Membrane-free CO<sub>2</sub> electrolyzer design for economically efficient formic acid electro-synthesis.
basic_science · Level V
Where this comes from
- Record sourced from PubMed, PMID 41107254.
- Also identified by DOI 10.1038/s41467-025-64306-0 and PMC identifier 12534513.
- Licence recorded as CC BY-NC-ND.
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Abstract
Reducing the electrical energy consumption for formic acid electro-synthesis is indispensable for advancing its industrial implementation. In a conventional CO<sub>2</sub> electrolyzer, most input electrical energy is consumed by the unprofitable anodic oxygen evolution reaction (OER) and ohmic drop. Electrolyzer engineering provides a promising platform to boost electrical energy utilization efficiency beyond catalyst optimization. Herein, we demonstrate a membrane-free CO<sub>2</sub> electrolyzer design that pairs electrochemical CO<sub>2</sub> reduction (CO<sub>2</sub>R) with an all-liquid-phase anodic reaction, enabling dual production of formate at both electrodes with significantly reduced cell voltage. The optimized design exhibits the lowest electrical energy consumption (< 310 kJ mol<sup>-1</sup><sub>formate</sub>) at cell voltages below 2.7 V across a current density range of 0.05-0.4 A cm<sup>-2</sup>. This cell also maintains stable operation at 2.25 V for 313 h with a < 20 % increase in electrical energy consumption. Systematic techno-economic analysis (TEA) evaluates the economic viability of this design for formic acid electro-synthesis, revealing a potential roadmap towards low-cost formic acid production. This strategy provides guidelines for CO<sub>2</sub>R electrolyzer engineering toward energy-efficient, economically viable production of valuable chemicals.