化学
电合成
电解
阳极
乙二醇
格式化
法拉第效率
纳米技术
光电解
工作电极
化学工程
无机化学
电解槽
能量转换
电阻式触摸屏
电化学电池
电化学
金属有机骨架
多相催化
参比电极
电催化剂
电解水
化学修饰电极
辅助电极
气体扩散电极
化学能
气体扩散
可逆氢电极
电极
催化作用
作者
Xin‐Yao Yu,Hesamoddin Rabiee,Abhijit Dutta,Yaqiang Li,Zsolt Szakály,Soma Vesztergom,Lucas Warmuth,Alain Rieder,Peter Broekmann
摘要
The rising accumulation of poly(ethylene terephthalate) (PET) waste and atmospheric CO2 presents serious environmental and health challenges. Herein, we introduce a novel strategy for the simultaneous electrochemical upcycling of PET and CO2 in a single integrated electrolyzer, enabling ampere-level coproduction of formate. Leveraging careful electrode design of three-dimensional Ni foam at the anode for ethylene glycol (EG, derived from PET hydrolysis) electrolysis, formate formation at 1.2 A cm-2 was achieved─outperforming all reported performances for non-noble metal catalysts. A Bi2O2CO3-based gas diffusion electrode (GDE) enabled the selective reduction of CO2 (CO2RR) to formate at the cathode. By prioritizing enhanced reactant transport and electrode architecture beyond catalyst discovery, this integrated system achieved 100 h of stable operation at 0.50 A cm-2 with Faradaic efficiencies of 93.7% (anode) and 86.0% (cathode). Superior energy efficiency was achieved in the proposed membrane-free electrolyzer, with a cell voltage of 2.91 V at 1.0 A cm-2, reducing the input energy by 65% to ca. 0.1 kWh mol-1. This study highlights the critical role of anodic reaction choices and electrode engineering strategies in developing integrated electrolyzers with superior performance metrics.
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