Fast pyrolysis of oil mallee woody biomass: Effect of temperature on the yield and quality of pyrolysis products

被引:313
作者
Garcia-Perez, Manuel
Wang, Xiao Shan
Shen, Jun
Rhodes, Martin J.
Tian, Fujun
Lee, Woo-Jin
Wu, Hongwei
Li, Chun-Zhu
机构
[1] Monash Univ, Dept Chem Engn, Clayton, Vic 3800, Australia
[2] Washington State Univ, Dept Biol Syst Engn, Pullman, WA 99164 USA
[3] Curtin Univ Technol, Dept Chem Engn, Bentley, WA 6845, Australia
[4] Taiyuan Univ Technol, Dept Chem Engn, Taiyuan, Shanxi 030024, Peoples R China
关键词
D O I
10.1021/ie071497p
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper presents an investigation of the production of crude bio-oil, char, and pyrolytic gases from the fast pyrolysis of mallee woody biomass in Australia. The feedstock was ground, sieved to several narrow particle size ranges, and dried prior to pyrolysis in a novel laboratory-scale fluidized-bed reactor. The effects of pyrolysis temperature (350-600 degrees C), and biomass particle size (100-600 mu m), on the yields and composition of bio-oil, gas, and char are reported. In agreement with previous reports, the pyrolysis temperature has an important impact on the yield and composition of bio-oil, char, and gases. Biomass particle size has a significant effect on the water content of bio-oil. It is interesting to note that the temperature for maximum bio-oil yield, between 450 and 475 degrees C, resulted in an oil with the highest content of oligomers and, consequently, with the highest viscosity. Such observations suggest that the conventional viewpoint of pyrolyzing biomass at temperatures over 400 degrees C to maximize bio-oil yield needs to be carefully reevaluated, considering the final use of the produced bio-oil. The increases in oil yield with increasing temperature from 350 to 500 degrees C were mainly due to the increases in the production of lignin-derived oligomers insoluble in water but soluble in CH2Cl2. The yield and some fuel properties of the pyrolysis products were compared with those herein obtained for pine as well as those reported in the literature for other lignocellulosic feedstocks but using similar reactors.
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页码:1846 / 1854
页数:9
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