Fundamentals, kinetics and endothermicity of the biomass pyrolysis reaction

被引:487
作者
Van de Velden, Manon
Baeyens, Jan [1 ,2 ]
Brems, Anke [4 ]
Janssens, Bart [4 ]
Dewil, Raf [3 ,4 ]
机构
[1] Univ Warwick, Sch Engn, Coventry CV4 7AL, W Midlands, England
[2] UCL, Dept Chem Engn, London, England
[3] Katholieke Univ Leuven, Dept Chem Engn, Chem & Biochem Proc Technol & Control Sect, B-3001 Heverlee, Belgium
[4] Katholieke Univ Leuven, Dept Chem Engn, St Katelijne Waver, Belgium
关键词
Biomass; Pyrolysis; Kinetics; Heat of pyrolysis; Experimental and operating conditions; COMPUTATIONAL ASPECTS; FLASH PYROLYSIS; PROJECT; PART; WOOD; CELLULOSE; DECOMPOSITION; TEMPERATURE; DEGRADATION; PARTICLES;
D O I
10.1016/j.renene.2009.04.019
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The paper reviews the pyrolysis of biomass constituents and possible secondary reactions. Biomass pyrolysis yields mostly liquid and solid fuel, easy to store and transport. Relevant working conditions for experiments and large-scale operation are: (i) biomass particles < 200 mu m, (ii) a particle heating rate of at least about 80 K min(-1) and (iii) a reactor environment where the internal resistance to heat penetration is smaller than the external resistance to heat transfer (Biot-number, Bi < 1). The circumstances of TGA and DSC experiments meet these requirements and fully determine the reaction kinetics and endothermicity of the pyrolysis reaction. The reaction rate constant and the heat of reaction are essential parameters in the design of a pyrolysis reactor. For most of the biomass species tested, the first order reaction rate constant is large and >0.5 s(-1). The heat of reaction ranges from 207 to 434 kJ kg(-1). All results tie in with literature data, although the reader is cautioned in using literature data since experiments were not always performed under relevant testing conditions. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:232 / 242
页数:11
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