Efficient catalytic abatement of greenhouse gases: Methane reforming with CO2 using a novel and thermally stable Rh-CeO2 catalyst

被引:126
作者
Djinovic, Petar [1 ,2 ]
Batista, Jurka [1 ,2 ]
Pintar, Albin [1 ,2 ]
机构
[1] Natl Inst Chem, SI-1001 Ljubljana, Slovenia
[2] Ctr Excellence Low Carbon Technol, SI-1001 Ljubljana, Slovenia
关键词
Greenhouse gas abatement; Methane dry reforming; Hydrogen; Syngas; Rh-CeO2; catalyst; CARBON-DIOXIDE; HYDROGEN-PRODUCTION; MESOPOROUS SILICA; COPRECIPITATION; PLATINUM; SUPPORT; SYNGAS; OXIDE; CERIA; CH4;
D O I
10.1016/j.ijhydene.2011.10.107
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
2% Rh-CeO2 catalyst was synthesized using the hard template method and characterized by means of N-2 adsorption/desorption, XRD and H-2-TPR methods. The prepared powdered catalyst exhibited high thermal stability and high surface area with negligible sintering during 24-h exposure to 973 K in an inert atmosphere. During the temperature programmed methane dry reforming reaction between 473 and 1073 K, an increase in the molar H-2/CO ratio from 0.3 at 623 K to as high as 0.96 at 1073 K was observed. Besides H-2 and CO, H2O was identified among reaction products, originating from the simultaneously occurring reverse water-gas shift reaction. During the isothermal test performed at 923 K, the 2% Rh-CeO2 catalyst exhibited stable performance and produced syngas with the average H-2/CO ratio equal to 0.62. A relative drop of catalyst activity equal to 11% was observed within 70-h time on stream at 1023 K, with the average H-2/CO ratio at the reactor outlet equal to 0.71. Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:2699 / 2707
页数:9
相关论文
共 39 条
[1]   REVERSIBILITY OF HYDROGEN CHEMISORPTION ON A CERIA-SUPPORTED RHODIUM CATALYST [J].
BERNAL, S ;
CALVINO, JJ ;
CIFREDO, GA ;
RODRIGUEZIZQUIERDO, JM ;
PERRICHON, V ;
LAACHIR, A .
JOURNAL OF CATALYSIS, 1992, 137 (01) :1-11
[2]   The state of zirconia supported platinum catalysts for CO2/CH4 reforming [J].
Bitter, JH ;
Seshan, K ;
Lercher, JA .
JOURNAL OF CATALYSIS, 1997, 171 (01) :279-286
[3]   Catalytic reforming of methane with carbon dioxide over nickel catalysts .2. Reaction [J].
Bradford, MCJ ;
Vannice, MA .
APPLIED CATALYSIS A-GENERAL, 1996, 142 (01) :97-122
[4]   Negative Net CO2 Emissions from Oxy-Decarbonization of Biogas to H2 [J].
Budzianowski, Wojciech M. .
INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2010, 8
[5]   An oxy-fuel mass-recirculating process for H2 production with CO2 capture by autothermal catalytic oxyforming of methane [J].
Budzianowski, Wojciech M. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (14) :7454-7469
[6]   Autothermal reforming of ethanol for hydrogen production over an Rh/CeO2 catalyst [J].
Cai, Weijie ;
Wang, Fagen ;
Van Veen, A. C. ;
Provendier, H. ;
Mirodatos, C. ;
Shen, Wenjie .
CATALYSIS TODAY, 2008, 138 (3-4) :152-156
[7]  
Djinovic P, 2009, ACTA CHIM SLOV, V56, P868
[8]   Comparison of water-gas shift reaction activity and long-term stability of nanostructured CuO-CeO2 catalysts prepared by hard template and co-precipitation methods [J].
Djinovic, Petar ;
Batista, Jurka ;
Levec, Janez ;
Pintar, Albin .
APPLIED CATALYSIS A-GENERAL, 2009, 364 (1-2) :156-165
[9]   A transient kinetic study of the carbon dioxide reforming of methane over supported Ru catalysts [J].
Ferreira-Aparicio, P ;
Márquez-Alvarez, C ;
Rodríguez-Ramos, I ;
Schuurman, Y ;
Guerrero-Ruiz, A ;
Mirodatos, C .
JOURNAL OF CATALYSIS, 1999, 184 (01) :202-212
[10]   TEMPERATURE-PROGRAMMED DESORPTION OF CO AND CO2 FROM PT/CEO2 - AN IMPORTANT ROLE FOR LATTICE OXYGEN IN CO OXIDATION [J].
JIN, T ;
OKUHARA, T ;
MAINS, GJ ;
WHITE, JM .
JOURNAL OF PHYSICAL CHEMISTRY, 1987, 91 (12) :3310-3315