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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.
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页码:51 / 58
页数:8
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