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dc.contributor.authorDíaz Sainz, Guillermo 
dc.contributor.authorÁlvarez Guerra, Manuel 
dc.contributor.authorÁvila Bolívar, Beatriz
dc.contributor.authorSolla Gullón, José
dc.contributor.authorMontiel Leguey, Vicente
dc.contributor.authorIrabien Gulías, Ángel 
dc.contributor.otherUniversidad de Cantabriaes_ES
dc.date.accessioned2020-09-30T14:21:25Z
dc.date.available2023-02-28T00:17:35Z
dc.date.issued2021-02-01
dc.identifier.issn1385-8947
dc.identifier.issn1873-3212
dc.identifier.otherCTQ2016-76231-C2-1-Res_ES
dc.identifier.otherCTQ2016-76231-C2-2-Res_ES
dc.identifier.urihttp://hdl.handle.net/10902/19249
dc.description.abstractThe electrochemical conversion of CO2 is gaining increasing attention because it could be considered as an appealing strategy for making value-added products at mild conditions from CO2 captured. In this work, we report a process for the electrocatalytic reduction of CO2 to formate (HCOO-) operating in a continuous way, employing a single pass of the reactants through the electrochemical reactor and using Bi carbon supported nanoparticles in the form of a membrane electrode assembly composed by a Gas Diffusion Electrode, a current collector and a cationic exchange membrane. This contribution presents the best trade-off between HCOO- concentration, Faradaic Efficiency and energy consumption in the literature. We also show noteworthy values of energy consumption required of only 180 kWh·kmol-1 of HCOO-, lower than previous approaches, working at current densities that allow achieving formate concentration higher than 300 g·L-1 and simultaneously, a Faradaic Efficiency close to 90%. The results here displayed make the electrochemical approach closer for future implementation at the industrial scale.es_ES
dc.description.sponsorshipThe authors of this work would like to acknowledge to the financial support from the MINECO, through the projects CTQ2016-76231-C2-1-R and CTQ2016-76231-C2-2-R (AEI/FEDER, UE). J.S.G acknowledges financial support from VITC (Vicerrectorado de Investigación y Transferencia de Conocimiento) of the University of Alicante (UTALENTO16-02). G.D.S, M.A.G and A.I filed a patent application on the experimental reaction system discussed here.es_ES
dc.format.extent28 p.es_ES
dc.language.isoenges_ES
dc.publisherElsevieres_ES
dc.rights© 2020. This manuscript version is made available under the CC-BY-NC-ND 4.0 licensees_ES
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.sourceChemical Engineering Journal, 2021, 405, 126965es_ES
dc.subject.otherCO2 electroreductiones_ES
dc.subject.otherFormatees_ES
dc.subject.otherBismuth electrocatalystses_ES
dc.subject.otherGas Diffusion Electrode (GDE)es_ES
dc.subject.otherMembrane electrode assembly (MEA)es_ES
dc.subject.otherElectrochemical filter press reactores_ES
dc.titleImproving trade-offs in the figures of merit of gas-phase single-pass continuous CO2 electrocatalytic reduction to formatees_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.relation.publisherVersionhttps://doi.org/10.1016/j.cej.2020.126965es_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.1016/j.cej.2020.126965
dc.type.versionacceptedVersiones_ES


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© 2020. This manuscript version is made available under the CC-BY-NC-ND 4.0 licenseExcepto si se señala otra cosa, la licencia del ítem se describe como © 2020. This manuscript version is made available under the CC-BY-NC-ND 4.0 license