Catalytic hydrothermal liquefaction of lignin over carbon nanotube supported metal catalysts for production of monomeric phenols

被引:38
作者
Jia, Pengfei [1 ]
Wang, Juan [1 ]
Zhang, Weiliang [2 ]
机构
[1] Shijiazhuang Univ, Shijiazhuang Chem Fiber Technol Innovat Ctr, Shijiazhuang 050035, Hebei, Peoples R China
[2] North China Pharmaceut Co Ltd, Shijiazhuang 052165, Hebei, Peoples R China
关键词
Lignin; Hydrothermal liquefaction; CNT catalyst; Phenolic monomer; FISCHER-TROPSCH; DEPOLYMERIZATION; PYROLYSIS; CONVERSION; SELECTIVITY; BIOMASS; RICE;
D O I
10.1016/j.joei.2020.09.014
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
The catalytic hydrothermal liquefaction (HTL) of lignin was studied at different temperature (260, 280 and 300 degrees C) with different metal supported (Co, Ni and Fe) on carbon nanotube (CNT) in the presence of different solvents including water, ethanol and methanol for 30 min Reaction time. In comparison with water solvent liquefaction, the bio-oil yield significantly increased under alcoholic solvent (ethanol and methanol). As the reaction temperature increased from 260 to 300 degrees C, there was an increase in the conversion (70.9-86.9 wt%) of lignin. The highest bio-oil yield (66.2 wt%) was found with 10.wt.% Co/CNT catalyst using an ethanol solvent system at 280 degrees C. Moreover lower temperature showed lower yield of bio-oil. Catalyst acidity and surface area were seen to affects the alkali lignin depolymerization. Co/CNT and Ni/CNT catalysts are mainly responsible for the depolymerization of lignin into higher monomer phenolic compounds. A higher area percentage of vanillin obtained during catalytic liquefaction reaction as the presence of a catalyst, and alcoholic solvent accelerated the b-O-4 bond cleavages. Also elemental and GPC analysis showed that during the liquefaction reaction promotes the hydrogenation/hydrodeoxygenation and produced lower molecular weight bio-oils. (C) 2020 Published by Elsevier Ltd on behalf of Energy Institute.
引用
收藏
页码:1 / 10
页数:10
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