Engineering biochar-supported nickel catalysts for efficient CO2 methanation

被引:0
|
作者
Frainetti, Alexandra J. [1 ,2 ]
Klinghoffer, Naomi B. [1 ,2 ,3 ]
机构
[1] Western Univ, Dept Chem & Biochem Engn, 1151 Richmond St, London, ON N6A 3K7, Canada
[2] Western Univ, Inst Chem & Fuels Alternat Resources ICFAR, 22312 Wonderland Rd, Ilderton, ON N0M 2A0, Canada
[3] Western Univ, Western Acad Adv Res, 1151 Richmond St, London, ON N6A 3K7, Canada
来源
BIOMASS & BIOENERGY | 2024年 / 184卷
基金
加拿大自然科学与工程研究理事会;
关键词
Methanation; Biochar; CO2; utilization; Catalysis; Pyrolysis; Nickel catalyst; CARBON NANOTUBES; CHAR; KINETICS; TEMPERATURE; DEPOSITION; BEHAVIORS; HYDROGEN; ALUMINA; COBALT; OXIDES;
D O I
10.1016/j.biombioe.2024.107179
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Carbon dioxide methanation is a promising approach to convert captured CO2 into green natural gas. Developing high performance biochar-supported nickel catalysts promotes a circular economy and the application of sustainable catalysts. Western red cedar biochar was produced via pyrolysis at 400, 500, and 600 degrees C and loaded with nickel via incipient wetness impregnation. Methanation was done at 400, 500, and 600 degrees C with the highest methane yield of 59% achieved at 500 degrees C with 10 wt.% Ni loading. This is comparable to a gamma-Al2O3 supported catalyst prepared and tested similarly, which achieved a methane yield of 53%. Biochar-supported catalysts showed deactivation whereby methane yield decreased from 59% to 51% over 5 h, likely due to coking and/or the sintering of nickel. Various space velocities were tested, and results demonstrated that with a space velocity of 37.5 mL/g.min methane selectivity was 89% after 1 h on stream compared to methane selectivity of 42%, which was achieved at a space velocity of 112.5 mL/g.min. This shows that a much higher rate of deactivation is observed at higher space velocities. Increasing the nickel loading from 5 wt.% to 10 wt.% increased methane yield from 40% to 58% after 1 h on stream. The higher loading also showed significantly less deactivation. Future work focusing on the extent and impact of metal -support interactions and metal dispersion on catalytic performance and deactivation during CO2 methanation is recommended.
引用
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页数:9
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