Bio-gasoline production from co-cracking of hydroxypropanone and ethanol

被引:29
作者
Wang, Shurong [1 ]
Cai, Qinjie [1 ]
Wang, Xiangyu [1 ]
Guo, Zuogang [1 ]
Luo, Zhongyang [1 ]
机构
[1] Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China
基金
中国国家自然科学基金;
关键词
Bio-oil; Upgrading; Ketones; Co-cracking; Bio-gasoline; BIOMASS PYROLYSIS OIL; HZSM-5; ZEOLITE; OXYGENATE COMPONENTS; ZSM-5; CONVERSION; METHANOL; TRANSFORMATION; HYDROCARBONS; CATALYSTS; MECHANISM;
D O I
10.1016/j.fuproc.2013.02.005
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Hydroxypropanone was selected as the model compound of bio-oil ketones to study its cracking behavior for bio-gasoline production. The cracking of pure hydroxypropanone generated inferior oil phase which had a content of high oxygenated compounds. The quality of oil phase was obviously improved when ethanol was adopted as the co-reactant. Furthermore, increasing cracking pressure also benefited the yield and quality of the oil phase. The conversion yield of the reactants reached 100% and the selectivity of the oil phase reached 31.9 wt.% in the co-cracking process under 400 degrees C and 2 MPa. The oil phase also had an outstanding quality with a hydrocarbon content of 100% and mainly contained hydrocarbons with carbon numbers ranging from 7 to 10, which are also important components in commercial gasoline. Based on the results, a co-cracking mechanism was proposed to illustrate the role of ethanol in promoting hydroxypropanone cracking. (c) 2013 Elsevier B.V. All rights reserved.
引用
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页码:86 / 93
页数:8
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