Wang Meng, Luo Chenxi, Mi Ziyu, Chang Yu-Chia, Chueh Yu-Ting, Luo Ping, Zhang Mingsheng, Zhang Jiguang, Yang Ruoou, Yang Qin, Wang Sibo, Chen Shuo, Jia Jinfeng, Leow Wan Ru, Aabdin Zainul, Hung Sung-Fu, Lum Yanwei
Department of Chemical and Biomolecular Engineering, National University of Singapore, Singapore, 117585, Republic of Singapore.
Institute of Materials Research and Engineering, Agency for Science, Technology and Research (A*STAR), 2 Fusionopolis Way, Innovis #08-03, Singapore, 138634, Republic of Singapore.
Angew Chem Int Ed Engl. 2025 Jul 7;64(28):e202505987. doi: 10.1002/anie.202505987. Epub 2025 May 8.
Renewable energy-powered co-electrolysis of CO and NO offers a promising pathway toward sustainable urea production. However, achieving high urea selectivity is challenging due to substantial competing side reactions. Here, we show that engendering a high density of CO bubbles on the catalyst surface creates numerous triple-phase boundaries that are key toward enhancing CO versus NO availability for selective urea production. We implemented this strategy using a bipolar membrane in a zero-gap electrolyzer, which allows for the in situ conversion of (bi)carbonate to CO bubbles at the catalyst/electrolyte interface. Notably, we demonstrate that this electrolyzer system can utilize simulated flue gas (20% CO + 5% O) for urea production. With a CuRu catalyst, we achieve a urea Faradaic efficiency of 58% at 2 V full-cell voltage over an extended 30-h period and a peak production rate of 35.46 mmol h g . Under these conditions, the Faradaic efficiency to hydrogen evolution and nitrate reduction are 14.7% and 21.6%, respectively. Strikingly, these results with simulated flue gas are comparable to previously reported systems that employ pure CO. Our results introduce a simple yet effective design approach toward developing efficient electrolyzer systems for urea production.
由可再生能源驱动的一氧化碳和一氧化氮共电解为可持续尿素生产提供了一条很有前景的途径。然而,由于大量竞争性副反应的存在,实现高尿素选择性具有挑战性。在此,我们表明在催化剂表面产生高密度的一氧化碳气泡会形成大量三相边界,这是提高一氧化碳与一氧化氮选择性用于尿素生产的关键。我们在零间隙电解槽中使用双极膜实施了这一策略,该策略允许在催化剂/电解质界面将(双)碳酸盐原位转化为一氧化碳气泡。值得注意的是,我们证明了这种电解槽系统可以利用模拟烟道气(20%一氧化碳 + 5%氧气)来生产尿素。使用铜钌催化剂,在2 V全电池电压下经过30小时的长时间运行,我们实现了58%的尿素法拉第效率,峰值产率为35.46 mmol h g。在这些条件下,析氢和硝酸盐还原的法拉第效率分别为14.7%和21.6%。引人注目的是,这些使用模拟烟道气的结果与先前报道的使用纯一氧化碳系统相当。我们的结果为开发用于尿素生产的高效电解槽系统引入了一种简单而有效的设计方法。