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dc.contributor.author
Martínez Figueredo, Karla Geraldine

dc.contributor.author
Virgilio, Emanuel Martin

dc.contributor.author
Segobia, Dario Jobino

dc.contributor.author
Bertero, Nicolas Maximiliano

dc.date.available
2023-10-04T18:38:17Z
dc.date.issued
2022-06
dc.identifier.citation
Martínez Figueredo, Karla Geraldine; Virgilio, Emanuel Martin; Segobia, Dario Jobino; Bertero, Nicolas Maximiliano; Production of pentyl valerate from γ-valerolactone, pentanol and H2 using Pd and Rh-based bifunctional catalysts; Royal Society of Chemistry; Reaction Chemistry and Engineering; 7; 9; 6-2022; 1997-2008
dc.identifier.uri
http://hdl.handle.net/11336/214139
dc.description.abstract
The production of pentyl valerate (PV) from γ-valerolactone (GVL) in the liquid phase in the presence of pentanol and H2 over Rh and Pd-based catalysts, using SiO2-Al2O3 (SA) as a support, was studied in this work. Both catalysts had metal loadings lower than 1 wt% and were prepared by incipient wetness impregnation using chlorinated metal precursors. The M0/SA catalysts exhibited a specific surface area and pore volume slightly lower than those of the SA support and the presence of metal nanoparticles with an average size of 5.6 nm for Rh/SA and 3.7 nm for Pd/SA. A total acid site density 10% lower than that of SA was determined for Rh/SA, whereas a value 45% higher was observed for Pd/SA. The relative strength of acid sites followed the pattern: Pd/SA > Rh/SA > SA with mainly Lewis acid sites in all the cases. Pd/SA showed a higher activity, selectivity to PV and carbon balance than Rh/SA. These results indicate that both a relatively high acid site density and smaller metal particles promote the conversion of adsorbed intermediates, reaching a GVL conversion of 81.1% and a PV yield of 70.1% over Pd/SA after 8 h. Therefore, PV productivity values 25% and 120% higher than the best reported value were reached over Rh/SA and Pd/SA, respectively, showing the potential of these catalysts to convert GVL into biofuels for transportation purposes. Finally, with Pd/SA, the apparent activation energy was equal to 25.6 kcal mol−1, the reaction order for H2 was about zero and a unitary reaction order for GVL was determined.
dc.format
application/pdf
dc.language.iso
eng
dc.publisher
Royal Society of Chemistry

dc.rights
info:eu-repo/semantics/openAccess
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.subject
PENTYL VALERATE
dc.subject
BIOFUEL
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GAMMA-VALEROLACTONE
dc.subject
BIOMASS
dc.subject
Pd AND Rh-BASED CATALYSTS
dc.subject
ONE-POT PROCESS
dc.subject.classification
Ingeniería de Procesos Químicos

dc.subject.classification
Ingeniería Química

dc.subject.classification
INGENIERÍAS Y TECNOLOGÍAS

dc.title
Production of pentyl valerate from γ-valerolactone, pentanol and H2 using Pd and Rh-based bifunctional catalysts
dc.type
info:eu-repo/semantics/article
dc.type
info:ar-repo/semantics/artículo
dc.type
info:eu-repo/semantics/publishedVersion
dc.date.updated
2023-07-07T21:01:15Z
dc.identifier.eissn
2058-9883
dc.journal.volume
7
dc.journal.number
9
dc.journal.pagination
1997-2008
dc.journal.pais
Reino Unido

dc.journal.ciudad
Londres
dc.description.fil
Fil: Martínez Figueredo, Karla Geraldine. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; Argentina
dc.description.fil
Fil: Virgilio, Emanuel Martin. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; Argentina
dc.description.fil
Fil: Segobia, Dario Jobino. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; Argentina
dc.description.fil
Fil: Bertero, Nicolas Maximiliano. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; Argentina
dc.journal.title
Reaction Chemistry and Engineering
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/url/https://pubs.rsc.org/en/content/articlelanding/2022/RE/D2RE00121G
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1039/d2re00121g
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