Steering the Selectivityof Electrochemical CO<sub>2</sub> Reduction on the Cu Catalyst viathe Interplay between theElectrode Morphology and Electrolyte Anion Identity

Electrochemical carbon dioxide (CO<sub>2</sub>) reduction (ECR) holds promise as a viable pathway for the generation of fuels and chemicals. Several strategies have been explored to enhance the product selectivity of ECR on copper (Cu) catalysts. A systematic approach to optimize the local reaction microenvironment, however, remains elusive. Engineering the electrode structure and reaction microenvironment is a facile but effective strategy for steering the product selectivity of ECR reactions and can enable the rational design of highly selective Cu electrodes. Herein, we demonstrate that the synergy between an optimized Cu gas diffusion electrode (GDE) morphology and electrolyte anion identity can steer ECR product selectivity toward ethylene (C<sub>2+</sub>) or methane via the local CO<sub>2</sub> availability, pH, and electrode morphology regulation. We show that using a relatively thin 100 nm Cu catalyst layer (CL) sputtered on an optimized macropore-sized hydrophobic poly(tetrafluoroethylene) substrate promotes methane selectivity at high reaction rates. We achieved a methane partial current density of 126 mA cm<sup>–2</sup> and a Faradaic efficiency (FE) of 42%. In contrast, a relatively thick 500 nm Cu CL favors ethylene production, reaching a high FE of 52% at 250 mA cm<sup>–2</sup> (with a total C<sub>2+</sub> value of 77%) in a near-neutral KHCO<sub>3</sub> electrolyte. Utilizing KI electrolyte significantly enhances methane selectivity, achieving ca. 56% at a partial current density of 168 mA cm<sup>–2</sup> while effectively suppressing the hydrogen evolution reaction (HER) on the thin CL. Furthermore, on the relatively thick CL, a higher C<sub>2+</sub> FE of 84% was achieved at 250 mA cm<sup>–2</sup>, demonstrating the impact of electrolyte anion identity and CL thickness on product selectivity in ECR. In addition, we find that a further increase in the Cu CL thickness does not result in a superior C<sub>2+</sub> performance in KI compared to the KHCO<sub>3</sub> electrolyte. Our result highlights the critical role of the interplay between Cu electrode morphology and the electrolyte anion identity, which can facilitate efficient CO<sub>2</sub> mass transport, enable selective Cu sites, and tune local pH – thereby steering ECR product selectivity.

Publication Details

Journal
Figshare
Published
2025-03-24
DOI
https://doi.org/10.1021/acscatal.4c08113.s001
Primary Topic
CO2 Reduction Techniques and Catalysts
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article
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article

Steering the Selectivityof Electrochemical CO2 Reduction on the Cu Catalyst viathe Interplay between theElectrode Morphology and Electrolyte Anion Identity

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CO2 Reduction Techniques and Catalysts
article

Steering the Selectivityof Electrochemical CO2 Reduction on the Cu Catalyst viathe Interplay between theElectrode Morphology and Electrolyte Anion Identity

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Abstract

Electrochemical carbon dioxide (CO<sub>2</sub>) reduction (ECR) holds promise as a viable pathway for the generation of fuels and chemicals. Several strategies have been explored to enhance the product selectivity of ECR on copper (Cu) catalysts. A systematic approach to optimize the local reaction microenvironment, however, remains elusive. Engineering the electrode structure and reaction microenvironment is a facile but effective strategy for steering the product selectivity of ECR reactions and can enable the rational design of highly selective Cu electrodes. Herein, we demonstrate that the synergy between an optimized Cu gas diffusion electrode (GDE) morphology and electrolyte anion identity can steer ECR product selectivity toward ethylene (C<sub>2+</sub>) or methane via the local CO<sub>2</sub> availability, pH, and electrode morphology regulation. We show that using a relatively thin 100 nm Cu catalyst layer (CL) sputtered on an optimized macropore-sized hydrophobic poly(tetrafluoroethylene) substrate promotes methane selectivity at high reaction rates. We achieved a methane partial current density of 126 mA cm<sup>–2</sup> and a Faradaic efficiency (FE) of 42%. In contrast, a relatively thick 500 nm Cu CL favors ethylene production, reaching a high FE of 52% at 250 mA cm<sup>–2</sup> (with a total C<sub>2+</sub> value of 77%) in a near-neutral KHCO<sub>3</sub> electrolyte. Utilizing KI electrolyte significantly enhances methane selectivity, achieving ca. 56% at a partial current density of 168 mA cm<sup>–2</sup> while effectively suppressing the hydrogen evolution reaction (HER) on the thin CL. Furthermore, on the relatively thick CL, a higher C<sub>2+</sub> FE of 84% was achieved at 250 mA cm<sup>–2</sup>, demonstrating the impact of electrolyte anion identity and CL thickness on product selectivity in ECR. In addition, we find that a further increase in the Cu CL thickness does not result in a superior C<sub>2+</sub> performance in KI compared to the KHCO<sub>3</sub> electrolyte. Our result highlights the critical role of the interplay between Cu electrode morphology and the electrolyte anion identity, which can facilitate efficient CO<sub>2</sub> mass transport, enable selective Cu sites, and tune local pH – thereby steering ECR product selectivity.

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CO2 Reduction Techniques and Catalysts
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