Reduction of NOx over various Fe/zeolite catalysts

被引:83
作者
Chen, HY [1 ]
Wang, X [1 ]
Sachtler, WMH [1 ]
机构
[1] Northwestern Univ, Dept Chem, Ctr Catalysis & Surface Sci, VN Ipatieff Lab, Evanston, IL 60208 USA
关键词
SCR of No-x; Fe/zeolite catalysts; physical mixture catalysts; site accessibility in zeolite;
D O I
10.1016/S0926-860X(99)00364-6
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
A systematic comparison was made of the catalytic activity of a variety of Fe/zeolite catalysts in the selective catalytic reduction of NOx with iso-butane or propane, both with dry and wet feeds. All catalysts were prepared by subliming FeCl3 vapor onto the H-form of the zeolite, followed by Cl removal. The activities decrease in the order Fe/BEA > Fe/MFI >> Fe/FER > Fe/MOR approximate to Fe/Y. These differences are rationalized in terms of our mechanistic model and the known pore geometry of the zeolites. FT-TR shows that some Fe loaded narrow pore zeolites are able to oxidize NO to NO2 and form NOy. chemisorption complexes, but unable to let iso-butane enter the pores. Unlike some wider pore zeolites that become covered by a carbonaceous deposit at low temperature, these materials retain their high activity for NO oxidation. Mixtures of Fe loaded wide and narrow pore zeolites, therefore, lead to higher steady-state activities at low temperature than single catalysts. In particular, the combination of Fe/MFI with Fe/FER displays a spectacular activity enhancement. (C) 2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:159 / 168
页数:10
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