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. 2025 Sep 3;8(18):13607-13619.
doi: 10.1021/acsaem.5c01866. eCollection 2025 Sep 22.

Highly Selective Electrolytic Reduction of CO2 to Ethylene

Affiliations

Highly Selective Electrolytic Reduction of CO2 to Ethylene

Monsuru Olatunji Dauda et al. ACS Appl Energy Mater. .

Abstract

We investigate the reduction of CO2 to ethylene across buffered anolyte pH values 4 to 14 using a copper-phosphorus (Cu-P) electrocatalyst in a zero-gap membrane electrode assembly. Electrochemical CO2 reduction using alkaline electrolytes typically shows limited carbon efficiencies and single-pass efficiencies, while acidic conditions typically favor the hydrogen evolution reaction. Results from this work show that weakly phosphate-buffered acidic anolytes (pH 6) maximize ethylene production with a 73% FE at 300 mA cm-2 and 51% FE at 500 mA cm-2, including a 51% single-pass CO2 conversion efficiency for over 400 h of continuous operation. We propose a mechanism based on pH-dependent CO coverage that controls the selectivity at the *HCCOH intermediate. Low CO coverage at pH 6 favors hydroxide elimination to *CCH, yielding ethylene (98% of C2 products), while high coverage at pH 14 promotes hydrogenation to ethanol (44% of C2). The HER mechanism transitions from H2O-mediated at pH 14 to phosphate-mediated (H2PO4 -/HPO4 2-) at weakly acidic pH, minimizing HER competition at pH 6. This mechanistic understanding enables controlled C2 product selectivity through manipulation of the CO coverage and local proton activity.

Keywords: CO2 electroreduction; copper-based electrocatalyst; ethylene selectivity; membrane electrode assembly; pH optimization.

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Figures

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Morphology and structural characterization. The (A) SEM image of Cu–P showing spherical nanoparticles with average diameters around 100 nm. (B, C) EDS elemental mapping shows a uniform distribution of Cu and P elements. (D) XRD patterns of Cu–P, (E, F) Cu 2p, and P 2p XPS spectra of Cu–P.
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CO2 electrolysis to ethylene. (A) Schematic representation of the membrane electrode assembly system studied in this work. (B) Comparison of reported CO2-to-ethylene electrocatalytic systems.
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Electrocatalytic CO2 reduction performance at constant cell potential of 4 V. (A) The effect of phosphorus content on the FE distribution of CO2 reduction products in KHCO3 (pH = 8). (B) The influence of pH on the single-pass CO2 conversion efficiency (SPCE), C1 product selectivity, and C2 product selectivity during CO2 reduction on Cu–P0.065. (C) The effect of pH on the FE for various CO2 reduction products. (D) Relative selectivity distribution of C2 products across the pH range.
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Membrane, pH, and cation effects on the CO2 electroreduction performance. (A) FE distribution across pH 2–6 in a CEM system using pure H3PO4. (B) FE distribution across different membranes after K+ (1 M) addition. (C) Long-term stability test of the AEM system at pH 6. (D) Effect of the K+ concentration (0.1–2 M) on the product distribution at pH 6.
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Effects of cation identity and anion type on CO2 electroreduction performance. (A) FE distribution across different cation systems (Na+, K+, and Cs+) at pH 14. (B) Relative selectivity of C2 products showing an ethylene:ethanol ratio at pH 14. (C) Faradaic efficiencies across different anions (PO4 2–, SO4 2–, and NO3 ) at pH 6. (D) Relative selectivity of C2 products across anions at pH 6.
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Effect of current density on CO2 reduction performance in the AEM system. (A) FE distribution for CO2 reduction products as a function of current density (100–500 mA cm–2) at pH 6 using Cu–P0.065 electrocatalyst. (B) Total C2 product selectivity and relative distribution of C2 products (ethylene and ethanol) across different current densities (100–500 mA cm–2) at pH 6 using the Cu–P0.065 electrocatalyst. (C) FE distribution for CO2 reduction products as a function of current density (100–500 mA cm–2) at pH 6 using an unmodified Cu electrocatalyst. (D) Total C2 product selectivity and relative distribution of C2 products (ethylene and ethanol) across different current densities (100–500 mA cm–2) at pH 6 using an unmodified Cu electrocatalyst.
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Proposed mechanism for the formation of C2 products from CO2 electrolysis. As CO coverage increases, selectivity shifts from ethylene to ethanol and then to acetate.
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Relative rates of the Volmer step for five different proton donors as a function of electrolyte pH at a constant U RHE. The black line shows the total HER rate for all proton donors in an electrolyte with 1 mol/L total phosphate.

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