Catalytic evaluation of perovskite-type oxide LaNi1-xRuxO3 in methane dry reforming

被引:100
作者
de Arauj, Genira Carneiro [1 ,2 ]
de Lima, Sania Maria [3 ]
Assaf, Jose Mansur [3 ]
Pena, Miguel Antonio [2 ]
Garcia Fierro, Jose Luis [2 ]
Rangel, Maria do Carmo [1 ]
机构
[1] Univ Fed Bahia, Grp Estudos Cinet & Catalise, BR-40170290 Salvador, BA, Brazil
[2] CSIC, Inst Catalisis & Petr Quim, E-28049 Madrid, Spain
[3] Univ Fed Sao Carlos, Lab Catalise, Departmento Engn Quim, Sao Paulo, Brazil
关键词
perovskite; dry reforming; methane;
D O I
10.1016/j.cattod.2007.12.049
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The methane reforming with carbon dioxide (dry reforming) has been proposed as one of the most promising technologies for producing hydrogen by the use of two greenhouse gases. However, undesirable coke formation is the crucial issue to develop efficient catalysts for the reaction. In order to find alternative catalysts, which can be more resistant against coke deactivation, perovskite-type oxides LaRuxNi1-xO3 (0.0 < x < 1.0) were studied in this work. Samples were prepared by thermal decomposition of amorphous citrate precursors followed by heating at 800 or 1000 degrees C, for 12 h, in air. The solids were characterized by X-ray diffraction, temperature-programmed reduction, temperature-programmed desorption, specific surface area measurements and X-ray photoelectron spectroscopy. The catalysts were reduced under hydrogen and tested in methane dry reforming at 1 atm and 750 degrees C. The coke produced was characterized by thermogravimetry, carbon measurement and scanning and transmission electron microscopy. The oxide precursors showed low specific surface areas and different reducing behavior. All catalysts were active in the reaction. They all produced filamentous coke but it was not harmful to the catalysts. Nickel is more active and selective to hydrogen than ruthenium but the later improved the stability of the catalysts decreasing coke formation. The most promising catalyst was the LaNi0.8Ru0.2O3 sample, which was the most resistant against coke deposition. (c) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:129 / 135
页数:7
相关论文
共 35 条
[1]   Gasification behavior of catalytic filamentous carbon [J].
Avdeeva, LB ;
Reshetenko, TV ;
Fenelonov, VB ;
Chuvilin, AL ;
Ismagilov, ZR .
CARBON, 2004, 42 (12-13) :2501-2507
[2]   Iron-containing catalysts of methane decomposition: accumulation of filamentous carbon [J].
Avdeeva, LB ;
Reshetenko, TV ;
Ismagilov, ZR ;
Likholobov, VA .
APPLIED CATALYSIS A-GENERAL, 2002, 228 (1-2) :53-63
[3]   Support effect in supported Ni catalysts on their performance for methane partial oxidation [J].
Barbero, J ;
Peña, MA ;
Campos-Martin, JM ;
Fierro, JLG ;
Arias, PL .
CATALYSIS LETTERS, 2003, 87 (3-4) :211-218
[4]  
Cao L, 1997, STUD SURF SCI CATAL, V107, P467
[5]   THE SURFACE-CHEMISTRY OF SOME PEROVSKITE OXIDES [J].
CRESPIN, M ;
HALL, WK .
JOURNAL OF CATALYSIS, 1981, 69 (02) :359-370
[6]   DEACTIVATION OF STEAM-REFORMING MODEL CATALYSTS BY COKE FORMATION .2. PROMOTION WITH POTASSIUM AND EFFECT OF WATER [J].
DEMICHELI, MC ;
DUPREZ, D ;
BARBIER, J ;
FERRETTI, OA ;
PONZI, EN .
JOURNAL OF CATALYSIS, 1994, 145 (02) :437-449
[7]   DEACTIVATION OF STEAM-REFORMING MODEL CATALYSTS BY COKE FORMATION .1. KINETICS OF THE FORMATION OF FILAMENTOUS CARBON IN THE HYDROGENOLYSIS OF CYCLOPENTANE ON NI/AL2O3 CATALYSTS [J].
DUPREZ, D ;
DEMICHELI, MC ;
MARECOT, P ;
BARBIER, J ;
FERRETTI, OA ;
PONZI, EN .
JOURNAL OF CATALYSIS, 1990, 124 (02) :324-335
[8]   Double perovskite oxides A2FeMoO6-δ (A = Ca, Sr and Ba) as catalysts for methane combustion [J].
Falcón, H ;
Barbero, JA ;
Araujo, G ;
Casais, MT ;
Martínez-Lope, MJ ;
Alonso, JA ;
Fierro, JLG .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2004, 53 (01) :37-45
[9]   SrFeO3-δ perovskite oxides:: Chemical features and performance for methane combustion [J].
Falcón, H ;
Barbero, JA ;
Alonso, JA ;
Martínez-Lope, MJ ;
Fierro, JLG .
CHEMISTRY OF MATERIALS, 2002, 14 (05) :2325-2333
[10]   Production of synthesis gas by steam- and CO2-reforming of natural gas [J].
Froment, GF .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2000, 163 (1-2) :147-156