Influence of reaction conditions on bio-oil production from pyrolysis of construction waste wood

被引:49
作者
Kim, Jeong Wook [1 ]
Lee, Hyung Won [1 ]
Lee, In-Gu [2 ]
Jeon, Jong-Ki [3 ]
Ryu, Changkook [4 ]
Park, Sung Hoon [5 ]
Jung, Sang-Chul [5 ]
Park, Young-Kwon [1 ,6 ]
机构
[1] Univ Seoul, Grad Sch Energy & Environm Syst Engn, Seoul 130743, South Korea
[2] Korea Inst Energy Res, Taejon 303343, South Korea
[3] Kongju Natl Univ, Dept Chem Engn, Cheonan 330717, South Korea
[4] Sungkyunkwan Univ, Sch Mech Engn, Suwon 440746, South Korea
[5] Sunchon Natl Univ, Dept Environm Engn, Sunchon 540950, South Korea
[6] Univ Seoul, Sch Environm Engn, Seoul 130743, South Korea
基金
新加坡国家研究基金会;
关键词
Construction waste wood; Pyrolysis; Reactor; Bio-oil; Reaction conditions; Catalyst; CATALYTIC PYROLYSIS; FLUIDIZED-BED; OPERATING PARAMETERS; MANDARIN RESIDUE; KINETICS; THERMOGRAVIMETRY; CHEMICALS; ZEOLITE; LIGNIN; CAKE;
D O I
10.1016/j.renene.2013.07.009
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The pyrolysis characteristics of construction waste wood were investigated for conversion into renewable liquid fuels. The activation energy of pyrolysis derived from thermogravimetric analysis increased gradually with temperature, from 149.41 kJ/mol to 590.22 kJ/mol, as the decomposition of cellulose and hemicellulose was completed and only lignin remained to be decomposed slowly. The yield and properties of pyrolysis oil were studied using two types of reactors, a batch reactor and a fluidized-bed reactor, for a temperature range of 400-550 degrees C. While both reactors revealed the maximum oil yield at 500 degrees C, the fluidized-bed reactor consistently gave larger and less temperature-dependent oil yields than the batch reactor. This type of reactor also reduced the moisture content of the oil and improved the oil quality by minimizing the secondary condensation and dehydration. The oil from the fluidized-bed reactor resulted in a larger phenolic content than from the batch reactor, indicating more effective decomposition of lignin. The catalytic pyrolysis over HZSM-5 in the batch reactor increased the proportion of light phenolics and aromatics, which was helpful in upgrading the oil quality. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:41 / 48
页数:8
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