Investigation of the intrinsic CO2 gasification kinetics of biomass char at medium to high temperatures

被引:91
作者
Lin, Leteng [1 ]
Strand, Michael [1 ]
机构
[1] Linnaeus Univ, Sch Engn Bioenergy, S-35195 Vaxjo, Sweden
关键词
Biomass; Char; Gasification kinetics; Aerosol; TEOM; COAL-CHAR; STEAM GASIFICATION; PARTICLES; COMBUSTION; CONVERSION; PYROLYSIS; MODEL;
D O I
10.1016/j.apenergy.2013.04.027
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
In total eight char samples from pelletized wood, miscanthus, and straw were prepared under various pyrolysis conditions. The CO2 gasification kinetics for each sample was established in the temperature range from 800 degrees C to 1300 degrees C by the combination of thermogravimetric analysis (TGA) and a novel aerosol-based method. The aerosol-based method was used for the high temperature range between 1100 degrees C and 1300 degrees C, by gasifying suspended char particles (0.5-10 mu m) in an oxidizing carrier gas. A tapered element oscillating microbalance (TEOM) was used to measure the change of mass concentrations of particles in the carrier gas, before and after gasification. The results showed that the aerosol-based method could be used to investigate the intrinsic gasification kinetics of biomass char, at least up to 1300 degrees C. All char samples showed similar reactivity in the low temperature range. However, above 1000 degrees C there were significant differences in reactivity, and at 1300 degrees C the conversion of the wood was in the order of 10 times faster than that of straw. The general char reactivity order in this study was wood > miscanthus > straw. (C) 2013 Published by Elsevier Ltd.
引用
收藏
页码:220 / 228
页数:9
相关论文
共 38 条
  • [1] Kinetics of woodchips char gasification with steam and carbon dioxide
    Ahmed, I. I.
    Gupta, A. K.
    [J]. APPLIED ENERGY, 2011, 88 (05) : 1613 - 1619
  • [2] [Anonymous], 2012, LIND ENG DRESD PURCH
  • [3] [Anonymous], 2009, REV TECHNOLOGIES GAS
  • [4] Kinetics of rice husk char gasification
    Bhat, A
    Bheemarasetti, JVR
    Rao, TR
    [J]. ENERGY CONVERSION AND MANAGEMENT, 2001, 42 (18) : 2061 - 2069
  • [5] BHATIA SK, 1980, AICHE J, V26, P379, DOI 10.1002/aic.690260308
  • [6] THE TECHNICAL AND ECONOMIC-FEASIBILITY OF BIOMASS GASIFICATION FOR POWER-GENERATION
    BRIDGWATER, AV
    [J]. FUEL, 1995, 74 (05) : 631 - 653
  • [7] Cortus AB, 2012, WOODROLL PROCESS
  • [8] Combustion and gasification rates of lignocellulosic chars
    Di Blasi, Colomba
    [J]. PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2009, 35 (02) : 121 - 140
  • [9] Kinetic modelling of steam gasification of various woody biomass chars: Influence of inorganic elements
    Dupont, Capucine
    Nocquet, Timothee
    Da Costa, Jose Augusto, Jr.
    Verne-Tournon, Christele
    [J]. BIORESOURCE TECHNOLOGY, 2011, 102 (20) : 9743 - 9748
  • [10] Properties of high ash coal-char particles derived from inertinite-rich coal: II. Gasification kinetics with carbon dioxide
    Everson, Raymond C.
    Neomagus, Hein W. J. P.
    Kaitano, Rufaro
    Falcon, Rosemary
    du Cann, Vivien M.
    [J]. FUEL, 2008, 87 (15-16) : 3403 - 3408