Anion exchange membrane co-electrolysis of CO2 and water using CuOx nanoparticles-based gas diffusion electrode for the conversion of carbon dioxide into carbonaceous fuels

• CuOx nanoparticles-gas diffusion electrode was used for CO 2 -water co-electrolysis. • A zero-gap AEM electrolysis cell was used with an analysis of outlet composition. • Co-electrolysis cell was operated at 0.3 A cm −2 with a voltage efficiency of 65%. • Faradaic efficiency >38 % for ethylene production was recorded at 0.3 A cm −2 . • An analysis of the reaction mechanism in alkaline environment was made. Low temperature CO 2 − water co-electrolysis was studied in a zero-gap cell based on an anion exchange membrane to produce synthetic fuels at suitable energy efficiency and current density thanks to a proper combination of specific materials, cell configuration and operating conditions. The electrochemical cell consisted of gas-diffusion electrodes containing non-precious electrocatalysts such as nanosized particles-based copper oxide for the cathode and Ni-Fe oxide-hydroxide for the anode. The stability of these electrocatalysts was favoured by a high internal operating pH assured through the recirculation of KOH at the anode. The CO 2 stream was humidified at the operating cell temperature or higher before being fed to the cathode. The process was studied in terms of outlet stream composition, electrochemical performance, faradaic and voltage efficiency through galvanostatic operation at practical current densities, e.g. 0.3 A cm −2 , combined to gas chromatographic analysis. Electrochemical diagnostics, such as polarization curves and ac-impedance spectroscopy combined to productivity data, allowed to derive an interpretation of the cell behaviour under different operating conditions revealing a paramount effect of the ionomer dispersion, added to the cathode, and the operating current density. A useful strategy was adopted to mitigate the precipitation of carbonates. Promising results were observed in terms of production of ethylene and syngas at suitable voltage and faradaic efficiencies. A possible reaction mechanism for the CO 2 reduction under alkaline conditions was considered in relation to the formed products.

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Publication Details

Journal
Chemical Engineering Journal
Published
2025-05-15
DOI
https://doi.org/10.1016/j.cej.2025.163798
Citations
2
Primary Topic
CO2 Reduction Techniques and Catalysts
Type
article
Field-Weighted Citation Impact
0.73

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article

Anion exchange membrane co-electrolysis of CO2 and water using CuOx nanoparticles-based gas diffusion electrode for the conversion of carbon dioxide into carbonaceous fuels

V. Chiodo, Susanna Maisano, A.S. Aricò, Mariarosaria Pascale et al.
2 citations
Chemical Engineering Journal
CO2 Reduction Techniques and Catalysts
0.73
article

Anion exchange membrane co-electrolysis of CO2 and water using CuOx nanoparticles-based gas diffusion electrode for the conversion of carbon dioxide into carbonaceous fuels

V. Chiodo, Susanna Maisano, A.S. Aricò, Mariarosaria Pascale, Charly Azra, Sabrina Campagna Zignani, Alessandra Carbone, Marianna Gigliotti De Fazio, Ervin Tal Gutelmacher, Luca Rillo, Anna Ramunni
article en
2 citations

Abstract

• CuOx nanoparticles-gas diffusion electrode was used for CO 2 -water co-electrolysis. • A zero-gap AEM electrolysis cell was used with an analysis of outlet composition. • Co-electrolysis cell was operated at 0.3 A cm −2 with a voltage efficiency of 65%. • Faradaic efficiency >38 % for ethylene production was recorded at 0.3 A cm −2 . • An analysis of the reaction mechanism in alkaline environment was made. Low temperature CO 2 − water co-electrolysis was studied in a zero-gap cell based on an anion exchange membrane to produce synthetic fuels at suitable energy efficiency and current density thanks to a proper combination of specific materials, cell configuration and operating conditions. The electrochemical cell consisted of gas-diffusion electrodes containing non-precious electrocatalysts such as nanosized particles-based copper oxide for the cathode and Ni-Fe oxide-hydroxide for the anode. The stability of these electrocatalysts was favoured by a high internal operating pH assured through the recirculation of KOH at the anode. The CO 2 stream was humidified at the operating cell temperature or higher before being fed to the cathode. The process was studied in terms of outlet stream composition, electrochemical performance, faradaic and voltage efficiency through galvanostatic operation at practical current densities, e.g. 0.3 A cm −2 , combined to gas chromatographic analysis. Electrochemical diagnostics, such as polarization curves and ac-impedance spectroscopy combined to productivity data, allowed to derive an interpretation of the cell behaviour under different operating conditions revealing a paramount effect of the ionomer dispersion, added to the cathode, and the operating current density. A useful strategy was adopted to mitigate the precipitation of carbonates. Promising results were observed in terms of production of ethylene and syngas at suitable voltage and faradaic efficiencies. A possible reaction mechanism for the CO 2 reduction under alkaline conditions was considered in relation to the formed products.

Chemical Engineering JournalVol. 515
Medi-Tate (Israel) (IL), Institute for Advanced Energy Technologies (IT), University of Milano-Bicocca (IT)
Horizon 2020 Framework Programme
Openalex Percentile: Top 31%
CO2 Reduction Techniques and Catalysts
0.73
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