The deactivation study of Co-Ru-Zr catalyst depending on supports in the dry reforming of carbon dioxide

被引:35
作者
Lee, Ji-Hye [1 ,2 ]
You, Young-Woo [2 ]
Ahn, Hong-Chan [2 ]
Hong, Ji-Sook [2 ]
Kim, Seong-Bo [2 ]
Chang, Tae-Sun [2 ]
Suh, Jeong-Kwon [1 ,2 ]
机构
[1] Univ Sci & Technol, Taejon 305350, South Korea
[2] Korea Res Inst Chem Technol, Environm & Resource Proc Res Ctr, Taejon 305600, South Korea
关键词
Dry reforming; Carbon deposition; Gamma-alumina; Silica; Magnesia; Support; FISCHER-TROPSCH SYNTHESIS; PROMOTED NI CATALYSTS; BIMETALLIC CATALYSTS; METHANE; COBALT; HYDROGENATION; CO/SIO2; METALS; MN;
D O I
10.1016/j.jiec.2013.03.036
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Carbon dioxide reforming of methane was performed over Co-Ru-Zr catalyst (0.4 wt% Ru added, calcined at 400 degrees C) with different supports (SiO2, gamma-Al2O3 and MgO) in order to study their deactivation. The Co-Ru-Zr/gamma-Al2O3 showed the highest activity at first, but severe deactivation was observed due to carbon deposition. Co-Ru-Zr/MgO exhibited low activity because of its low specific surface area. However, the high conversions could be obtained in Co-Ru-Zr/SiO2, and activity was kept almost constantly for 500 h reaction. The characteristics of the catalysts, before and after the reaction, were investigated employing BET, XRD, TPR, TGA-DTA and TEM. (C) 2013 The Korean Society of Industrial and Engineering Chemistry. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:284 / 289
页数:6
相关论文
共 25 条
[1]   A novel Co/SiO2 catalyst for hydrogenation [J].
Backman, LB ;
Rautiainen, A ;
Krause, AOI ;
Lindblad, M .
CATALYSIS TODAY, 1998, 43 (1-2) :11-19
[2]   Effect of MgO additive on catalytic properties of Co/SiO2 in the dry reforming of methane [J].
Bouarab, R ;
Akdim, O ;
Auroux, A ;
Cherifi, O ;
Mirodatos, C .
APPLIED CATALYSIS A-GENERAL, 2004, 264 (02) :161-168
[3]  
Chun H. J., 2002, INTRO CATALYST
[4]  
Flego C., 2001, CATAL COMMUN, V2, P43
[5]   Effect of MgO addition on the basicity of Ni/ZrO2 and on its catalytic activity in carbon dioxide reforming of methane [J].
Garcia, Veronica ;
Fernandez, Jhon J. ;
Ruiz, Wilson ;
Mondragon, Fanor ;
Moreno, Andres .
CATALYSIS COMMUNICATIONS, 2009, 11 (04) :240-246
[6]   Transient study of the dry reforming of methane over Pt supported on different γ-Al2O3 [J].
Garcia-Dieguez, M. ;
Pieta, I. S. ;
Herrera, M. C. ;
Larrubia, M. A. ;
Malpartida, I. ;
Alemany, L. J. .
CATALYSIS TODAY, 2010, 149 (3-4) :380-387
[7]   Deactivation study on a coprecipitated Fe-Cu-K-Al catalyst in CO2 hydrogenation [J].
Hong, JS ;
Hwang, JS ;
Jun, KW ;
Sur, JC ;
Lee, KW .
APPLIED CATALYSIS A-GENERAL, 2001, 218 (1-2) :53-59
[8]   Production of synthesis gas via methane reforming with CO2 on noble metals and small amount of noble-(Rh-) promoted Ni catalysts [J].
Hou, ZY ;
Chen, P ;
Fang, HL ;
Zheng, XM ;
Yashima, T .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2006, 31 (05) :555-561
[9]   Small amounts of Rh-promoted Ni catalysts for methane reforming with CO2 [J].
Hou, ZY ;
Yashima, T .
CATALYSIS LETTERS, 2003, 89 (3-4) :193-197
[10]   Auto-thermal and dry reforming of landfill gas over a Rh/γAl2O3 monolith catalyst [J].
Kohn, McKenzie P. ;
Castaldi, Marco J. ;
Farrauto, Robert J. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2010, 94 (1-2) :125-133