A Systematic Approach to Determining the Kinetics of the Combustion of Biomass Char in a Fluidised Bed Reactor

被引:0
作者
Newman, S. G. [1 ]
Kwong, K. Y. [1 ]
Marek, E. J. [1 ]
机构
[1] Univ Cambridge, Dept Chem Engn & Biotechnol, Philippa Fawcett Dr, Cambridge CB3 0AS, England
关键词
biochar; kinetics; effectiveness factor; combustion; ACTIVE PARTICLES; SOLID REACTIONS; MASS-TRANSFER; GASIFICATION; MODEL; TEMPERATURE; EVOLUTION; OXYGEN; ORDER; CO;
D O I
10.3390/pr12102103
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The aim of this work was to investigate the combustion of biochar in a fluidised bed and determine the intrinsic kinetic parameters for combustion: pre-exponential constant Ai and activation energy Ei. When analysing the rates of reaction, Regimes I, II and III were demonstrated, with values for the activation energy of 155, 57 and 9 kJ/mol, respectively, when combustion was limited by different factors: intrinsic kinetics, intraparticle and external mass transport phenomena. These mass transport phenomena were decoupled from a set of 'apparent' kinetics incorporating effectiveness factors, which we used as a starting point in the determination of the intrinsic kinetic parameters. We also investigated a simple approach to model the evolution of the char structure over the course of oxidation using an empirical function, fX, fitted with an O(7) polynomial. We then reassessed the division into three combustion regimes by exploring the changes in fX and the intraparticle effectiveness factor that occurred upon increasing the combustion temperature. Overall, we demonstrate that experiments in a fluidised bed can be used to determine biochar kinetics in a simplified but trustworthy way.
引用
收藏
页数:13
相关论文
共 24 条
  • [1] EVOLUTION OF PORE SURFACE-AREA DURING NONCATALYTIC GAS SOLID REACTIONS .2. EXPERIMENTAL RESULTS AND MODEL VALIDATION
    BALLAL, G
    ZYGOURAKIS, K
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (09) : 1787 - 1796
  • [2] BHATIA SK, 1980, AICHE J, V26, P379, DOI 10.1002/aic.690260308
  • [3] Using an experimentally-determined model of the evolution of pore structure for the gasification of chars by CO2
    Dai, Peng
    Dennis, John S.
    Scott, Stuart A.
    [J]. FUEL, 2016, 171 : 29 - 43
  • [4] Combustion and gasification rates of lignocellulosic chars
    Di Blasi, Colomba
    [J]. PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2009, 35 (02) : 121 - 140
  • [5] The order with respect to oxygen and the activation energy for the burning of an anthracitic char in O2 in a fluidised bed, as measured using a rapid analyser for CO and CO2
    Fennell, P. S.
    Dennis, J. S.
    Hayhurst, A. N.
    [J]. PROCEEDINGS OF THE COMBUSTION INSTITUTE, 2009, 32 : 2051 - 2058
  • [6] Numerical approaches for thermochemical conversion of char
    Haugen, Nils Erland L.
    Loong, Brandon Ka Yan
    Mitchell, Reginald E.
    [J]. PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2022, 91
  • [7] Improving the accuracy of predicting effectiveness factors for mth order and Langmuir rate equations in spherical coordinates
    Hong, JH
    Hecker, WC
    Fletcher, TH
    [J]. ENERGY & FUELS, 2000, 14 (03) : 663 - 670
  • [8] Application of particle-scale modelling to the combustion of a char particle in a fluidised bed of CLOU particles
    Kwong, K. Y.
    Dennis, J. S.
    Marek, E. J.
    [J]. FUEL, 2023, 342
  • [9] Chemical Looping Combustion of a Biomass Char in Fe2O3-, CuO-, and SrFeO3-delta-Based Oxygen Carriers
    Kwong, K. Y.
    Harrison, A. R. P.
    Gebers, J. C.
    Dennis, J. S.
    Marek, E. J.
    [J]. ENERGY & FUELS, 2022, 36 (17) : 9437 - 9449
  • [10] Combustion of Biomass in Fluidized Beds: A Review of Key Phenomena and Future Perspectives
    Kwong, K. Y.
    Marek, E. J.
    [J]. ENERGY & FUELS, 2021, 35 (20) : 16303 - 16334