Hydrodeoxygenation of angelica lactone dimers and trimers over silica-alumina supported nickel catalyst

被引:15
|
作者
Ayodele, Olubunmi O. [1 ,2 ,3 ]
Dawodu, Folasegun A. [2 ]
Yan, Dongxia [1 ]
Lu, Xingmei [1 ]
Xin, Jiayu [1 ]
Zhang, Suojiang [1 ]
机构
[1] Chinese Acad Sci, State Key Lab Multiphase Complex Syst, Key Lab Green Proc & Engn, Inst Proc Engn, Beijing 100190, Peoples R China
[2] Univ Ibadan, Dept Chem Ind, Ibadan, Oyo State, Nigeria
[3] Forestry Res Inst Nigeria, Dept Forest Prod Dev & Utilizat, Ibadan, Oyo State, Nigeria
基金
中国国家自然科学基金;
关键词
Angelica lactone; Levulinic acid; Di/trimerization; Biogasoline; Bifunctional catalyst; GAMMA-VALEROLACTONE; BIOMASS; LIQUID; CONVERSION; ALKANES; HYDROCARBONS; FUELS;
D O I
10.1016/j.renene.2015.09.008
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Fractionation of biomass to furan derivatives followed by hydrodeoxygenation could provide an efficient route for bioalkanes production. A simple catalytic process to obtain fuels rich in alkanes with 8-12 carbons via hydrodeoxygenation of biomass-derived angelica lactone dimers/trimers was investigated. Dimers and trimers obtained by C-C coupling of alpha- and beta-angelica lactones were hydrodeoxygenated over a bifunctional catalyst, nickel supported on silica-alumina (Ni/SiO2-Al2O3). Reaction conditions such as hydrogen pressure, temperature and time were considered and it was observed that changes in reaction conditions had significant effect on product distributions. Effective conversion of di/trimers of angelica lactone was achieved over Ni/SiO2-Al2O3 with highly branched alkanes and aromatics being selectively produced. The hydrogenated products which are similar in composition to fossil-derived gasoline could further encourage research into more efficient processes to produce bioalkanes on an industrial scale. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:943 / 948
页数:6
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