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. 2025 Mar 3;5(3):287-297.
doi: 10.1021/acsenvironau.4c00121. eCollection 2025 May 21.

Silver-Doped Porous Copper Catalysts for Efficient Resource Utilization of CO-Containing Flue Gases

Affiliations

Silver-Doped Porous Copper Catalysts for Efficient Resource Utilization of CO-Containing Flue Gases

Zhengkai Zhuang et al. ACS Environ Au. .

Abstract

CO is both a key intermediate in the electrocatalytic conversion of CO2 and a valuable C1 resource, with the potential to reduce carbon emissions and mitigate the energy crisis. However, industrially emitted CO remains underutilized due to inefficiencies and economic challenges. Electrocatalytic CO reduction offers a promising approach for the efficient and environmentally friendly utilization of CO-containing flue gases. Nevertheless, current technologies face limitations, such as low operating currents and difficulties in adaptation to complex reaction gas components. Here, we report a low-cost silver-doped porous copper oxide (Ag-pCuO) catalyst. The doping of a moderate amount of Ag (0.875% doping) endows porous CuO with highly selective Cu-Ag active sites, enhanced CO adsorption, and improved surface valence stability, allowing Ag0.875%-pCuO to achieve remarkable catalytic performance in a carbon-doped titanium-based membrane electrode assembly electrolytic cell. It achieves a remarkable C2+ faradic efficiency of up to 94% at a high current density of -4 A under a simulated calcium carbide furnace gas atmosphere and demonstrates exceptional stability, with only a 6.08% decline in C2+ faradic efficiency after over 110 h of continuous operation. In summary, this research presents a novel approach for applying Ag-doped copper-based catalysts to industrially utilize CO-containing flue gases, especially from calcium carbide furnaces.

Keywords: CO reduction; electrocatalytic; electrolyzer; flue gas; resource utilization.

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Figures

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Preparation methods and characterization of Ag x%-pCuO, pCuO, and Cu­(OH)2 needles. (a) Schematic illustration of the preparation of Ag x%-pCuO, (b) TEM images of Cu­(OH)2 needles, (c) SEM images of Ag0.875%-pCuO, (d, g) TEM images of Ag0.875%-pCuO, (e) TEM images of pCuO, (f) high-resolution TEM (HR-TEM) images of Ag0.875%-pCuO, and (h–k) element mapping analyses of Ag0.875%-pCuO.
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Structural characterizations of the Ag-pCuO series and pCuO. (a) XRD patterns of Ag-pCuO series and pCuO, (b) Cu 2p spectra of Ag0.875%-pCuO, (c) Ag 3d spectra of Ag-pCuO series and pCuO, and (d) specific surface area measurement of Ag-pCuO series and pCuO.
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Lab-scale measurement of Ag-pCuO series’ electrocatalytic CORR performances. Faradic efficiency of the reduction products for (a) Ag0.875%-pCuO and (b) pCuO at different applied currents.
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Pilot test of Ag-pCuO series’ electrocatalytic CORR performances. FE distribution of the CORR products for the (a) Ag0.875%-pCuO and (b) pCuO catalyst at different currents in an MEA cell, (c) comparison of the electrocatalytic performances of Ag-pCuO series and pCuO at −4 A, and (d) FE distribution of the CORR products for the Ag0.875%-pCuO at different currents in a reaction system with two cells in parallel. The gas source of all of the tests is simulated CCFS and (e) chronopotentiometry stability test of Ag0.875%-pCuO at −4 A (−111.11 mA cm–2) in MEA.
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Auger patterns (a) of Ag0.875%-pCuO materials after the 110 h CORR reaction and Auger patterns (b) of Ag-pCuO materials after the 4.5 h CORR reaction.
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(a) In situ Raman spectroscopy studies of Ag0.875%-pCuO in a flow cell with the electrodes in contact with 1 M KOH; (b) schematic illustration of the possible reaction pathway of CO reduction over Ag0.875%-pCuO.

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