A novel production of phase-divided jet-fuel-range hydrocarbons and phenol-enriched chemicals from catalytic co-pyrolysis of lignocellulosic biomass with low-density polyethylene over carbon catalysts

被引:29
作者
Duan, Dengle [1 ,2 ,4 ]
Zhang, Yayun [1 ,3 ]
Lei, Hanwu [1 ]
Qian, Moriko [1 ]
Villota, Elmar [1 ]
Wang, Chenxi [1 ]
Wang, Yunpu [4 ]
Ruan, Roger [5 ,6 ]
机构
[1] Washington State Univ, Dept Biol Syst Engn, 2710 Crimson Way, Richland, WA 99354 USA
[2] Zhongkai Univ Agr & Engn, Coll Light Ind & Food, Guangzhou 510225, Peoples R China
[3] East China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
[4] Nanchang Univ, Engn Res Ctr Biomass Convers, Minist Educ, Nanchang 330047, Jiangxi, Peoples R China
[5] Univ Minnesota, Ctr Biorefining, 1390 Eckles Ave, St Paul, MN 55108 USA
[6] Univ Minnesota, Dept Bioprod & Biasyst Engn, 1390 Eckles Ave, St Paul, MN 55108 USA
基金
美国食品与农业研究所; 中国国家自然科学基金;
关键词
DOUGLAS-FIR SAWDUST; RICH BIO-OIL; MICROWAVE PYROLYSIS; ACTIVATED CARBON; LIGNIN DEPOLYMERIZATION; SYNGAS PRODUCTION; FIXED-BED; CONVERSION; GASOLINE; PLASTICS;
D O I
10.1039/d0se00419g
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The catalytic co-pyrolysis of Douglas fir and low-density polyethylene with commercial activated carbon catalysts was investigated for the first time. Six types of activated carbon catalysts were tested and compared. The obtained liquid product contained physically separated parts being in the oil and water phases, where the percentage of the oil phase ranged from 10.10 to 64.4 wt% depending on various co-pyrolysis conditions. The oil phase of bio-oil was rich in C-8-C(16)aromatics and aliphatics (up to 98.6 area%) that were compatible with transportation jet fuel. In addition, the main components of the bio-oil in the water phase were phenols and guaiacols, in which high phenol selectivity (up to 92.9 area%) and phenol concentration (up to 26.4 mg mL(-1)) were achieved. Hydrogen, methane, carbon dioxide, and carbon monoxide were the main fractions of gaseous products, where a high concentration of methane (23.6 vol%) and carbon monoxide (39.1 vol%) could be obtained. The process was optimized based on an overall consideration of bio-oil yield, C-8-C(16)hydrocarbon selectivity, and phenol concentration. Furthermore, a reaction mechanism for the production of phenols and hydrocarbons was proposed. Our findings may provide a novel, green, and cost-effective route to produce phase-divided phenol-enriched chemicals and transportation jet fuels.
引用
收藏
页码:3687 / 3700
页数:14
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