Boosting syngas production from corncob tar reforming over Ni/MgAl hydrotalcite-derived catalysts

被引:20
|
作者
Ren, Jie [1 ]
Liu, Yi-Ling [2 ]
机构
[1] Rhein Westfal TH Aachen, Inst Tech & Macromol Chem ITMC, Worringerweg 2, D-52074 Aachen, Germany
[2] China Univ Min & Technol, Key Lab Coal Proc & Efficient Utilizat, Minist Educ, Xuzhou 221116, Jiangsu, Peoples R China
关键词
Catalytic reforming; Biomass tar; Toluene; Mg-Al hydrotalcite; Syngas production; LAYERED DOUBLE HYDROXIDES; BIOMASS TAR; HYDROGEN-PRODUCTION; SUPPORTED CATALYSTS; CARBON DEPOSITION; MODEL-COMPOUND; PYROLYSIS; TOLUENE; GASIFICATION; MECHANISM;
D O I
10.1016/j.fuel.2021.121779
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this work, various Mg-Al hydrotalcites with tailored morphologies were prepared by the co-precipitation method and then supported Ni using incipient impregnation for corncob tar reforming. Mg-Al hydrotalcites prepared under a pH of 10 and subsequently supported 20 wt% Ni (Ni/MgAl-10) exhibited excellent activity in syngas production (26.3 mmol/g) from corncob tar reforming at 600 degrees C. For a better understanding of the activity of the obtained catalysts, their activities for steam reforming of toluene (SRT) were investigated. In comparison with commercial Ni/Al2O3 and other Ni/MgAl hydrotalcite-derived catalysts, Ni/MgAl-10 had higher stability in SRT at 550 degrees C, which maintained >90% of toluene conversion during 10 h time-on-stream. The characterizations indicated that the excellent performance of Ni/MgAl-10 in both biomass tar and toluene reforming can be attributed to high dispersion of Ni particles, large specific surface area (119.9 m(2)/g), high reducibility (96%), and high basicity (1.33 mmol/g(eat)). Moreover, the kinetic study confirmed that Ni/MgAl-10 with a lower activation energy (23.5 kJ/mol) than commercial Ni/Al2O3 could exhibit better performance in SRT at low temperatures. The results could provide a design of a novel Ni-based catalyst and its application for tar reforming in the process of biomass gasification.
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页数:9
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