Influence of Fe, La, Zr, Ce, and Ca on the catalytic performance and coke formation in dry reforming of methane over Ni/MgO.Al2O3 catalyst

被引:30
|
作者
Miri, Somaye Sadat [1 ]
Meshkani, Fereshteh [1 ,2 ]
Rastegarpanah, Ali [3 ]
Rezaei, Mehran [4 ]
机构
[1] Univ Kashan, Fac Engn, Chem Engn Dept, Catalyst & Adv Mat Res Lab, Kashan, Iran
[2] Univ Kashan, Inst Nanosci & Nanotechnol, Kashan, Iran
[3] Beijing Univ Technol, Coll Environm & Energy Engn, Dept Chem & Chem Engn,Lab Catalysis Chem & Nanosc, Beijing Key Lab Green Catalysis & Separat,Key Lab, Beijing 100124, Peoples R China
[4] Iran Univ Sci & Technol IUST, Sch Chem Petr & Gas Engn, Tehran, Iran
关键词
Dry reforming of methane; Ni based catalyst; Mesoporous catalyst; Simultaneously sol-gel method; Promoters; HIGH-SURFACE-AREA; SYNGAS PRODUCTION; NICKEL-CATALYSTS; NI CATALYSTS; SUPPORTED NI; THERMOCATALYTIC DECOMPOSITION; SEQUENTIAL IMPREGNATION; HYDROGEN-PRODUCTION; NANOCRYSTALLINE LA; NI/AL2O3; CATALYST;
D O I
10.1016/j.ces.2021.116956
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The catalytic and structural properties of the mesoporous nanocrystalline 10 wt.% Ni-MeOx (Me= Fe, La, Zr, Ce, Ca)-MgAl2O4 catalysts were investigated in dry reforming of methane. The catalysts were synthesized simultaneously via a simple and novel surfactant-free self-assembly sol-gel method. The prepared samples with different promoters showed the high surface area ranging from 283.61 to 312.86m(2)/g. The characterization of prepared catalysts was determined using different BET, XRD, SEM, TPR and TPO analysis. The addition of Ce to Ni/MgAl2O4 dramatically improved the catalytic performance and the Ce-promoted catalysts exhibited the highest CH4 conversion among the promoted and unpromoted catalysts. Also Ce suppressed the carbon deposition because CeO2 enhanced the Ni dispersion and reactivity of carbon deposits. The findings of the study showed 3 wt. % Ce promoted catalysts exhibited the best performance in temperature and stability test, more than 50% CH4 with a lower amount of deposited carbon among other powders in dry reforming reaction. Also, no deactivation was observed for this catalyst at a period of 900 minutes of time on stream and at the special condition which despite high feed ratio CH4/CO2=2 and the high GHSV=24000 mL h(-1) g(cat)(-1). (c) 2021 Published by Elsevier Ltd.
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页数:15
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