Assessing the activity and stability of Cu2O/SnO2-based gas diffusion electrodes for the CO2 conversion in different electrolytes: Bicarbonate vs. Ionic Liquid/Acetonitrile

• CO 2 electroreduction in aqueous medium was assessed up to 24 h in a 10.2 cm 2 flow cell. • Cu-based GDE stably produced CO over 84 % of Faradaic efficiency in KHCO 3 electrolyte up to 100 mA cm −2 . • Cu-based GDE is electrochemically unstable in IL-ACN electrolyte. • A maximum CO/H 2 ratio >3 was reached with 0.3 M [BMIM][TfO] in acetonitrile. • Ab initio molecular dynamics show a strong Cu-ACN affinity, with Cu dissolution stabilised by the triflate anion in the IL. Gas diffusion electrodes (GDEs) are key components for enabling the deployment of electrochemical CO 2 conversion on a large scale. Most studies focused on optimising the GDEs’ performance in aqueous electrolytes, while their use with non-conventional electrolytes integrating CO 2 capture and co-catalytic conversion abilities is missing in the literature. Herein, the performance of a newly designed Cu 2 O/SnO 2 -based GDE was investigated for the first time in a continuous-feed flow cell at a 10.2 cm 2 scale, both in an aqueous KHCO 3 medium and in a binary ionic liquid-organic solvent solution. Outstanding catalyst stability and selectivity, i.e. Faradaic efficiency to CO (FE CO ) from 84 to 90 % in the aqueous electrolyte, was demonstrated at current densities between −20 and −100 mA cm −2 , establishing a benchmark for the CO 2 reduction to CO on a Cu-based GDE. In comparison, a FE CO of 35 % (CO/H 2 ratio > 3) was reached at –20 mA cm −2 with 1-Butyl-3-methylimidazolium triflate ([BMIM][TfO]) in acetonitrile (ACN). Still, stability issues and a performance drop were faced during operation in this aprotic media. Molecular dynamics simulations and ex-situ physical–chemical characterisation assessed that the changes in the catalyst/GDE structure and electrolyte properties started with the displacement of Cu surface atoms from their equilibrium position by ACN molecules, which promotes the subsequent dissolution of Cu in the presence of [BMIM][TfO] molecules. Our findings highlight the significant influence of electrolyte composition on catalyst surface transformation and performance during the reaction. This work unveils critical issues for the practical application of IL-based electrolytes as co-catalysts and CO 2 capture media for CO 2 electrochemical conversion systems and proposes some mitigation strategies.

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Journal
Chemical Engineering Journal
Published
2025-05-01
DOI
https://doi.org/10.1016/j.cej.2025.163265
Citations
1
Primary Topic
CO2 Reduction Techniques and Catalysts
Type
article
Field-Weighted Citation Impact
0.36
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article

Assessing the activity and stability of Cu2O/SnO2-based gas diffusion electrodes for the CO2 conversion in different electrolytes: Bicarbonate vs. Ionic Liquid/Acetonitrile

Hilmar Guzmán, Elena Simone, Simelys Hernández, Alberto Lopera et al.
1 citations
Chemical Engineering Journal
CO2 Reduction Techniques and Catalysts
0.36
article

Assessing the activity and stability of Cu2O/SnO2-based gas diffusion electrodes for the CO2 conversion in different electrolytes: Bicarbonate vs. Ionic Liquid/Acetonitrile

Hilmar Guzmán, Elena Simone, Simelys Hernández, Alberto Lopera, Federica Zammillo, Daniela Polino, Nunzio Russo, Giovanni Maria Pavan, Roger Miró, Maddalena Zoli, Miriam Díaz de los Bernardos, Emmanuele Parisi, Alessia Fortunati, Mariajose López-Tendero
article en
1 citations

Abstract

• CO 2 electroreduction in aqueous medium was assessed up to 24 h in a 10.2 cm 2 flow cell. • Cu-based GDE stably produced CO over 84 % of Faradaic efficiency in KHCO 3 electrolyte up to 100 mA cm −2 . • Cu-based GDE is electrochemically unstable in IL-ACN electrolyte. • A maximum CO/H 2 ratio >3 was reached with 0.3 M [BMIM][TfO] in acetonitrile. • Ab initio molecular dynamics show a strong Cu-ACN affinity, with Cu dissolution stabilised by the triflate anion in the IL. Gas diffusion electrodes (GDEs) are key components for enabling the deployment of electrochemical CO 2 conversion on a large scale. Most studies focused on optimising the GDEs’ performance in aqueous electrolytes, while their use with non-conventional electrolytes integrating CO 2 capture and co-catalytic conversion abilities is missing in the literature. Herein, the performance of a newly designed Cu 2 O/SnO 2 -based GDE was investigated for the first time in a continuous-feed flow cell at a 10.2 cm 2 scale, both in an aqueous KHCO 3 medium and in a binary ionic liquid-organic solvent solution. Outstanding catalyst stability and selectivity, i.e. Faradaic efficiency to CO (FE CO ) from 84 to 90 % in the aqueous electrolyte, was demonstrated at current densities between −20 and −100 mA cm −2 , establishing a benchmark for the CO 2 reduction to CO on a Cu-based GDE. In comparison, a FE CO of 35 % (CO/H 2 ratio > 3) was reached at –20 mA cm −2 with 1-Butyl-3-methylimidazolium triflate ([BMIM][TfO]) in acetonitrile (ACN). Still, stability issues and a performance drop were faced during operation in this aprotic media. Molecular dynamics simulations and ex-situ physical–chemical characterisation assessed that the changes in the catalyst/GDE structure and electrolyte properties started with the displacement of Cu surface atoms from their equilibrium position by ACN molecules, which promotes the subsequent dissolution of Cu in the presence of [BMIM][TfO] molecules. Our findings highlight the significant influence of electrolyte composition on catalyst surface transformation and performance during the reaction. This work unveils critical issues for the practical application of IL-based electrolytes as co-catalysts and CO 2 capture media for CO 2 electrochemical conversion systems and proposes some mitigation strategies.

Chemical Engineering JournalVol. 514
University of Applied Sciences and Arts of Southern Switzerland (CH), Politecnico di Torino (IT), Fundació CTM Centre Tecnològic (ES), Parque Tecnológico de la Salud (ES)
Openalex Percentile: Top 44%
CO2 Reduction Techniques and Catalysts
0.36
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