Novel hierarchical Ni/MgO catalyst for highly efficient CO methanation in a fluidized bed reactor

被引:22
|
作者
Li, Jun [1 ]
Zhu, Qingshan [1 ]
Peng, Wencai [2 ]
Zhang, Qiang [2 ]
Luo, Guohua [2 ]
Wei, Fei [2 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
[2] Tsinghua Univ, Beijing Key Lab Green Chem React Engn & Technol, Dept Chem Engn, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
hierarchical particles; Ni; MgO; CO methanation; fluidized-bed; SYNTHETIC NATURAL-GAS; SUPPORTED NICKEL-CATALYSTS; NI-BASED CATALYSTS; STRUCTURE SENSITIVITY; CARBON-DIOXIDE; NANOPARTICLES; DEACTIVATION; PERFORMANCE; REDUCTION; SYSTEM;
D O I
10.1002/aic.15597
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A facile synthesis of the hierarchical Ni/MgO catalyst is reported, with extremely fine dispersion of Ni nanoparticles (NPs) and high surface oxygen mobility. The hierarchical Ni/MgO catalyst exhibits higher activity for CH4 formation than that prepared by the impregnation method. The enhanced activity and thermal stability of the hierarchical Ni/MgO catalyst is attributed to hierarchical MgO particles with a multilayer structure and high surface oxygen mobility. This induces better metal-support interactions, high Ni dispersion to prevent Ni NPs sintering, and the high surface oxygen mobility provides a high resistance to carbon deposition. Compared to the impregnated Ni/MgO catalyst, the hierarchical Ni/MgO catalyst exhibits a better fluidization quality and a higher attrition-resistance in a fluidized-bed reactor. This approach to improve the catalytic activity by creation of hierarchical Ni/MgO particles is encouraging for the design of novel catalysts for synthetic natural gas production, especially from the perspective of matching catalysts with fluidized-bed reactors. (c) 2017 American Institute of Chemical Engineers AIChE J, 63: 2141-2152, 2017
引用
收藏
页码:2141 / 2152
页数:12
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