Influence of supports on catalytic behavior of nickel catalysts in carbon dioxide reforming of toluene as a model compound of tar from biomass gasification

被引:84
|
作者
Kong, Meng [1 ]
Fei, Jinhua [1 ]
Wang, Shuai [1 ]
Lu, Wen [1 ]
Zheng, Xiaoming [1 ]
机构
[1] Zhejiang Univ, Inst Catalysis, Key Lab Appl Chem Zhejiang Prov, Hangzhou 310028, Peoples R China
关键词
Tar removal; CO2 reforming of toluene; Ni catalyst; Coke; Fluidized bed; STEAM; METHANE; GAS; ELIMINATION; REDUCTION; SYNGAS;
D O I
10.1016/j.biortech.2010.09.054
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
A series of supported Ni catalysts including Ni/MgO, Ni/gamma-Al2O3, Ni/SiO2 and Ni/ZrO2 was tested in CO2 reforming of toluene as a model compound of tar from biomass gasification in a fluidized bed reactor, and characterized by the means of temperature programmed reduction with hydrogen (H-2-TPR), XRD, TEM and temperature programmed oxidation (TPO). Combining the characterization results with the performance tests, the activity of catalyst greatly depended on Ni particles size, and the stability was affected by the coke composition. Both of them (Ni particle size and coke composition) were closely related to the interaction between nickel and support which would determine the chemical environment where Ni inhabited. The best catalytic performance was observed on Ni/MgO due to the strong interaction between NiO and MgO via the formation of Ni-Mg-O solid solution, and the highest dispersion of Ni particle in the basic environment. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2004 / 2008
页数:5
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