Yang Kang, Li Ming, Gao Tianqi, Xu Guoliang, Li Di, Zheng Yao, Li Qiang, Duan Jingjing
MIIT Key Lab Thermal Control Electronic Equipment, School of Energy and Power Engineering, Nanjing University of Science and Technology, 210094, Nanjing, China.
School of Chemical Engineering, The University of Adelaide, Adelaide, SA, 5005, Australia.
Nat Commun. 2024 Aug 16;15(1):7060. doi: 10.1038/s41467-024-51475-7.
Industrial CO electrolysis via electrochemical CO reduction has achieved progress in alkaline solutions, while the same reaction in acidic solution remains challenging because of severe hydrogen evolution side reactions, acid corrosion, and low target product selectivity. Herein, an industrial acidic CO electrolysis to pure HCOOH system is realized in a proton-exchange-membrane electrolyzer using an acid-tolerant Bi-based metal-organic framework guided by a Pourbaix diagram. Significantly, the Faradaic efficiency of HCOOH synthesis reaches 95.10% at a large current density of 400 mA/cm with a high CO single-pass conversion efficiency of 64.91%. Moreover, the proton-exchange-membrane device also achieves an industrial-level current density of 250 mA/cm under a relatively low voltage of 3.5 V for up to 100 h with a Faradaic efficiency of 93.5% for HCOOH production, which corresponds to an energy consumption of 200.65 kWh/kmol, production rate of 12.1 mmol/m/s, and an energy conversion efficiency of 38.2%. These results will greatly aid the contemporary research moving toward commercial implementation and success of CO electrolysis technology.
通过电化学CO还原进行的工业CO电解在碱性溶液中已取得进展,而在酸性溶液中进行同样的反应仍然具有挑战性,这是由于严重的析氢副反应、酸腐蚀和低目标产物选择性。在此,在质子交换膜电解槽中,利用基于Pourbaix图指导的耐酸铋基金属有机框架,实现了工业酸性CO电解制纯HCOOH系统。值得注意的是,在400 mA/cm的大电流密度下,HCOOH合成的法拉第效率达到95.10%,CO单程转化效率高达64.91%。此外,质子交换膜装置在3.5 V的相对低电压下,还实现了250 mA/cm的工业级电流密度,持续100 h,HCOOH生产的法拉第效率为93.5%,这对应于200.65 kWh/kmol的能耗、12.1 mmol/m/s的生产率和38.2%的能量转换效率。这些结果将极大地有助于当代研究朝着CO电解技术的商业实施和成功迈进。