Efficient hydrodeoxygenation of phenolic compounds and raw lignin-oil under a temperature-controlled phase-transfer catalysis

被引:18
作者
Yang, Zhi [1 ]
Luo, Bowen [1 ]
Shu, Riyang [1 ]
Tian, Zhipeng [1 ]
Kang, Yu [1 ]
Chen, Ying [1 ]
机构
[1] Guangdong Univ Technol, Sch Mat & Energy, Guangdong Prov Key Lab Funct Soft Condensed Matte, Guangzhou 510006, Peoples R China
基金
中国国家自然科学基金;
关键词
Binary catalyst; Tungstic acid; HDO; Temperature-controlled phase-transfer; Lignin-oil; NOBLE-METAL CATALYSTS; BIO-OIL; MODEL COMPOUNDS; DEPOLYMERIZATION; CONVERSION; PYROLYSIS; CHEMICALS; BIOMASS; TRANSFORMATION; FRACTIONATION;
D O I
10.1016/j.fuel.2020.120091
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
An effective binary catalyst by using tungstic acid (H2WO4) and Ru/C was employed for the hydrodeoxygenation (HDO) of phenolic compounds and raw lignin-oil. H2WO4 was presented as solid at ambient temperature, but it dissolved at high temperature above 100 degrees C and therefore functioned as an active homogeneous catalyst. This phenomenon resulted in a temperature-controlled phase-transfer behavior in the HDO of phenolic compounds. An efficient HDO performance and an exceptional reusability for guaiacol HDO were presented by this bifunctional catalyst, which can be reused more than 10 times with guaiacol conversion and cyclohexane selectivity over 90%. The comparison of traditional liquid organic and mineral acids, as well as solid acids, with H2WO4 confirmed the outstanding catalytic performance of H2WO4 and highlighted the advantages of H2WO4 as a homogeneous catalyst. Besides guaiacol, other phenolic compounds including various monomers and dimers all exhibited good HDO results, with 100% conversion and cycloalkanes selectivity. Moreover, the raw lignin-oil can be efficiently deoxygenated under the catalysis of this bifunctional catalyst. 99.3% content of hydrocarbons was obtained in the upgraded lignin-oil, which was promising to be used as fuel directly. This catalytic system has great potential for the industrial application of lignin-oil upgrade.
引用
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页数:9
相关论文
共 54 条
[51]   Production of hydrocarbon fuels from heavy fraction of bio-oil through hydrodeoxygenative upgrading with Ru-based catalyst [J].
Zhang, Xinghua ;
Tang, Wenwu ;
Zhang, Qi ;
Li, Yuping ;
Chen, Lungang ;
Xu, Ying ;
Wang, Chenguang ;
Ma, Longlong .
FUEL, 2018, 215 :825-834
[52]   Production of Hydrocarbons via Hydrodeoxygenation of Lignin-Derived Phenolic Compounds [J].
Zhang Xinghua ;
Chen Lungang ;
Zhang Qi ;
Long Jinxing ;
Wang Tiejun ;
Ma Longlong .
PROGRESS IN CHEMISTRY, 2014, 26 (12) :1997-2006
[53]   Hydrodeoxygenation of lignin-derived phenolic compounds to hydrocarbons over Ni/SiO2-ZrO2 catalysts [J].
Zhang, Xinghua ;
Zhang, Qi ;
Wang, Tiejun ;
Ma, Longlong ;
Yu, Yuxiao ;
Chen, Lungang .
BIORESOURCE TECHNOLOGY, 2013, 134 :73-80
[54]   Highly Selective Catalytic Conversion of Phenolic Bio-Oil to Alkanes [J].
Zhao, Chen ;
Kou, Yuan ;
Lemonidou, Angeliki A. ;
Li, Xuebing ;
Lercher, Johannes A. .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2009, 48 (22) :3987-3990