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PACKED BED COMBUSTION MODELING: A PROPOSED METHODOLOGY FOR INDUSTRIAL BIOMASS GRATE BURNERS

机译:袋式燃烧模型:工业生物质炉排燃烧器的拟议方法

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In this paper, a new approach for the combustion modelling of thick particles in a packed bed isrnpresented. This research work is mainly devoted to an industrial application, so it requires an adequate balancernbetween computational costs and accuracy. Consequently, the fuel bed is idealized as a porous medium with arnconstant volume and the different reactions that represent the particles combustion (drying, pyrolysis and charrnconversion) take place on its specific surface area. Over the bed, the gaseous species released during pyrolysis andrnchar reactions are oxidised thanks to the secondary air supply. Accordingly, a set of nine equations is applied for thernentire domain (fuel bed and freeboard) and each reaction rate is expressed under an Arrhenius form. Summing up, thernmethodology described in the present paper aims to investigate the modelling possibilities of packed bed combustionrnof solid biomass, which is not yet directly implemented in available CFD softwares. The results will be furtherrnvalidated for a medium-scale grate boiler, a promising firing technology for heat supply in both domestic andrnindustrial sectors, based on biomass combustion.
机译:本文提出了一种填充床中厚颗粒燃烧模型的新方法。这项研究工作主要致力于工业应用,因此需要在计算成本和准确性之间取得适当的平衡。因此,理想的燃料床是具有恒定体积的多孔介质,代表颗粒燃烧(干燥,热解和炭转化)的不同反应发生在其比表面积上。在床层上,由于二次空气的供应,在热解和炭反应期间释放的气态物质被氧化。因此,将一组九个方程式应用于整个温度域(燃料床和干舷),并且每个反应速率均以Arrhenius形式表示。综上所述,本文描述的方法学旨在研究填充床燃烧固体生物质的建模可能性,该模型尚未在可用的CFD软件中直接实现。结果将进一步验证中型炉排锅炉,这是一种基于生物质燃烧的家庭和工业领域供热的有前途的燃烧技术。

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