Synergistic effect of Ni and NiO in hydrogen reduction for CO methanation

被引:3
作者
Li, Jiaxin [1 ]
Liang, Yifei [1 ]
Li, Zhao [1 ]
Fan, Ke [1 ]
Wang, Chunxue [1 ]
Li, Kai [1 ,2 ]
Li, Yuan [1 ,2 ]
Sun, Xin [1 ,2 ]
Ning, Ping [1 ,2 ]
Wang, Fei [1 ,2 ]
机构
[1] Kunming Univ Sci & Technol, Fac Environm Sci & Engn, Kunming 650500, Peoples R China
[2] Natl Reg Engn Ctr Recovery Waste Gases Met & Chem, Kunming 650500, Peoples R China
基金
中国国家自然科学基金;
关键词
Ni/Al2O3; H-2; reduction; Synergy effect; CO hydrogenation; CARBON-MONOXIDE HYDROGENATION; HIGHER ALCOHOL SYNTHESIS; SYNTHETIC NATURAL-GAS; SELECTIVE METHANATION; SYNGAS METHANATION; NI/AL2O3; CATALYSTS; SUPPORT; DRIFTS; AL2O3;
D O I
10.1016/j.seppur.2023.126178
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The synthesis of methane from syngas represents a pivotal technology in the artificial synthesis of natural gas, with the study of methanation catalysts being a fundamental aspect of this process. Extensive research has focused on CO methanation using Ni/Al2O3 catalysts; however, enhancements in catalyst stability and low-temperature activity are still required. This research investigated the structure of Ni/Al2O3 under H-2 reduction at varying temperatures and the catalytic performance in natural gas synthesis (SNG) through CO methanation. It was observed that a higher reduction temperature resulted in nickel species agglomeration. Notably, Ni catalysts reduced at 600 C-o demonstrated optimal CO conversion and CH4 selectivity under the tested conditions. Characterization studies uncovered a synergistic effect between Ni and NiO species, which was most effective for catalytic activity under hydrogen reduction at 600 C-o but only at an appropriate reduction temperature. These insights are significant for the advancement of Ni/Al2O3 methanation catalysts in natural gas production.
引用
收藏
页数:10
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