Particle sized distribution simulation for an industrial fluidised bed urea granulator by PNB method considering non-uniform growth rate

IF 0.9 Q4 ENGINEERING, CHEMICAL
H. Nemati, S. A. Shekoohi
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引用次数: 0

Abstract

ABSTRACT The present work is an extension of the PNB method. Contrary to the previous works, it is assumed that the growth rate of particles/granules is not constant along the granulator length and it depends on the granule mass flow rate and molten urea spray mass flowrate. With these assumptions, the governing equations were extracted, and the analytical solution was derived. Since this method is based on the particle number and the measured data are mass-based (defined based on mass fraction distribution), a general procedure was also proposed to transfer between number-based and mass-based quantities. Finally, the results were compared with measured data taken from a large-scale industrial urea granulator and close agreements were observed. This method is introduced as an effective tool for the simulation of other applications, like driers. GRAPHICAL ABSTRACT
考虑非均匀生长速率的PNB法模拟工业流化床尿素造粒机的粒度分布
摘要本工作是PNB方法的扩展。与之前的工作相反,假设颗粒/颗粒的生长速率沿造粒机长度不是恒定的,它取决于颗粒质量流量和熔融尿素喷雾质量流量。利用这些假设,提取了控制方程,并导出了解析解。由于该方法基于粒子数,并且测量数据基于质量(根据质量分数分布定义),因此还提出了一种在基于数量和基于质量的量之间转换的通用程序。最后,将结果与大型工业尿素造粒机的测量数据进行了比较,并观察到了密切的一致性。该方法是作为模拟其他应用(如干燥器)的有效工具引入的。图形摘要
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来源期刊
Indian Chemical Engineer
Indian Chemical Engineer ENGINEERING, CHEMICAL-
CiteScore
3.00
自引率
6.70%
发文量
33
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