Improving the Stability of Gas Diffusion Electrodes for CO<sub>2</sub> Electroreduction to Formate with Sn and In-Based Catalysts at 500 mA cm<sup>–2</sup>: Effect of Electrode Design and Operation Mode

The electrochemical carbon dioxide reduction reaction (CO<sub>2</sub>RR) using renewable electricity sources could provide a sustainable solution for generating valuable chemicals, such as formate salt or formic acid. However, an efficient, stable, and scalable electrode generating formate at industrially viable current densities (>100 mA cm<sup>-2</sup>) is yet to be developed. Sn or In-based catalysts in gas diffusion electrodes (GDE) can efficiently produce formate. However, their long-term durability is limited owing to catalyst deactivation, carbonate deposition, and electrode flooding. Herein, a systematic study of 20 cm<sup>2</sup> GDEs with SnO<sub>2</sub> and In<sub>2</sub>O<sub>3</sub> catalyst layers is presented in conjunction with various electrode operation strategies (i.e., flow-by vs flow through, dry vs humidified CO<sub>2</sub>, continuous vs reverse polarity pulse electrolysis). It is demonstrated that the incorporation of CeO<sub>2</sub> nanoparticles as a promoter in either SnO<sub>2</sub> or In<sub>2</sub>O<sub>3</sub> catalyst layers coupled with intermittent reverse polarity pulse operation dramatically improves the GDE stability during 12 h of tests at 500 mA cm<sup>-2</sup> with over 90% formate Faradaic efficiency. Due to its strong oxidizing capacity, CeO<sub>2</sub> helps Sn and In regain their valence state of + IV and + III, respectively, which are in situ reduced during CO<sub>2</sub>RR, as shown by the surface characterization of the electrodes. The effect of the initial particle size of SnO<sub>2</sub> and reverse polarity pulse on the catalytic activity, durability, and carbonate salt precipitation in the GDE have also been addressed. Regarding two-phase flow dynamics, the quasi-convective gas flow through the GDE was more beneficial than the gas flow-by mode for enabling stable operation at high current densities (up to 500 mA cm<sup>-2</sup>). The synergistic approach of catalyst layer engineering coupled with diverse GDE operation modes explored here is promising for the scale-up of efficient and durable reactors for the CO<sub>2</sub>RR to formate and CO<sub>2</sub> redox flow batteries.

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Publication Details

Journal
ACS Omega
Published
2024-12-20
DOI
https://doi.org/10.1021/acsomega.4c09202
Citations
6
Primary Topic
CO2 Reduction Techniques and Catalysts
Type
article
Field-Weighted Citation Impact
0.61

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article

Improving the Stability of Gas Diffusion Electrodes for CO2 Electroreduction to Formate with Sn and In-Based Catalysts at 500 mA cm–2: Effect of Electrode Design and Operation Mode

Előd Gyenge, Shahid M. Bashir
6 citations
ACS Omega
CO2 Reduction Techniques and Catalysts
0.61
article

Improving the Stability of Gas Diffusion Electrodes for CO2 Electroreduction to Formate with Sn and In-Based Catalysts at 500 mA cm–2: Effect of Electrode Design and Operation Mode

Előd Gyenge, Shahid M. Bashir
article en
6 citations

Abstract

The electrochemical carbon dioxide reduction reaction (CO<sub>2</sub>RR) using renewable electricity sources could provide a sustainable solution for generating valuable chemicals, such as formate salt or formic acid. However, an efficient, stable, and scalable electrode generating formate at industrially viable current densities (>100 mA cm<sup>-2</sup>) is yet to be developed. Sn or In-based catalysts in gas diffusion electrodes (GDE) can efficiently produce formate. However, their long-term durability is limited owing to catalyst deactivation, carbonate deposition, and electrode flooding. Herein, a systematic study of 20 cm<sup>2</sup> GDEs with SnO<sub>2</sub> and In<sub>2</sub>O<sub>3</sub> catalyst layers is presented in conjunction with various electrode operation strategies (i.e., flow-by vs flow through, dry vs humidified CO<sub>2</sub>, continuous vs reverse polarity pulse electrolysis). It is demonstrated that the incorporation of CeO<sub>2</sub> nanoparticles as a promoter in either SnO<sub>2</sub> or In<sub>2</sub>O<sub>3</sub> catalyst layers coupled with intermittent reverse polarity pulse operation dramatically improves the GDE stability during 12 h of tests at 500 mA cm<sup>-2</sup> with over 90% formate Faradaic efficiency. Due to its strong oxidizing capacity, CeO<sub>2</sub> helps Sn and In regain their valence state of + IV and + III, respectively, which are in situ reduced during CO<sub>2</sub>RR, as shown by the surface characterization of the electrodes. The effect of the initial particle size of SnO<sub>2</sub> and reverse polarity pulse on the catalytic activity, durability, and carbonate salt precipitation in the GDE have also been addressed. Regarding two-phase flow dynamics, the quasi-convective gas flow through the GDE was more beneficial than the gas flow-by mode for enabling stable operation at high current densities (up to 500 mA cm<sup>-2</sup>). The synergistic approach of catalyst layer engineering coupled with diverse GDE operation modes explored here is promising for the scale-up of efficient and durable reactors for the CO<sub>2</sub>RR to formate and CO<sub>2</sub> redox flow batteries.

ACS OmegaVol. 10(1)
University of British Columbia (CA)
Mitacs, University of British Columbia, Natural Sciences and Engineering Research Council of Canada
Affordable and clean energy
Openalex Percentile: Top 38%
CO2 Reduction Techniques and Catalysts
0.61
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