Hydrodeoxygenation of lignin-derived phenolic compounds over Ru/TiO2 catalyst: Effect of TiO2 morphology

被引:21
|
作者
Zhong, Zhuojie [1 ]
Li, Junxuan [1 ]
Jian, Minyin [1 ]
Shu, Riyang [1 ]
Tian, Zhipeng [1 ]
Wang, Chao [1 ]
Chen, Ying [1 ]
Shi, Ning [2 ]
Wu, Yanxue [3 ]
机构
[1] Guangdong Univ Technol, Sch Mat & Energy, Guangdong Prov Key Lab Funct Soft Condensed Matter, Guangzhou 510006, Peoples R China
[2] Guizhou Inst Technol, Sch Chem Engn, Guiyang 550003, Peoples R China
[3] Guangdong Univ Technol, Anal & Test Ctr, Guangzhou 510006, Peoples R China
基金
中国国家自然科学基金;
关键词
Hydrodeoxygenation; Phenolic compounds; Ru; TiO2; morphology; Acid site; GAS-PHASE HYDRODEOXYGENATION; BIO-OIL; GUAIACOL; ANISOLE; HYDROCARBONS; PYROLYSIS; GLYCEROL;
D O I
10.1016/j.fuel.2022.126241
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 (HDO) reaction is a necessary refinery process for lignin-derived phenolic compounds to be used as high quality liquid fuels. Catalyst morphology makes a big difference on the HDO performance through changing the properties of metal site and acid site, while the catalytic mechanism is still not very clear. In this work, four kinds of Ru/TiO2 catalysts with different morphology were prepared by photochemical method and all of them achieved a high Ru metal dispersion. A series of catalyst characterizations were carried out, including XRD, BET, SEM, TEM, H2-TPD and NH3-TPD, in order to explore the crystal structure, surface property, Ru metal dispersion, hydrogen adsorption capacity as well as acid properties. Results showed that Ru/TNP catalyst possessed a large surface area, an abundance of medium strength acid sites and a good hydrogen adsorption capacity. The HDO performances on lignin-derived phenolic compounds were also compared, in which Ru/TNP catalyst presented the best HDO performance. The guaiacol conversion and the selectivity of cyclohexane product were both close to 100 % at 250 degrees C under 1 MPa hydrogen pressure. Moreover, the content of hydro-carbons increased from 11.1 % to 60.8 % in the lignin-oil upgrading process.
引用
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页数:9
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