Dual-site Pd/perovskite monolithic catalysts for methane catalytic combustion

被引:25
作者
Cimino, S
Lisi, L
Pirone, R
Russo, G
机构
[1] CNR, Ist Ric Combust, I-80125 Naples, Italy
[2] Univ Naples Federico II, Dipartimento Ingn Chim, Naples, Italy
关键词
D O I
10.1021/ie049656h
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Novel monolithic catalysts for the high-temperature combustion of methane have been developed with a dual-site nature, to combine low and high temperature activity within a single system and widen its operating range. Such catalysts are based on strongly interacting Pd and LaMnO3 active phases supported onto La/gamma-alumina and applied as a thick washcoat on ceramic honeycombs. Optimization of the preparation procedure and catalyst characterization were performed with respect to the effects of Pd deposition method, catalyst activation strategy, and thermal history in comparison with previously developed catalysts based only on supported perovskite. Extensive methane combustion tests (steady state and transient) were run under both isothermal and autothermal lean premixed conditions in order to study intrinsic oxidation activity, light-off behavior, and real life performance in the middle to high temperature range. Experimental evidence is presented for improved activity, stability, and durability of the catalytic system, and for a self-regenerative behavior of Pd active sites through reversible interaction with perovskite lattice. Implications of novel combined catalyst functionalities are addressed with respect to operation of a fully catalytic burner.
引用
收藏
页码:6670 / 6679
页数:10
相关论文
共 37 条
[11]   Catalytic combustion of methane over palladium-based catalysts [J].
Ciuparu, D ;
Lyubovsky, MR ;
Altman, E ;
Pfefferle, LD ;
Datye, A .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 2002, 44 (04) :593-649
[12]   Preparation of axially non-uniform Pd catalytic monoliths by chemical vapour deposition [J].
Cominos, V ;
Gavriilidis, A .
APPLIED CATALYSIS A-GENERAL, 2001, 210 (1-2) :381-390
[13]   Catalytic combustion gas turbine systems: The preferred technology for low emissions electric power production and co-generation [J].
DallaBetta, RA .
CATALYSIS TODAY, 1997, 35 (1-2) :129-135
[14]  
DALLABETTA RA, 1994, Patent No. 5326253
[15]   Temperature excursions during the transient behaviour of high temperature catalytic combustion monoliths [J].
Di Benedetto, A ;
Cimino, S ;
Pirone, R ;
Russo, G .
CATALYSIS TODAY, 2003, 83 (1-4) :171-182
[16]   Oxidative dehydrogenation of ethane over a perovskite-based monolithic reactor [J].
Donsì, F ;
Pirone, R ;
Russo, G .
JOURNAL OF CATALYSIS, 2002, 209 (01) :51-61
[17]   Deactivation of palladium catalyst in catalytic combustion of methane [J].
Euzen, P ;
Le Gal, JH ;
Rebours, B ;
Martin, G .
CATALYSIS TODAY, 1999, 47 (1-4) :19-27
[18]   Status and perspectives of catalytic combustion for gas turbines [J].
Forzatti, P .
CATALYSIS TODAY, 2003, 83 (1-4) :3-18
[19]   Effect of ceria on palladium supported catalysts for high temperature combustion of CH4 under lean conditions [J].
Groppi, G ;
Cristiani, C ;
Lietti, L ;
Ramella, C ;
Valentini, M ;
Forzatti, P .
CATALYSIS TODAY, 1999, 50 (02) :399-412
[20]   The palladium catalysed oxidation of methane: reaction kinetics and the effect of diffusion barriers [J].
Hayes, RE ;
Kolaczkowski, ST ;
Li, PKC ;
Awdry, S .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (16) :4815-4835