a sepiolite subjected to acid treatment. On the other hand, when raw sepiolite is used as a support, the Cu0-crystal size is much larger (15–20 nm). This difference in Cu0-crystal size showed a variable catalytic behavior for the hydrogenation reaction of furfural in gas-phase. Catalysts with larger particle size promote the hydrogenation reaction, obtaining a yield towards furfuryl alcohol close to 60% after 5 h at 190 °C. In contrast, catalysts with smaller particle size promote the hydrogenation reaction and subsequently the hydrogenolysis reaction, obtaining methylfuran as a product with a yield of 58% after 1 h of reaction at 190 °C; however, the sites where hydrogenolysis are involved are more prone to be deactivated. | es_ES |
| dc.identifier.citation | Guerrero-Torres, A.; Maderuelo-Solera, R.; García-Sancho, C.; Quirante-Sánchez, J.J.; Moreno-Tost, R.; Maireles-Torres, P.J.; Cecilia, J.A. Modification of Sepiolite for Its Catalytic Upgrading in the Hydrogenation of Furfural. Ceramics 2025, 8, 21. https://doi.org/10.3390/ceramics8010021 | es_ES |
| dc.identifier.doi | 10.3390/ceramics8010021 | |
| dc.identifier.uri | https://hdl.handle.net/10630/40299 | |
| dc.language.iso | eng | es_ES |
| dc.publisher | MDPI | es_ES |
| dc.rights.accessRights | open access | es_ES |
| dc.subject | Sepiolita | es_ES |
| dc.subject.other | Cu-based catalysts | es_ES |
| dc.subject.other | Sepiolite | es_ES |
| dc.subject.other | Acid Treatment | es_ES |
| dc.subject.other | Furfural Hydrogenation | es_ES |
| dc.subject.other | Furfuryl Alcohol | es_ES |
| dc.subject.other | 2-Methylfuran | es_ES |
| dc.title | Modification of Sepiolite for Its Catalytic Upgrading in the Hydrogenation of Furfural | es_ES |
| dc.type | journal article | es_ES |
| dc.type.hasVersion | VoR | es_ES |
| dspace.entity.type | Publication | |
| relation.isAuthorOfPublication | 1795b56c-12cc-4e3c-944b-d9597623a70e | |
| relation.isAuthorOfPublication | d28727a2-e60b-4d59-8eec-17f8d0f92a50 | |
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| relation.isAuthorOfPublication | d40b59f8-1061-40c5-a3cc-bb854403414f | |
| relation.isAuthorOfPublication.latestForDiscovery | 1795b56c-12cc-4e3c-944b-d9597623a70e |
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