基于Weibull和Dincer模型的绿色颗粒干燥特性

Xiaoping Zhang , Zihao Fan , Hongliang Wu , Junqiang Cong , Jialong Yang , Baoliang Wen
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引用次数: 0

摘要

绿色颗粒的干燥是颗粒生产过程中的关键步骤。为了优化和控制生料颗粒的干燥过程,有必要了解不同干燥条件下生料颗粒水分随时间的变化。本研究考察了不同干燥条件对绿色颗粒干燥特性的影响,并评价了Weibull和Dincer模型在描述绿色颗粒干燥过程中的适用性。结果表明:青粒的干燥过程可分为加速和减速两个阶段,不存在恒速率阶段;提高干燥空气温度和风速,减小干燥层重,减小生粒直径,有利于缩短生粒的干燥完成时间。Weibull和Dincer模型可以准确地描述绿色颗粒的干燥行为,为确定绿色颗粒干燥过程中的水分扩散系数和传质系数值提供了一种简单可靠的方法。β和Bi值的计算表明,绿色颗粒的干燥过程受到内部和外部水分传递阻力的限制。计算得到绿色颗粒干燥过程的活化能Ea值为13.56 kJ mol−1。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Drying characteristics of green pellets based on the Weibull and Dincer models
The drying of green pellets is a critical step in the pellet production process. To optimize and control the drying process of green pellets, it is essential to understand the green pellets moisture variation over time under different drying conditions. This study investigates the impact of various drying conditions on the drying characteristic of green pellets and evaluates the applicability of the Weibull and Dincer models in describing the drying process of green pellets. The results show that the drying process of green pellets can be divided into acceleration and deceleration periods, with no constant-rate period. Increasing the drying air temperature and air velocity, decreasing the drying layer weight, and reducing the green pellets diameter help shorten the drying completion time of green pellets. The Weibull and Dincer models can accurately describe the drying behavior of green pellets, providing a simple yet reliable method for determining the moisture diffusivity and mass transfer coefficient values during the drying process of green pellets. The calculations of β and Bi values suggest that the drying process of green pellets is limited by both internal and external moisture transfer resistances. The activation energy Ea value for the drying process of green pellets is calculated to be 13.56 ​kJ ​mol−1.
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