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dc.contributor.authorGallego Villada, Luis Alfonso-
dc.contributor.authorAlarcón Durango, Edwin Alexis-
dc.contributor.authorSathicq, Ángel G.-
dc.contributor.authorRomanelli, Gustavo P.-
dc.date.accessioned2024-06-16T18:56:59Z-
dc.date.available2024-06-16T18:56:59Z-
dc.date.issued2024-
dc.identifier.citationGallego-Villada, L.A., Alarcón, E.A., Sathicq, Á.G. et al. Kinetic modeling of microwave-assisted esterification for biofuel additive production: conversion of levulinic acid with pentanol using Dowex® 50WX8 catalyst. Reac Kinet Mech Cat (2024). https://doi.org/10.1007/s11144-024-02657-3spa
dc.identifier.issn1878-5190-
dc.identifier.urihttps://hdl.handle.net/10495/40065-
dc.description.abstractABSTRACT: This study explores the esterifcation of levulinic acid with 1-pentanol, employing Dowex® 50WX8 as a catalyst under microwave irradiation. Key parameters such as the pentanol/acid molar ratio, temperature, and catalyst loading were evaluated and utilized for kinetic modeling. The kinetic behavior of the reaction was investigated using a dual-model approach: a pseudo-homogeneous model to account for the microwave efect and catalytic contributions modeled through LHHW and Eley–Rideal mechanisms. The best model was chosen based on statistical results obtained from Markov Chain Monte Carlo (MCMC) analysis, which involved an LHHW model with the surface reaction as the limiting step, resulting in an activa- tion energy of 50.6 kJ mol−1 for the catalytic synthesis of pentyl levulinate. The role of the alcohol in the esterifcation route was explained, and catalytic stability was confrmed, with the catalyst maintaining activity over multiple cycles. The absence of mass transfer limitations was proved using the Weisz–Prater criterion. A plausible reaction pathway was proposed for the levulinic acid esterifcation over the 50WX8 catalyst.spa
dc.format.extent23 páginasspa
dc.format.mimetypeapplication/pdfspa
dc.language.isoengspa
dc.publisherSpringerspa
dc.publisherAkadémiai Kiadóspa
dc.type.hasversioninfo:eu-repo/semantics/publishedVersionspa
dc.rightsinfo:eu-repo/semantics/openAccessspa
dc.rights.urihttp://creativecommons.org/licenses/by/2.5/co/*
dc.titleKinetic modeling of microwave‑assisted esterification for biofuel additive production: conversion of levulinic acid with pentanol using Dowex® 50WX8 catalystspa
dc.typeinfo:eu-repo/semantics/articlespa
dc.publisher.groupCatálisis Ambientalspa
dc.identifier.doi10.1007/s11144-024-02657-3-
oaire.versionhttp://purl.org/coar/version/c_970fb48d4fbd8a85spa
dc.rights.accessrightshttp://purl.org/coar/access_right/c_abf2spa
dc.identifier.eissn1878-5204-
oaire.citationtitleReaction Kinetics, Mechanisms and Catalysisspa
oaire.citationstartpage1spa
oaire.citationendpage23spa
dc.rights.creativecommonshttps://creativecommons.org/licenses/by/4.0/spa
dc.publisher.placePaíses Bajosspa
dc.type.coarhttp://purl.org/coar/resource_type/c_2df8fbb1spa
dc.type.redcolhttps://purl.org/redcol/resource_type/ARTspa
dc.type.localArtículo de investigaciónspa
dc.subject.decsCinética-
dc.subject.decsKinetics-
dc.subject.lembMétodo de Montecarlo-
dc.subject.lembMonte carlo method-
dc.subject.agrovocÁcido levulínico-
dc.subject.agrovocLevulinic acid-
dc.subject.proposalDowex® 50WX8spa
dc.subject.agrovocurihttp://aims.fao.org/aos/agrovoc/c_4302-
dc.description.researchgroupidCOL0001941spa
dc.subject.meshurihttps://id.nlm.nih.gov/mesh/D007700-
dc.relation.ispartofjournalabbrevReac. Kinet. Mech. Cat.spa
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