Regeneration and sulfur poisoning behavior of In/H-BEA catalyst for NOx reduction by CH4

被引:38
|
作者
Pan, Hua [1 ]
Jian, Yanfei [1 ]
Yu, Yanke [1 ]
He, Chi [1 ]
Shen, Zhenxing [1 ]
Liu, Hongxia [1 ]
机构
[1] Xi An Jiao Tong Univ, Dept Environm Sci & Engn, Xian 710049, Peoples R China
基金
中国国家自然科学基金;
关键词
Sulfur poisoning; Regeneration; ln/H-BEA; NOx reduction by CH4; Hydrogen reduction; SELECTIVE REDUCTION; ACTIVE-SITES; NITRIC-OXIDE; METHANE; SCR; INDIUM; SO2; MECHANISM; ZEOLITE; STORAGE;
D O I
10.1016/j.apsusc.2016.12.201
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Sulfur poisoning and regeneration behavior of In/H-BEA catalyst were carried out in NOx reduction by CH4. In/H-BEA catalyst exhibited a poor resistance to sulfur dioxide after addition of 200 ppm SO2 and 10 vol.% H2O into NO reduction with CH4 at 450 degrees C for 45 h. Sulfur poisoning of In/H-BEA was attributed to the inhibition of NOx adsorption on Bronsted acid sites, suppression of reaction intermediates generation on the active sites, and the formation of surface sulfate species. The formation of surface sulfate reduced the availability of surface active sites, blocked the pore structure and decreased the surface area of catalyst. These changes in chemical and textural properties resulted in a severe loss in the activity of sulfated In/H-BEA catalyst for NO reduction with CH4. H-2 reduction is a promising technology for regeneration of In/H-BEA deactivated by SO2 for removing NOx from lean-burn and diesel exhausts. Indium sulfate could be reduced by H-2 to InO+ with In2O3 and In(OH)(2)(+) as the intermediates. The optimal parameters of H2 reduction was regeneration temperature of 400 degrees C and regeneration time of 60 min which completely recovered the catalytic activity of In/H-BEA. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:120 / 126
页数:7
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