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EXPERIMENTAL AND MODELING INVESTIGATION OF LIGNITE DRYING IN A FLUIDIZED BED DRYER

机译:流化床烘干机中褐煤干燥的实验和建模研究

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The nitrogen as drying medium and the fluidized bed were used to study the drying characteristics of two kinds of lignite. The results show that the drying process of the lignite could be divided into three stages: a pre-heating period, a constant heating period, and a quick-down heating period. For the same lignite sample, the drying rate of lignite samples increases with rising drying temperature or flow rate of drying medium. For the different lignite samples, the composition structure of lignite and the modes of occurrence of moisture in the lignite influence the drying characteristics of lignite, besides drying medium temperature and flow rate influence lignite drying. According to the heat transfer rule equation of wet-ball in the forced flow, the drying rate formula of lignite particle in the fluidized bed has been got based on the heat transfer theory and mass transfer theory, and the formula can well interpret the effect of the experimental parameters on the lignite drying.
机译:氮作为干燥介质和流化床用于研究两种褐煤的干燥特性。结果表明,褐煤的干燥过程可分为三个阶段:预热时段,恒定加热时段和快速加热时段。对于相同的褐煤样品,褐煤样品的干燥速率随着干燥温度的上升或干燥介质的流速而增加。对于不同的褐煤样品,除了干燥介质温度和流速影响褐煤干燥之外,褐煤中褐煤的组成结构和褐煤中水分的发生模式影响了褐煤。根据湿球在强制流动中的传热规则方程,基于传热理论和传统转移理论的流化床中褐煤颗粒的干燥速率配方,配方可以很好地解释效果褐煤干燥的实验参数。

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