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ANALYSIS OF CHEMICAL AND PHYSICAL PROCESSES DURING THE PYROLYSIS OF LARGE BIOMASS PELLETS.

机译:大型生物质球团热解过程中的化学和物理过程分析。

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The detailed chemical and physical processes that occur during the pyrolysis of large biomass pellets have been studied both experimentally and mathematically. The quantitative effects on product distribution of chemical composition and physical variables, such as external heat flux, pellet length, density and wood grain orientation, are determined systematically by using a Box-Behnken experimental design. The yield of each product is reported as a function of these variables in the form of a second order polynomial.; The experimental apparatus consists of a single pellet reactor with one-dimensional radiant heat flux (2-6 cal/cm('2)-sec) applied to a surface of the cylindrical pellet. Volatile products, which are collected by a cold trap and an automatic gas sampling system, are analyzed by gas chromatography. Temperatures along the pellet length are measured by an optical pyrometer and thermocouples, and the pellet density is obtained by an X-ray technique.; The theoretical analysis extends previous mathematical models to include a multi-step reaction mechanism which predicts char yield. Variable properties, heat, and mass transfer effects during the pyrolysis are also treated. The differential equations are solved using a finite difference method. Predictions of product distribution and volatile release rates as well as temporal temperature profiles are in good agreement with the experimental results. Modeling results indicate the temperature and product distribution are sensitive to the values of the rate coefficient for char production and thermal conductivity. Experimental results in large particle pyrolysis show a different maximum release rate for each volatile component which offers a possibility for increased selectivity. Heat flux has the most significant effect on the pyrolysis rate and product distribution. Pellet length and grain orientation are secondary. When the major heat flux is perpendicular to the wood grain, shrinkage can enhance the pyrolysis rate.; The results obtained from this study will be useful in many applications such as improving wood combustion and fire safety. The methodology used in this work may also apply to coal and oil-shale pyrolysis.
机译:大型生物质颗粒热解过程中发生的详细化学和物理过程已通过实验和数学方法进行了研究。使用Box-Behnken实验设计系统地确定了对化学成分和物理变量(例如外部热通量,颗粒长度,密度和木纹方向)等产品分布的定量影响。每个产品的产量以这些变量的函数形式报告为二阶多项式。实验设备由一个单颗粒反应器组成,该反应器将一维辐射热通量(2-6 cal / cm('2)-sec)施加到圆柱形颗粒的表面。通过冷阱和自动气体采样系统收集的挥发性产物通过气相色谱分析。沿颗粒长度的温度通过光学高温计和热电偶测量,并且颗粒密度通过X射线技术获得。理论分析扩展了先前的数学模型,以包括预测炭产量的多步反应机理。热解过程中的可变性质,热和传质效果也得到处理。微分方程使用有限差分法求解。产品分布和挥发性释放速率以及时间温度曲线的预测与实验结果非常吻合。建模结果表明,温度和产品分布对焦炭生产速率系数和导热系数敏感。大颗粒热解的实验结果表明,每种挥发性组分的最大释放速率不同,这为提高选择性提供了可能性。热通量对热解速率和产物分布具有最显着的影响。颗粒长度和晶粒取向是次要的。当主要热通量垂直于木纹时,收缩可提高热解速率。这项研究获得的结果将在许多应用中有用,例如改善木材燃烧和防火安全。这项工作中使用的方法也可能适用于煤和油页岩的热解。

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