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.
Authors
- Előd Gyenge (ORCID: https://orcid.org/0000-0002-1977-4407)
- Shahid M. Bashir
Institutions
- University of British Columbia (CA)
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
Funders
- Mitacs
- University of British Columbia
- Natural Sciences and Engineering Research Council of Canada