Anionic Ionomer: Released Surface-Immobilized Cations and an Established Hydrophobic Microenvironment for Efficient and Durable CO<sub>2</sub>-to-Ethylene Electrosynthesis at High Current over One Month
Electrosynthesis of multicarbon products, such as C<sub>2</sub>H<sub>4</sub>, from CO<sub>2</sub> reduction on copper (Cu) catalysts holds promise for achieving carbon neutrality. However, maintaining a steady high current-level C<sub>2</sub>H<sub>4</sub> electrosynthesis still encounters challenges, arising from unstable alkalinity and carbonate precipitation caused by undesired ion migration at the cathode under a repulsive electric field. To address these issues, we propose a universal "charge release" concept by incorporating tiny amounts of an oppositely charged anionic ionomer (e.g., perfluorinated sulfonic acid, PFSA) into a cationic covalent organic framework on the Cu surface (cCOF/PFSA). This strategy effectively releases the hidden positive charge within the cCOF, enhancing surface immobilization of cations to impede both outward migration of generated OH<sup>-</sup> and inward migration of cations, inhibiting carbonate precipitation and creating a strong alkaline microenvironment. Meanwhile, the ionomer's hydrophobic chains create a hydrophobic environment within the cCOF, facilitating efficient gas transport. In situ characterizations and theoretical calculations demonstrate that the cCOF/PFSA catalyst establishes a hydrophobic strong alkaline microenvironment, optimizing the adsorption strength and configuration of *CO intermediates to promote the C<sub>2</sub>H<sub>4</sub> formation. The optimized catalyst achieves a 70.5% Faradaic efficiency for C<sub>2</sub>H<sub>4</sub> with a partial current density over 470 mA cm<sup>-2</sup>. Notably, it delivers a high single-pass carbon efficiency of 96.5% for CO<sub>2</sub>RR and sustains an exceptional stability over 760 h. When implemented in a large-area MEA electrolyzer and a 5-cell MEA stack, the system achieves an industrial current of 15 A and continuous C<sub>2</sub>H<sub>4</sub> production exceeding 19 mL min<sup>-1</sup>, marking a significant step toward industrial feasibility in CO<sub>2</sub>RR-to-C<sub>2</sub>H<sub>4</sub> conversion.
Authors
- Xiao-Chen Feng (ORCID: https://orcid.org/0000-0002-8188-8368)
- Zewen Wang (ORCID: https://orcid.org/0000-0001-9436-2456)
- Liming Dai (ORCID: https://orcid.org/0000-0001-7536-160X)
- Mingwei Fang
- Ying Zhu (ORCID: https://orcid.org/0000-0001-5611-4291)
- Lei Jiang (ORCID: https://orcid.org/0000-0003-4579-728X)
- Zihao Huang (ORCID: https://orcid.org/0009-0005-8364-7444)
- Meiling Wang (ORCID: https://orcid.org/0000-0002-4881-7189)
- Xiang Miao (ORCID: https://orcid.org/0000-0002-1577-1698)
Institutions
- Chinese Academy of Sciences (CN)
- UNSW Sydney (AU)
- Technical Institute of Physics and Chemistry (CN)
- Beijing Advanced Sciences and Innovation Center (CN)
- Beihang University (CN)
Publication Details
- Journal
- Journal of the American Chemical Society
- Published
- 2024-09-19
- DOI
- https://doi.org/10.1021/jacs.4c09168
- Citations
- 67
- Primary Topic
- CO2 Reduction Techniques and Catalysts
- Type
- article
- Field-Weighted Citation Impact
- 6.86
Funders
- National Natural Science Foundation of China
- Beihang University
- Chinese Academy of Sciences
- Higher Education Discipline Innovation Project
- Australian Research Council