Mostrar el registro sencillo

dc.contributor.authorGuzmán, Hilmar
dc.contributor.authorAlbo Sánchez, Jonathan 
dc.contributor.authorIrabien Gulías, Ángel 
dc.contributor.authorCastellino, Micaela
dc.contributor.authorHernández, Simelys Pris
dc.contributor.otherUniversidad de Cantabriaes_ES
dc.date.accessioned2025-10-27T10:50:18Z
dc.date.available2025-10-27T10:50:18Z
dc.date.issued2024-12
dc.identifier.issn2730-7700
dc.identifier.otherTED2021-129810B-C21es_ES
dc.identifier.urihttps://hdl.handle.net/10902/37971
dc.description.abstractThis research is a significant step forward in understanding how the electrochemical cell setup influences CO2 conversion. The performance of Cu-Zn-Al metal oxide-based catalysts was compared in two reactor configurations: a gas diffusion electrode (GDE) cell with an aqueous electrolyte and a Membrane Electrode Assembly (MEA) cell operating in the gas phase without catholyte. The different operations induced significant morphological and crystalline structural changes, profoundly impacting the catalytic behaviour. The MEA configuration, for instance, led to the formation of a higher Cu0/Cu1+ ratio in the catalysts, promoting C-C coupling for C2H4 production. Conversely, the GDE operation favoured alcohol (ethanol and methanol) production by balancing copper oxidation states formed in situ in the presence of the aqueous catholyte. Zn and Al oxides also played a role in stabilising the resulting Cu species, some of which remained oxidised on the electrode surface. These findings underscore the crucial influence of varying cell operation conditions on catalyst reconstruction, shaping the quantity of Cu0 + Cu1+ species formed in situ to tailor catalyst selectivity.es_ES
dc.description.sponsorshipSH acknowledge the financial support received from Fondazione Compagnia di San Paolo through the project CO2Synthesis (ID ROL: 67910) funded in the Call Trapezio—Linea 1. J. A. fully acknowledge the financial support received from the Spanish State Research Agency (AEI) through the project TED2021-129810B-C21 (MCIN/AEI/https:// doi. org/ 10. 13039/ 50110 00110 33 and Union Europea Next Generation EU/PRTR).es_ES
dc.format.extent14 p.es_ES
dc.language.isoenges_ES
dc.publisherSpringeres_ES
dc.rightsAttribution 4.0 Internationales_ES
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/*
dc.sourceDiscover Chemical Engineering, 2024, 4(1), 12es_ES
dc.subject.otherCopper oxidees_ES
dc.subject.otherZinc oxidees_ES
dc.subject.otherAluminaes_ES
dc.subject.otherGas diffusion electrodees_ES
dc.subject.otherCatholyte-less conditionses_ES
dc.subject.otherCO dimerisationes_ES
dc.subject.otherC2+ productses_ES
dc.subject.otherElectrochemical CO2 reductiones_ES
dc.titleRole of electrochemical cell configuration on the selectivity of CuZnAl-oxide-based electrodes for the continuous CO2 conversion: aqueous electrolyte vs. catholyte-less configurationes_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.1007/s43938-024-00049-6
dc.type.versionpublishedVersiones_ES


Ficheros en el ítem

Thumbnail

Este ítem aparece en la(s) siguiente(s) colección(ones)

Mostrar el registro sencillo

Attribution 4.0 InternationalExcepto si se señala otra cosa, la licencia del ítem se describe como Attribution 4.0 International