dc.contributor.author | Díaz Sainz, Guillermo | |
dc.contributor.author | Álvarez Guerra, Manuel | |
dc.contributor.author | Solla Gullón, José | |
dc.contributor.author | García Cruz, Leticia | |
dc.contributor.author | Montiel Leguey, Vicente | |
dc.contributor.author | Irabien Gulías, Ángel | |
dc.contributor.other | Universidad de Cantabria | es_ES |
dc.date.accessioned | 2020-09-28T13:40:14Z | |
dc.date.available | 2021-09-30T02:45:18Z | |
dc.date.issued | 2020-09 | |
dc.identifier.issn | 0001-1541 | |
dc.identifier.issn | 1547-5905 | |
dc.identifier.other | CTQ2016-76231-C2-1-R | es_ES |
dc.identifier.other | CTQ2016-76231-C2-2-R | es_ES |
dc.identifier.uri | http://hdl.handle.net/10902/19205 | |
dc.description.abstract | The use of bismuth-based catalysts is promising for formate production by the electroreduction of CO2 captured from waste streams. However, compared to the extensive research on catalysts, only a few studies have focused on electrochemical reactor performance. Hence, this work studied a continuous-mode gas-liquid-solid reaction system for investigating CO2 electroreduction to formate using Bi-catalyst-coated membrane electrodes as cathodes. The experimental setup was designed to analyze products obtained in both liquid and gas phases. The influence of relevant variables (e.g., temperature and input water flow) was analyzed, with the thickness of the liquid film formed over the cathode surface being a key parameter affecting system performance. Promising results, including a high formate concentration of 34 g/L with faradaic efficiency for formate of 72%, were achieved. | es_ES |
dc.description.sponsorship | Ministerio de Economía y Competitividad (MINECO) through the projects, Grant/Award Numbers: CTQ2016‐76231‐C2‐1‐R, CTQ2016‐76231‐C2‐2‐R (AEI/FEDER, UE).; Vicerrectorado de Investigación y Transferencia de Conocimiento (VITC) of the; University of Alicante, Grant/Award Number: (UTALENTO16‐02). | es_ES |
dc.format.extent | 46 p. | es_ES |
dc.language.iso | eng | es_ES |
dc.publisher | American Institute of Chemical Engineers | es_ES |
dc.rights | © American Institute of Chemical Engineers. Published by Wiley. This is the peer reviewed version of the following article: Díaz-Sainz, G, Alvarez-Guerra, M, Solla-Gullón, J, García-Cruz, L, Montiel, V, Irabien, A. Gas-liquid-solid reaction system for CO2 electroreduction to formate without using supporting electrolyte. AIChE J. 2020; 66:e16299, which has been published in final form at https://doi.org/10.1002/aic.16299. This article may be used for non-commercial purposes in accordance with Wiley Terms and Conditions for Self-Archiving. | es_ES |
dc.source | AIChE Journal, 2020, 66(9), e16299 | es_ES |
dc.subject.other | Bismuth | es_ES |
dc.subject.other | CCMEs | es_ES |
dc.subject.other | CO2 electroreduction | es_ES |
dc.subject.other | Formate | es_ES |
dc.subject.other | G–L–S reaction system | es_ES |
dc.title | Gas-liquid-solid reaction system for CO2 electroreduction to formate without using supporting electrolyte | es_ES |
dc.type | info:eu-repo/semantics/article | es_ES |
dc.relation.publisherVersion | https://doi.org/10.1002/aic.16299 | es_ES |
dc.rights.accessRights | openAccess | es_ES |
dc.identifier.DOI | 10.1002/aic.16299 | |
dc.type.version | acceptedVersion | es_ES |