Mn Modified Ni/Bentonite for CO2 Methanation

被引:40
作者
Jiang, Yuexiu [1 ]
Huang, Tongxia [1 ]
Dong, Lihui [1 ]
Su, Tongming [1 ]
Li, Bin [1 ]
Luo, Xuan [1 ]
Xie, Xinling [1 ]
Qin, Zuzeng [1 ,2 ]
Xu, Cuixia [3 ]
Ji, Hongbing [1 ,2 ]
机构
[1] Guangxi Univ, Sch Chem & Chem Engn, Guangxi Key Lab Electrochem Energy Mat, Nanning 530004, Peoples R China
[2] Sun Yat Sen Univ, Sch Chem, Guangzhou 510275, Guangdong, Peoples R China
[3] Lamar Univ, Dan F Smith Dept Chem Engn, Beaumont, TX 77710 USA
基金
中国国家自然科学基金;
关键词
CO2; methanation; Ni/bentonite catalyst; Solution combustion synthesis; Mn modification; SOLUTION COMBUSTION METHOD; NI/AL2O3; CATALYSTS; CARBON-DIOXIDE; LOW-TEMPERATURE; NICKEL-CATALYSTS; NI; HYDROGENATION; XPS; PROMOTION; OXIDATION;
D O I
10.3390/catal8120646
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
To enhance the low-temperature catalytic activity and stability of Ni/bentonite catalyst, Ni-Mn/bentonite catalyst was prepared by introducing Mn into Ni/bentonite catalyst and was used for CO2 methanation. The results indicated that the addition of Mn enhanced the interaction between the NiO and the bentonite carrier, increased the dispersion of the active component Ni and decreased the grain size of the active component Ni, increased the specific surface area and pore volume of the Ni/bentonite catalyst, and decreased the average pore size, which suppressed the aggregation of Ni particles grown during the CO2 methanation process. At the same time, the Mn addition increased the amount of oxygen vacancies on the Ni/bentonite catalyst surface, which promoted the activation of CO2 in the methanation reaction, increasing the low-temperature activity and stability of the Ni/bentonite catalyst. Under the reaction condition of atmospheric pressure, 270 degrees C, V(H-2):V(CO2) = 4, and feed gas space velocity of 3600 mL.g(cat)(-1).h(-1), the CO2 conversion on the Ni-Mn/bentonite catalyst with 2wt% Mn was 85.2%, and the selectivity of CH4 was 99.8%. On the other hand, when Mn was not added, the CO2 conversion reached 84.7% and the reaction temperature only raised to 300 degrees C. During a 150-h stability test, the CO2 conversion of Ni-2wt% Mn/bentonite catalyst decreased by 2.2%, while the CO2 conversion of the Ni/bentonite catalyst decreased by 6.4%.
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页数:15
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