Ammonia Decomposition in Catalytic Membrane Reactors: Simulation and Experimental Studies

被引:62
|
作者
Li, Gang [1 ]
Kanezashi, Masakoto [1 ]
Yoshioka, Tomohisa [1 ]
Tsuru, Toshinori [1 ]
机构
[1] Hiroshima Univ, Dept Chem Engn, Higashihiroshima 7398527, Japan
关键词
ammonia decomposition; catalytic membrane reactor; silica membrane; COx-free hydrogen; hydrogen production; COX-FREE HYDROGEN; CONCENTRATION POLARIZATION; SILICA MEMBRANES; STEAM; DEHYDROGENATION; PERMEATION; KINETICS; PERFORMANCE; GENERATION; NH3;
D O I
10.1002/aic.13794
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Catalytic decomposition of NH3 with H-2-selective microporous silica membranes for COx-free hydrogen production was studied theoretically and experimentally. The simulation study shows that NH3 conversion, H-2 yield and H-2 purity increase with the Damkohler number (Da), and their improvement is affected by the effect of H-2 extraction as well as NH3 and N-2 permeation through the membranes. The experimental study of NH3 decomposition was carried out in a bimodal catalytic membrane reactor (BCMR), consisting of a bimodal catalytic support and a H-2-selective silica layer. Catalytic membranes showed H-2 permeances of 6.2-9.8 x 10(-7) mol m(-2) s(-1) Pa-1, with H-2/NH3 and H-2/N-2 permeance ratios of 110-200 and 200-700, respectively, at 773 K. The effect of operating conditions on membrane reactor performance with respect to NH3 conversion, H-2 yield and H-2 purity was investigated, and the results were in agreement with those calculated by the proposed simulation model. (C) 2012 American Institute of Chemical Engineers AIChE J, 59: 168-179, 2013
引用
收藏
页码:168 / 179
页数:12
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