Hydrotreatment of bio-oil over Ni-based catalyst

被引:162
|
作者
Zhang, Xinghua [1 ,2 ]
Wang, Tiejun [1 ]
Ma, Longlong [1 ]
Zhang, Qi [1 ]
Jiang, Ting [1 ,2 ]
机构
[1] Chinese Acad Sci, Key Lab Renewable Energy & Gas Hydrate, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China
[2] Chinese Acad Sci, Grad Sch, Beijing 100049, Peoples R China
基金
中国国家自然科学基金;
关键词
Bio-oil; Phenol; Ni-based catalysts; Hydrodeoxygenation (HDO); Upgrading; PYROLYSIS OIL; LIQUID FUEL; HYDRODEOXYGENATION; BIOMASS; CONVERSION; FRACTION; LIGNIN; HZSM-5; PD;
D O I
10.1016/j.biortech.2012.07.119
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Inexpensive non-sulfided Ni-based catalysts were evaluated for hydrotreatments using phenol as model compound. HZSM-5, a zeolite with different ratio of Si/Al and gamma-Al2O3 were impregnated with Ni(NO3)(2)center dot 6H(2)O and calcined at 450 degrees C. Conversion rates and product distribution for treatment of phenol at 160-240 degrees C in the presence of catalysts with nickel loads of 6, 10, 14 and 17 wt.% were determined. Phenol conversion was highest (91.8%) at 240 degrees C in the presence of HZSM-5(Si/Al = 38) loaded with 10% Ni. When hydrotreatment was carried out with bio-oil obtained from pyrolysis of pine sawdust under the optimal conditions determined for phenol, the pH of bio-oil increased from 2.27 to 4.07, and the hydrogen content increased from 6.28 to 7.01 wt.%. The decrease in acidity is desirable for the use of upgraded bio-oil. (C) 2012 Published by Elsevier Ltd.
引用
收藏
页码:306 / 311
页数:6
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