Kinetic Modeling and Simulation of Pyrolysis of Shrinking BiomassParticle in Fixed Bed Gasifier

M. G. Sobamowo, S. J. Ojolo, C. Osheku, A. Kehinde
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引用次数: 1

Abstract

A B S T R A C T Pyrolysis plays an integrated role in the biomass conversion processes. The development of good mathematical models which in consequent leads to the design of pyrolysis reactors. The biomass gasifier is paramount in the scientific studies and understanding of the very important process in the thermochemical conversion of the solid fuels. However, due to the complexities of the biomass reaction scheme, the pyrolysis of biomass is generally modeled on the basis of apparent kinetics. Moreover, it is generally accepted that most important parameters affecting the process are temperature, concentration, residence time and heating conditions. This work presents the simulations of the pyrolysis kinetics of shrinking biomass particle under non-isothermal and isothermal heating conditions. The developed models were used to investigate the effects of shrinkage, heating conditions and heating rates on the pyrolysis of wood. There is a good agreement when the results of the developed models were compared to the experimental results. Theresults of this work could be used in estimating the optimum parameters in the pyrolysis of biomass and in the design of some pyrolysis reactors.
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生物质颗粒收缩在固定床气化炉中的热解动力学建模与模拟
热解在生物质转化过程中起着综合作用。建立良好的数学模型,从而指导热解反应器的设计。生物质气化炉在科学研究和理解固体燃料热化学转化过程中非常重要的过程是至关重要的。然而,由于生物质反应方案的复杂性,生物质热解通常基于表观动力学建模。此外,人们普遍认为影响工艺的最重要参数是温度、浓度、停留时间和加热条件。本文模拟了非等温和等温加热条件下收缩生物质颗粒的热解动力学。利用所建立的模型研究了收缩率、加热条件和加热速率对木材热解的影响。将所建模型的计算结果与实验结果进行了比较,结果吻合较好。研究结果可用于生物质热解过程中最佳参数的确定和某些热解反应器的设计。
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