分解
催化作用
氢
化学工程
膜反应器
制氢
氨
氧化钇稳定氧化锆
材料科学
膜
化学
立方氧化锆
有机化学
复合材料
陶瓷
生物化学
工程类
作者
Zhenyu Zhang,Simona Liguori,Thomas F. Fuerst,J. Douglas Way,Colin A. Wolden
出处
期刊:ACS Sustainable Chemistry & Engineering
[American Chemical Society]
日期:2019-02-27
卷期号:7 (6): 5975-5985
被引量:113
标识
DOI:10.1021/acssuschemeng.8b06065
摘要
Liquid ammonia is a high-density (17.7 wt %) hydrogen carrier with a well-established production and distribution infrastructure. Efficient decomposition and purification are essential for its use as a hydrogen-storage material. Here we demonstrate the production of high-purity (>99.7%) H2 from NH3 using a catalytic membrane reactor (CMR) in which a Ru catalyst is impregnated within a porous yttria-stabilized zirconia (YSZ) tube coated with a thin, 6 μm Pd film by electroless deposition. The intimate proximity of catalyst and membrane eliminates transport resistances that limit performance in the conventional packed-bed membrane reactor (PBMR) configuration. The addition of a Cs promoter enabled complete NH3 conversion at temperatures as low as 400 °C, exceeding equilibrium constraints without the need for a sweep gas. A reactor model was developed that captured CMR performance with high fidelity. NH3 decomposition was observed to follow first-order kinetics due to efficient H2 removal. Relative to a comparable PBMR, the Ru loading in the CMR was reduced an order of magnitude and the H2 recovery increased 35%, enabling record volumetric productivity rates (>30 mol m–3 s–1) that validate its promise for efficient, compact H2 delivery from ammonia.
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