Hydrogen production by steam reforming of fusel oil over Ni-based fiber catalyst

被引:4
|
作者
Le-Mai, T. H. [1 ,2 ,3 ]
Mhadmhan, S. [1 ,2 ]
Trieu, T. Q. [4 ]
Prasongthum, N. [5 ]
Suriya, P. [1 ,2 ,3 ]
Reubroycharoen, P. [1 ,2 ]
机构
[1] Chulalongkorn Univ, Ctr Excellence Catalysis Bioenergy & Renewable Ch, Fac Sci, Bangkok 10330, Thailand
[2] Chulalongkorn Univ, Dept Chem Technol, Fac Sci, Bangkok 10330, Thailand
[3] Chulalongkorn Univ Res Bldg, Ctr Excellence Petrochem & Mat Technol, Bangkok 10330, Thailand
[4] Ind Univ Ho Chi Minh City, Program Petrochem, Fac Chem Engn, Ho Chi Minh City 70000, Vietnam
[5] Thailand Inst Sci & Technol Res TISTR, Expert Ctr Innovat Clean Energy & Environm, Pathum Thani 12120, Thailand
关键词
Fusel oil reforming; Silica fiber; Silica porous; Nickel-based catalyst; Carbon nanotubes - silica fiber; CARBON NANOTUBES; H-2; PRODUCTION; ETHANOL; CO; STABILITY; MECHANISM; SILICA; NICKEL;
D O I
10.1016/j.matpr.2021.10.012
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
This research aimed to evaluate the fusel oil steam reforming over Ni/carbon nanotubes-silica fiber (Ni/ CNTs-SF) catalysts prepared by impregnation method with 10 wt% of Ni loading. CNTs-SF was synthesized by chemical vapor deposition (CVD) using ethanol as a source for CNTs over steam reforming. The prepared catalysts were analyzed by BET, XRD, TEM, FESEM-EDS, Raman, and TG/DTG. Ni/CNTs-SF catalyst was tested for fusel oil steam reforming and compared with Ni supported on conventional silica such as a silica fiber (SF) and a silica porous (SP) at the same loading. The results found that Ni/CNTs-SF catalyst showed better catalytic activity and stability than Ni/SF and Ni/SP. TGA profile of the catalysts after fusel oil steam reforming showed that the severe carbon deposited over Ni/SP at 64% (wt%), while at 31% was found over Ni/CNTs-SF catalyst and Ni/SF catalyst. In addition, Ni/CNTs-SF catalyst exhibited the highest hydrogen yield at 15%, and Ni/SF and Ni/SP catalysts gave a lower yield of hydrogen at 11% and 7%, respectively. Copyright (C) 2021 Elsevier Ltd. All rights reserved. Selection and peer-review under responsibility of the scientific committee of the International Symposium of Reaction Engineering, Catalysis & Sustainable Energy
引用
收藏
页码:1147 / 1153
页数:7
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