Enhancement of hydrogen production via methanol steam reforming using a Ni-based catalyst supported by spongy mesoporous alumina

被引:7
|
作者
Hu, Bin [1 ]
Shu, Riyang [1 ]
Tian, Zhipeng [1 ]
Wang, Chao [1 ]
Chen, Ying [1 ]
Xu, Ying [2 ]
机构
[1] Guangdong Univ Technol, Sch Mat & Energy, Guangdong Prov Key Lab Funct Soft Condensed Matter, Guangzhou 510006, Peoples R China
[2] Jimei Univ, Coll Mech Equipment & Mech Engn, Fujian Prov Clean Combust & Energy Utilizat Res Ct, Fujian Prov Key Lab Energy Clean Utilizat & Dev, Xiamen 316021, Peoples R China
基金
中国国家自然科学基金;
关键词
WATER-GAS SHIFT; CARBON DEPOSITION; ETHANOL; SURFACE; PERFORMANCE; STABILITY; PROMOTION;
D O I
10.1039/d4gc00397g
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
In situ methanol steam reforming for hydrogen production is a promising technology to provide a hydrogen source for full cells. However, the conventional methanol steam reforming usually encounters catalyst inefficiency and instability, which make its industrial application difficult. This work proposes a novel and stable Ni-based catalyst supported by spongy mesoporous alumina and achieves an enhancement of hydrogen production. The prepared Ni/gamma-Al2O3 catalyst exhibits a higher hydrogen production yield of 0.26 mol h(-1) than the commercial Ni/gamma-Al2O3-Com catalyst (0.21 mol h(-1)) at 450 degrees C, with an improvement of the hydrogen flow rate of 23.8%. The Ni/gamma-Al2O3 catalyst also presents a much superior performance to the reported noble metal-based catalysts and Ni-based catalysts. The special spongy mesoporous structure provides favorable conditions for high catalytic activity, mainly based on the high dispersion of the Ni metal site and the high catalyst stability. The Ni metal particles are highly dispersed over spongy mesoporous Al2O3 with an average particle size of only 3.7 nm. Characterization analysis shows that the spongy mesoporous structure of the catalyst enables quick adsorption of the reactants and reaction intermediates, and the highly dispersed Ni metal site can lead to the rapid dehydrogenation of methanol to increase the hydrogen yield. Moreover, the stability of the prepared Ni/gamma-Al2O3-5H catalyst is much superior to that of the commercial Ni/gamma-Al2O3-Com catalyst, where Ni/gamma-Al2O3-5H retained 100% of methanol conversion for 12 h, and the spongy mesoporous structure and the high dispersion of Ni particles were also well maintained. In addition, the reaction mechanism of methanol steam reforming over the Ni/gamma-Al2O3-5H catalyst is revealed in detail, especially based on the in situ DRIFTS characterization results. This research provides valuable insights for the development of catalytic methanol steam reforming for hydrogen production and in the field of green chemistry.
引用
收藏
页码:5485 / 5498
页数:14
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