Bed Agglomeration during Bio-oil Fast Pyrolysis in a Fluidized-Bed Reactor

被引:21
作者
Gao, Wenran [1 ]
Zhang, Mingming [1 ]
Wu, Hongwei [1 ]
机构
[1] Curtin Univ, Dept Chem Engn, GPO Box U1987, Perth, WA 6845, Australia
基金
澳大利亚研究理事会;
关键词
WATER-SOLUBLE FRACTION; BIOMASS FAST PYROLYSIS; MALLEE BIOMASS; WESTERN-AUSTRALIA; BIOSLURRY FUELS; CRUDE GLYCEROL; COMBUSTION; BIOCHAR; QUANTIFICATION; GASIFICATION;
D O I
10.1021/acs.energyfuels.8b00333
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
This study investigates bed agglomeration during fast pyrolysis of bio-oil in a fluidized-bed reactor at temperatures of 500-800 degrees C. The samples used include bio-oil, bio-oil water-soluble fraction (WSF), bio-oil water-insoluble fraction (WIF), and selected model compounds. Increasing pyrolysis temperature from 500 to 800 degrees C decreases the agglomeration yields of bio-oil, WSF, and WIF from 40% to 15%, 26.2% to 11.6%, and 15.0% to 5.2%, respectively. Investigation using model compounds suggests that the interactions between lignin-derived oligomers and sugar are mainly responsible for the high bed agglomeration yields of bio-oil and WSF, and such interactions weaken as pyrolysis temperature increases. Water has an insignificant effect on bed agglomeration during bio-oil or WSF pyrolysis. The results also show that the bed agglomeration yield and the formation of tar (and/or coke) are in broad linear correlations, indicating that the tar (and/or coke) formed during fast pyrolysis contributes to the bed agglomeration of bio-oil. The linear correlation from the data of bio-oil has a steeper gradient compared to that of WSF and WIF, clearly indicating the synergy taking place between the WSF and WIF during fast pyrolysis in enhancing bed agglomeration.
引用
收藏
页码:3608 / 3613
页数:6
相关论文
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[41]   Fuel Mixtures from Crude Glycerol, the Bio-oil Water-Soluble Fraction, and Biochar for Stationary Applications [J].
Zhang, Mingming ;
Wu, Hongwei .
ENERGY & FUELS, 2016, 30 (10) :8419-8424