Influence of barium and cerium oxides on alumina supported Pd catalysts for hydrocarbon combustion

被引:35
作者
Liotta, LF
Deganello, G
Sannino, D
Gaudino, MC
Ciambelli, P
Gialanella, S
机构
[1] CNR, ISMN, Ist Studio Mat Nanostrutturaki, Sezione Palermo, I-90146 Palermo, Italy
[2] Univ Viale Sci, Dipartimento Chim Inorgan, I-90128 Palermo, Italy
[3] Univ Salerno, Dipartimento Ingn Chim & Alimentare, Fisciano, SA, Italy
[4] Univ Trent, Dipartimento Ingn Mat, I-38050 Trent, Italy
关键词
palladium; ceria-alumina-baria; thermal stabilization; methane and ethene combustion;
D O I
10.1016/S0926-860X(02)00029-7
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 effects of baria and ceria additions to alumina-supported palladium catalysts have been investigated. Two series of binary Al2O3-BaO and ternary oxides Al2O3-CeO2-BaO were prepared using a sol-gel method and then characterized, after high-temperature treatments, by XRD, BET, TG, TEM and EDXS analyses. The influence of baria and ceria on the thermal stability and morphology of the supports was examined. A baria content of 12 wt.% appears the most effective for alumina stabilization. Palladium catalysts were prepared by impregnation method using Pd(NH3)(4)(NO3)(2) and were characterized by XRD and TEM. The catalysts showed high activity in the total oxidation of methane, in the temperature range 200-600degreesC. The methane oxidation activity of both PdAlBa and PdAlCeBa series increases with the specific surface area (SSA), ceria addition does not produce significant differences of activities, The ethene combustion was studied, also, on the series PdAlCeBa, as a model structure-sensitive reaction chosen to investigate possible palladium-ceria interactions. The reactivity was compared with that of PdAlBa catalyst with the same baria content. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:217 / 227
页数:11
相关论文
共 29 条
[1]  
Amato I., 1975, SINTERING CATALYSIS, P187
[2]   The effect of temperature on a ceria-alumina-baria-cordierite monolith combination under oxidising and reducing conditions [J].
Angove, DE ;
Cant, NW ;
French, DH ;
Kinealy, K .
APPLIED CATALYSIS A-GENERAL, 2000, 194 :27-34
[3]  
[Anonymous], XRAY DIFFRACTION PRO
[4]   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
[5]  
BURCH R, 2000, CATAL TODAY, V62, P51
[6]  
Chong K. R., 1999, CATAL TODAY, V47, P141
[7]   The effect of digestion on the surface area and porosity of alumina [J].
Chuah, GK ;
Jaenicke, S ;
Xu, TH .
MICROPOROUS AND MESOPOROUS MATERIALS, 2000, 37 (03) :345-353
[8]   Catalyst microstructure and methane oxidation reactivity during the Pd⇆PdO transformation on alumina supports [J].
Datye, AK ;
Bravo, J ;
Nelson, TR ;
Atanasova, P ;
Lyubovsky, M ;
Pfefferle, L .
APPLIED CATALYSIS A-GENERAL, 2000, 198 (1-2) :179-196
[9]  
DOLLIMORE D, 1964, J APPL CHEM, V14, P109
[10]  
DUPLAN JL, 1991, APPL CATAL, V67, P325