电解
甲酸
材料科学
析氧
阳极
电化学
电势能
催化作用
能源消耗
工艺工程
化学工程
格式化
纳米技术
化学
可再生能源
电力转天然气
电能消耗
环境科学
电解槽
制氢
电催化剂
电极
作者
Xiaotong Li,Kan Gao,Mingbo Qu,Nanhui Li,Xiangzhou Lv,Xiuju Wu,Qingyang Lin,Hao Bin Wu
标识
DOI:10.1038/s41467-025-64306-0
摘要
Reducing the electrical energy consumption for formic acid electro-synthesis is indispensable for advancing its industrial implementation. In a conventional CO2 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 CO2 electrolyzer design that pairs electrochemical CO2 reduction (CO2R) 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-1formate) at cell voltages below 2.7 V across a current density range of 0.05-0.4 A cm-2. 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 CO2R electrolyzer engineering toward energy-efficient, economically viable production of valuable chemicals.
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