Deep oxidation of methane on particles derived from YSZ-supported Pd-Pt-(O) coatings synthesized by Pulsed Filtered Cathodic Arc

被引:7
作者
Horwat, D. [1 ,2 ]
Endrino, J. L. [2 ,3 ]
Boreave, A. [4 ]
Karoum, R. [4 ]
Pierson, J. F. [1 ]
Weber, S. [5 ]
Anders, A. [2 ]
Vernoux, Ph. [4 ]
机构
[1] Ecole Mines, Inst Jean Lamour, Dept CP2S, F-54042 Nancy, France
[2] Univ Calif Berkeley, Lawrence Berkeley Lab, Plasma Applicat Grp, Berkeley, CA 94720 USA
[3] CSIC, Inst Ciencias Mat Madrid, E-28049 Madrid, Spain
[4] Univ Lyon 1, CNRS, UMR 5256, IRCELYON, F-69626 Villeurbanne, France
[5] Ecole Mines, CC MEM, Inst Jean Lamour, F-54042 Nancy, France
关键词
Total oxidation of methane; Palladium oxide; YSZ supported catalysts; Particles; Cathodic arc deposition; PALLADIUM CATALYSTS; ELECTROCHEMICAL PROMOTION; COMBUSTION; TEMPERATURE; REACTIVITY; OXYGEN;
D O I
10.1016/j.catcom.2009.03.008
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
Methane total oxidation was studied between 250 and 800 degrees C in a specific quartz reactor for Pd, PdOy, Pd0.6Pt0.4Oy and Pd0.4Pt0.6Oy thin films deposited on yttria stabilized zirconia (YSZ) substrates. Pt containing. films exhibited poor activity and a rapid thermal decomposition. Pd and PdOy films showed good activity and transformed to particles dispersed on the YSZ substrates. The higher reaction rate of PdOy films was explained by a better dispersion of the catalyst. A drop of the reaction rate was observed when the temperature exceeded 735 degrees C and 725 degrees C for initially Pd and PdOy, respectively, which can be associated with the decomposition of PdO into Pd and O-2. The good cycling stability and catalytic efficiency of the latter films render it promising for the pollution control in methane combustion. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:1410 / 1413
页数:4
相关论文
共 31 条
[1]   Filtered cathodic arc deposition with ion-species-selective bias [J].
Anders, Andre ;
Pasaja, Nitisak ;
Sansongsiri, Sakon .
REVIEW OF SCIENTIFIC INSTRUMENTS, 2007, 78 (06)
[2]  
Anders A, 2008, SPRINGER SER ATOM OP, V50, P1, DOI 10.1007/978-0-387-79108-1_1
[3]  
Anders S, 1995, SURF COAT TECH, V76, P167, DOI 10.1016/0257-8972(95)02508-1
[4]  
BOYLET A, 2008, APPL CATAL B-ENVIRON, P237
[5]   INVESTIGATION OF THE ACTIVE STATE OF SUPPORTED PALLADIUM CATALYSTS IN THE COMBUSTION OF METHANE [J].
BURCH, R ;
URBANO, FJ .
APPLIED CATALYSIS A-GENERAL, 1995, 124 (01) :121-138
[6]   Factors affecting the catalytic activity of Pd/ZrO2 for the combustion of methane [J].
Carstens, JN ;
Su, SC ;
Bell, AT .
JOURNAL OF CATALYSIS, 1998, 176 (01) :136-142
[7]   Supported palladium catalysts in environmental catalytic technologies for gaseous emissions [J].
Centi, G .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2001, 173 (1-2) :287-312
[8]   Application of catalytic combustion to a 1.5 MW industrial gas turbine [J].
Dalla Betta, RA ;
Rostrup-Nielsen, T .
CATALYSIS TODAY, 1999, 47 (1-4) :369-375
[9]   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
[10]   Structure and properties of silver-containing a-C(H) films deposited by plasma immersion ion implantation [J].
Endrino, J. L. ;
Galindo, R. Escobar ;
Zhang, H. -S. ;
Allen, M. ;
Gago, R. ;
Espinosa, A. ;
Anders, A. .
SURFACE & COATINGS TECHNOLOGY, 2008, 202 (15) :3675-3682