<p>Electrochemical upcycling of captured CO<sub>2</sub> under high pressure holds significant potential to bridge between CO<sub>2</sub> emissions and hydrocarbon commodities, yet it remains underexplored. Here we convert gas-phase high-pressure captured CO<sub>2</sub> into ethylene (C<sub>2</sub>H<sub>4</sub>) using a high-pressure membrane electrode assembly equipped with In/Cu catalysts, affording up to 85% Faradaic efficiency and 750 mA cm<sup>−2</sup> partial current density under 20 bar. Theoretical calculations and operando studies link enhanced C–C coupling to the pressure-modulated *CO adsorption configuration and elevated CO<sub>2</sub> coverage. High pressure also mitigates salt precipitation by relocating bicarbonate formation to the catalyst–membrane interface, enabling stable electrolysis for over 1,500 h at 600 mA cm<sup>−2</sup>. As a proof of concept, by recapturing residual CO<sub>2</sub>, the system delivers industrial-grade 99.9% purity C<sub>2</sub>H<sub>4</sub>, creating an opportunity to turn the otherwise costly CO<sub>2</sub> capture into a profit. Energy analysis suggests that directly valorizing high-pressure captured CO<sub>2</sub>, instead of depressurizing and repressurizing, is essential to minimize energy consumption.</p><p></p>

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Electrocatalytic upcycling of high-pressure captured CO2 to ethylene

  • Liang Huang,
  • Ge Gao,
  • Jiwu Zhao,
  • William L. Roberts,
  • Xu Lu

摘要

Electrochemical upcycling of captured CO2 under high pressure holds significant potential to bridge between CO2 emissions and hydrocarbon commodities, yet it remains underexplored. Here we convert gas-phase high-pressure captured CO2 into ethylene (C2H4) using a high-pressure membrane electrode assembly equipped with In/Cu catalysts, affording up to 85% Faradaic efficiency and 750 mA cm−2 partial current density under 20 bar. Theoretical calculations and operando studies link enhanced C–C coupling to the pressure-modulated *CO adsorption configuration and elevated CO2 coverage. High pressure also mitigates salt precipitation by relocating bicarbonate formation to the catalyst–membrane interface, enabling stable electrolysis for over 1,500 h at 600 mA cm−2. As a proof of concept, by recapturing residual CO2, the system delivers industrial-grade 99.9% purity C2H4, creating an opportunity to turn the otherwise costly CO2 capture into a profit. Energy analysis suggests that directly valorizing high-pressure captured CO2, instead of depressurizing and repressurizing, is essential to minimize energy consumption.