CO2 reforming of methane over MCM-41-supported nickel catalysts: altering support acidity by one-pot synthesis at room temperature

被引:90
作者
Lovell, Emma [1 ]
Jiang, Yijiao [1 ]
Scott, Jason [1 ]
Wang, Fenglong [1 ]
Suhardja, Yoel [1 ]
Chen, Mengmeng [2 ]
Huang, Jun [2 ]
Amal, Rose [1 ]
机构
[1] Univ New S Wales, Sch Chem Engn, ARC Ctr Excellence Funct Nanomat, Sydney, NSW 2052, Australia
[2] Univ Sydney, Sch Chem & Biomol Engn, Lab Catalysis Engn, Sydney, NSW 2006, Australia
基金
澳大利亚研究理事会;
关键词
CO2 reforming of methane; Nickel catalyst; MCM-41; Framework aluminium; Sodium ion; Support acidity; INCORPORATED MCM-41 CATALYSTS; CARBON-DIOXIDE; PARTIAL OXIDATION; SYNTHESIS GAS; SILICA; ALUMINA; CH4; NI; RESISTANCE; MECHANISM;
D O I
10.1016/j.apcata.2013.12.020
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
Highly structured neat MCM-41, Na-form, and Al-incorporated MCM-41 mesoporous materials were synthesized using a simple, one-pot procedure at room temperature. The neat MCM-41 material possessed a surface area comparable with other MCM-41 materials prepared using more conventional higher temperature methods. Incorporating Al into the MCM-41 framework increased support acidity while entrapping Na ions in the MCM-41 pores lowered acidity. The neat MCM-41, Na-form, and Al-incorporated MCM-41 were impregnated with 2.5, 5 and 10% Ni and catalytic performance was assessed for CO2 reforming of methane (CH4). XRD, TEM and H-2-TPR indicated at low loadings the Ni was highly dispersed on the support, whereby increasing the Ni loading encouraged the formation of larger Ni crystals on the external MCM-41 surface. 2.5% Ni catalysts supported on neat MCM-41 exhibited excellent catalytic activity invoking up to 98% CH4 conversion at 800 degrees C and 26% at 500 degrees C. Carbon accumulation on the catalyst was greater at higher Ni loadings although this was not to the detriment of activity over the reaction time-frame. This result coupled with variations in the H-2/CO product ratio and CH4/CO2 conversion difference suggested increasing the Ni loading promoted the Boudouard, CH4 cracking and reverse water gas shift side reactions. Incorporating the MCM-41 with either Al or Na lowered catalyst performance with the promoters found to enhance or suppress the side reactions to varying degrees. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:51 / 58
页数:8
相关论文
共 35 条
[1]   TEMPERATURE-PROGRAMMED REDUCTION OF SILICA-SUPPORTED NICKEL-CATALYSTS [J].
AFZAL, M ;
THEOCHARIS, CR ;
KARIM, S .
COLLOID AND POLYMER SCIENCE, 1993, 271 (11) :1100-1105
[2]   Activity and stability enhancement of Ni-MCM-41 catalysts by Rh incorporation for hydrogen from dry reforming of methane [J].
Arbag, Huseyin ;
Yasyerli, Sena ;
Yasyerli, Nail ;
Dogu, Gulsen .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (06) :2296-2304
[3]   PARTIAL OXIDATION OF METHANE TO SYNTHESIS GAS-USING CARBON-DIOXIDE [J].
ASHCROFT, AT ;
CHEETHAM, AK ;
GREEN, MLH ;
VERNON, PDF .
NATURE, 1991, 352 (6332) :225-226
[4]  
Berteau P., 1989, CATAL TODAY, V5, P121, DOI DOI 10.1016/0920-5861(89)80020-3
[5]   MECHANISM OF HYDROCARBON SYNTHESIS OVER FISCHER-TROPSCH CATALYSTS [J].
BILOEN, P ;
SACHTLER, WMH .
ADVANCES IN CATALYSIS, 1981, 30 :165-216
[6]   CO2 reforming of CH4 over supported Pt catalysts [J].
Bradford, MCJ ;
Vannice, MA .
JOURNAL OF CATALYSIS, 1998, 173 (01) :157-171
[7]   High carbon-resistance Ni/CeAlO3-Al2O3 catalyst for CH4/CO2 reforming [J].
Chen, Wei ;
Zhao, Guofeng ;
Xue, Qingsong ;
Chen, Li ;
Lu, Yong .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2013, 136 :260-268
[8]   Microfibrous entrapment of Ni/Al2O3 for dry reforming of methane: Heat/mass transfer enhancement towards carbon resistance and conversion promotion [J].
Chen, Wei ;
Sheng, Wenqian ;
Cao, Fahai ;
Lu, Yong .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (23) :18021-18030
[9]   MCM-41 supported PdNi catalysts for dry reforming of methane [J].
Damyanova, S. ;
Pawelec, B. ;
Arishtirova, K. ;
Fierro, J. L. G. ;
Sener, C. ;
Dogu, T. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2009, 92 (3-4) :250-261
[10]   The Fischer-Tropsch process: 1950-2000 [J].
Dry, ME .
CATALYSIS TODAY, 2002, 71 (3-4) :227-241