Selective catalytic reduction of NO under lean conditions by methane and propane over indium/cerium-promoted zeolites

被引:59
作者
Berndt, H
Schütze, FW
Richter, M
Sowade, T
Grünert, W
机构
[1] Inst Angew Chem Berlin Adlershof eV, D-12489 Berlin, Germany
[2] Ruhr Univ Bochum, Lehrstuhl Tech Chem, D-44780 Bochum, Germany
关键词
SCR of NOx; composite catalyst; ceria; indium zeolite; methane; propane; water influence;
D O I
10.1016/S0926-3373(02)00126-1
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
The potential of zeolites MFI and MOR promoted by In and Ce as catalysts for the SCR of NOx by methane and propane was studied, particularly considering their stability in the presence of water vapour. A preparation route for a zeolite-based Ce/In composite catalyst was developed and the influence of several reaction conditions was studied to optimise the catalyst performance. TPR and FTIRS were used to check the preparation steps and to investigate the catalyst structure. These data were used together with results from characterisation by X-ray-based techniques to describe the generation and catalytic function of different indium species ((InO)(+), In2O3 Cluster) and their co-operation with ceria in the composite catalyst. The primary role of the CeOx promoter is to catalyse the oxidation of NO to NO2. Probably, NO2 reacts with methane on Lewis-acidic and redoxactive (InO)(+) species, but the further reaction of the intermediate formed needs the presence of residual Bronsted-acid sites. SCR of NOx by methane or propane is still partially inhibited by adsorption competition between water and the hydrocarbons on the (InO)(+) species. Higher SCR activity could be achieved by increased hydrocarbon partial pressure in the feed, shifting presumably the competitive adsorption to enhanced adsorption of methane and propane, respectively. Furthermore, combining of methane and propane as reductants opens an opportunity to broaden the 'temperature window' for the SCR of NOx. Different influence of hydrothermal ageing was obtained with methane and propane, respectively, as reducing agent. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:51 / 67
页数:17
相关论文
共 22 条
[1]   The reactions of possible intermediates in the selective catalytic reduction of nitrogen oxides by hydrocarbons [J].
Cant, NW ;
Cowan, AD ;
Liu, IOY ;
Satsuma, A .
CATALYSIS TODAY, 1999, 54 (04) :473-482
[2]  
ERTL G, 1997, HDB HETEROGENEOUS CA, V4, pCH1
[3]  
JAHN M, 1999, THESIS TU BERLIN GER
[4]  
Kanazirev V., 1993, Proc. 9th Int. Zeolite Conf, P461
[5]   Promotive effect of additives to In/H-ZSM-5 catalyst for selective reduction of nitric oxide with methane in the presence of water vapor [J].
Kikuchi, E ;
Ogura, M ;
Aratani, N ;
Sugiura, Y ;
Hiromoto, S ;
Yogo, K .
CATALYSIS TODAY, 1996, 27 (1-2) :35-40
[6]   Selective reduction of nitric oxide with methane on gallium and indium containing H-ZSM-5 catalysts: Formation of active sites by solid-state ion exchange [J].
Kikuchi, E ;
Ogura, M ;
Terasaki, I ;
Goto, Y .
JOURNAL OF CATALYSIS, 1996, 161 (01) :465-470
[7]   SELECTIVE CATALYTIC REDUCTION OF NITROGEN MONOXIDE BY METHANE ON ZEOLITE CATALYSTS IN AN OXYGEN-RICH ATMOSPHERE [J].
KIKUCHI, E ;
YOGO, K .
CATALYSIS TODAY, 1994, 22 (01) :73-86
[8]   On the promotion of Ag-ZSM-5 by cerium for the SCR of NO by methane [J].
Li, ZJ ;
Flytzani-Stephanopoulos, M .
JOURNAL OF CATALYSIS, 1999, 182 (02) :313-327
[9]   Selective catalytic reduction of NO by methane over CeO2-zeolite catalysts -: Active sites and reaction steps [J].
Liese, T ;
Löffler, E ;
Grünert, W .
JOURNAL OF CATALYSIS, 2001, 197 (01) :123-130
[10]   Study of the reductive solid-state ion exchange of indium into an NH4-beta zeolite [J].
Mihalyi, RM ;
Beyer, HK ;
Mavrodinova, V ;
Minchev, C ;
Neinska, Y .
MICROPOROUS AND MESOPOROUS MATERIALS, 1998, 24 (4-6) :143-151