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Minimizing Energy Demand in the Conversion of LevulinicAcid to ‑Valerolactone via Photothermal Catalysis UsingRaney Ni

dc.contributor.authorBujaldón Carbó, Roger
dc.contributor.authorFons, Arnau
dc.contributor.authorGarcia-Amorós, Jaume
dc.contributor.authorVaca, Cristina
dc.contributor.authorNogués, Josep
dc.contributor.authorEsplandiu, María J.
dc.contributor.authorGómez, Elvira
dc.contributor.authorSepúlveda, Borja
dc.contributor.authorSerrà i Ramos, Albert
dc.date.accessioned2025-04-23T15:40:02Z
dc.date.available2025-04-23T15:40:02Z
dc.date.issued2025-04-17
dc.date.updated2025-04-23T15:40:02Z
dc.description.abstractThe valorization of lignocellulosic wastes emerges as a prime strategy tomitigate the global carbon footprint. Among the multiple biomass derivatives, -valerolactone is particularly attractive as precursor of high-value chemicals,biofuel, green solvent or perfumery. -Valerolactone can be synthesizedthrough a hydrogenation reaction from levulinic acid, obtained from cellulose.However, the high energy requirements of this synthetic pathway havehindered its industrial viability. To drastically reduce the reaction energyrequirements, here a novel synthetic strategy, based onsolvothermal-photothermal processes using cost-effective Raney-Ni asphotothermal catalyst, is proposed. First, the use of hydrogen gas is avoidedby selecting isopropanol as a safer and greener H-source. Second, aphotothermocatalytic process is used to minimize the reaction temperatureand time with respect to conventional reactions. This approach exploits thebroadband optical absorption of the Raney®-Ni, due to its highly dampedplasmonic behavior, to achieve fast and efficient catalyst heating inside thereactor. The photothermal reaction required less than 2 h and just 132 °C toreach over 95% conversion, thereby drastically reducing the reaction time andenergy consumption compared to conventional reactions. Importantly, theseconditions granted high catalyst reusability. This solvothermal-photothermalapproach could offer a sustainable alternative for the industrial production of -valerolactone.
dc.format.extent1 p.
dc.format.mimetypeapplication/pdf
dc.identifier.idgrec758166
dc.identifier.issn2198-3844
dc.identifier.urihttps://hdl.handle.net/2445/220552
dc.language.isoeng
dc.publisherWiley-VCH Verlag
dc.relation.isformatofReproducció del document publicat a: https://doi.org/DOI: 10.1002/advs.202416153
dc.relation.ispartofAdvanced Science, 2025, num.2416153
dc.relation.urihttps://doi.org/DOI: 10.1002/advs.202416153
dc.rightscc-by (c) Bujaldón, R. et al., 2025
dc.rights.accessRightsinfo:eu-repo/semantics/openAccess
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/
dc.sourceArticles publicats en revistes (Ciència dels Materials i Química Física)
dc.subject.classificationCatàlisi
dc.subject.classificationNíquel
dc.subject.classificationBiomassa
dc.subject.otherCatalysis
dc.subject.otherNickel
dc.subject.otherBiomass
dc.titleMinimizing Energy Demand in the Conversion of LevulinicAcid to ‑Valerolactone via Photothermal Catalysis UsingRaney Ni
dc.typeinfo:eu-repo/semantics/article
dc.typeinfo:eu-repo/semantics/publishedVersion

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