催化作用
氨生产
纳米颗粒
离解(化学)
材料科学
法拉第效率
氨
电化学
吸附
可逆氢电极
产量(工程)
化学工程
氢
无机化学
纳米技术
氧化物
解吸
桥接(联网)
电催化剂
阳极
钴
反应机理
制氢
多相催化
光化学
氧化还原
双金属片
电极
硝酸
反应速率
作者
Han Chen,Yu Gao,Jiaxin Du,Runlong Hao,Xuanhao Wu,Lidong Wang,ZhongBiao WU
出处
期刊:ACS Nano
[American Chemical Society]
日期:2026-01-02
卷期号:20 (2): 2323-2336
被引量:2
标识
DOI:10.1021/acsnano.5c18397
摘要
The electrochemical nitric oxide reduction reaction (NORR) provides a promising pathway for mitigating air pollutant NO while generating valuable ammonia (NH 3 ). However, most research has focused on high NO concentrations (≥10%), which contrast with industrial dilute streams (≤1%), where conventional catalysts, such as single-atom catalysts (SACs), struggle with insufficient active site density and limited *H supply, while nanoparticle catalysts suffer from hydrogen evolution reaction (HER) competition. To address these challenges, we designed a hybrid catalyst consisting of atomically dispersed Co–N 4 satellitic sites and Co(111) nanoparticles (Co SA-NPs). Through electronic interaction, Co(111) facilitated enhanced water dissociation to generate *H, while Co–N 4 sites strengthened NO adsorption and activation. This cooperative mechanism promoted rapid *H spillover, enabling selective NO hydrogenation to NH 3 while suppressing HER. Under 1% NO, Co SA-NPs achieved a significant NH 3 yield rate of 11389 μg cm –2 h –1, which is 2.6 to 243.9 times higher than all previously reported NORR catalysts. At industrially relevant and ultralow concentrations (0.05, 0.1, and 0.5%), it maintains a notable average Faradaic efficiency of 93.6% and NH 3 yield rates (556, 948, and 3120 μg cm –2 h –1 respectively) among the highest reported under such challenging conditions. Furthermore, the catalyst demonstrated durability with >85 h of stable operation, and a cumulative NH 3 production reaching the gram-scale, showcasing its practical potential. Techno-economic analysis (TEA) revealed that NORR with Co SA-NPs could achieve zero-cost NO treatment and even generate profit, compared to traditional NH 3 –SCR.
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