Direct hydrocracking of oxidized bio-oil to hydrocarbons

被引:30
|
作者
Tanneru, Sathish K. [1 ]
Steele, Philip H. [1 ]
机构
[1] Mississippi State Univ, Dept Sustainable Bioprod, Mississippi State, MS 39762 USA
关键词
Bio-oil; Oxidation; Hydrodeoxygenation; Hydrocracking; HHV; FAST PYROLYSIS OIL; CATALYTIC HYDRODEOXYGENATION; BIOMASS; FUELS;
D O I
10.1016/j.fuel.2015.03.080
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Hydrodeoxygenation is considered a promising technology to convert bio-oils to liquid transportation fuels. Recently we tested a hydrodeoxygenation method to convert oxidized bio-oil to increase liquid fuel yield, reduce char and reduce required hydrogen. In this current study we tested direct hydrocracking of the oxidized bio-oil to produce high-energy liquid hydrocarbons. We tested various reaction conditions (reaction temperature, hydrogen pressure, time and catalyst type) on the hydrocracking of the oxidized bio-oil. Direct hydrocracking of the oxidized bio-oil produced 36.6% higher hydrocarbons yield compared to direct hydrocracking of the raw bio-oil. The hydrocarbons mixture produced had a higher heating value (HHV) of 43.6 MJ/kg. The oxygen content and acid value were 0.5 wt% and 0.3 mg KOH/g, respectively. Density and viscosity were considerably low at 0.9 g/ml and 1.8 cSt, respectively. pH value was 8.4. The hydrocarbon mixture was also analyzed by GC-MS, FTIR, NMR and DHA. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:268 / 274
页数:7
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