Efficient Ammonia Decomposition in a Catalytic Membrane Reactor To Enable Hydrogen Storage and Utilization

被引:91
|
作者
Zhang, Zhenyu [1 ]
Liguori, Simona [1 ,2 ]
Fuerst, Thomas F. [1 ]
Way, J. Douglas [1 ]
Wolden, Colin A. [1 ]
机构
[1] Colorado Sch Mines, Dept Chem & Biol Engn, Golden, CO 80401 USA
[2] Worcester Polytech Inst, Dept Chem Engn, Worcester, MA 01609 USA
基金
美国国家科学基金会;
关键词
Ammonia; Hydrogen; Membrane reactor; Model; Kinetics; Purification; Process intensification; NH3; DECOMPOSITION; H-2; PRODUCTION; COMPOSITE MEMBRANES; GAS; GENERATION; KINETICS; RU; CHEMISTRY;
D O I
10.1021/acssuschemeng.8b06065
中图分类号
O6 [化学];
学科分类号
0703 ;
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%) H-2 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 mu m 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 degrees 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 H-2 removal. Relative to a comparable PBMR, the Ru loading in the CMR was reduced an order of magnitude and the H-2 recovery increased 35%, enabling record volumetric productivity rates (>30 mol m(-3) s(-1)) that validate its promise for efficient, compact H-2 delivery from ammonia.
引用
收藏
页码:5975 / 5985
页数:21
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