化学
氨
膜
分解
热分解
化学工程
氢
制氢
流出物
产量(工程)
氨生产
级联
碳纤维
无机化学
选择性
沉积(地质)
化学分解
氢气净化器
渗滤
膜技术
热解
铵
环境化学
作者
Shengyan Meng,Chen Yuxin,Zhaolun Cui,Yang Gu,Hongyan Xiao,Yi Liu,Shijie Yang,Junze Li,Kunpeng Yu,Chen Wang,Wenjing Hu,Hongbo Xie,Xiaoxia Gao,Wei Shao,Gaohong He,Jun Cai,Zhi Liu,Hui Li,Yanhui Yi,Yi Liu
摘要
Ammonia (NH3) is a principal carbon-free hydrogen (H2) carrier, yet its decomposition via conventional thermocatalysis is restricted by kinetically demanding high temperatures. Integrating the reaction with in situ product removal to achieve high decomposition efficiency under mild conditions presents a formidable challenge. Here, we report a plasma-enhanced dual-membrane ammonia decomposition system (PEDMADS) that synergistically couples dielectric barrier discharge (DBD), a highly dispersed atomic layer deposition (ALD)-synthesized Ru/SiO2 catalyst, and an integrated ultrathin Pd membrane (1.8 μm) to enable a high H2 space-time yield of 1567 mmol g-1 h-1 at 400 °C. Furthermore, a downstream cascade of high-performance Silicalite-1 (S-1) membranes achieved energy-efficient NH3 recovery, exhibiting unprecedented NH3/H2 and NH3/N2 separation factors of 686 and 7076 under ambient conditions. Molecular dynamics simulations revealed this selectivity arose from a preferential adsorption-driven molecular sieving mechanism. The five-stage cascade reduced the effluent NH3 concentration from 24.1% to below 4%, achieving 87% removal efficiency. Techno-economic analysis indicated a levelized cost of 0.92 $/kg H2 with a 95.9% carbon footprint reduction compared to the conventional thermal process, thus offering a compelling blueprint for a sustainable ammonia-hydrogen economy.
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