Qiaoqi Guo, Bowen Jiang, Le Huang, Kunyu Jiang, Rongrong Tang, Qinong Zhu, Huajun Feng, Mengyang Fan, Yijing Xia
Acidic CO2 electrolysis to formic acid circumvents carbonate formation and enables direct product recovery, yet is hindered by severe competition between formate-producing *OCHO and hydrogen-producing *H intermediates. Here, we develop a hierarchical site-solvation-transport regulation strategy to direct this competition toward formic acid. Mixed, undercoordinated Sn/SnOx nanoclusters provide catalytic environments associated with the *OCHO pathway, while K+-dependent interfacial solvation is associated with reduced hydrogen evolution reaction (HER) competition and enhanced formic acid selectivity. A Janus asymmetric-wettability electrode further stabilizes CO2 mass transport and prevents electrolyte flooding, sustaining a favorable cathodic microenvironment. This integrated strategy achieves ∼85% formic acid Faradaic efficiency in acidic media with an initial 18 h stability window at 400 mA cm-2. This work establishes a multiscale strategy for coupling intermediate selectivity with mass-transport management in acidic CO2 electrolysis.