Simulation of Bubbling Fluidized Bed using a One-Dimensional Model Based on the Euler-Euler Method

C. Agu, Marianne S. Eikeland, Lars-André Tokheim, Britt M. E. Moldestad
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引用次数: 2

Abstract

The behaviour of a fluidized bed can be modeled based on the Euler-Euler approach. This method has been fully utilized in both three-dimensional (3D) and twodimensional (2D) systems for obtaining, for example, the axial and radial distribution of fluidized bed properties. However, the bed property such as void fraction distribution along the flow direction can be of great interest for a design purpose. To save computational cost, an appropriate one-dimensional (1D) model can be used to obtain the average bed property along the vertical axis of a fluidized bed. In this paper, a 1D model based on the Euler-Euler method is presented. The results show that the model can be used to describe the behaviour of a fluidized bed. With a reasonable accuracy, the results also show that the 1D model can predict the minimum fluidization velocity and the superficial gas velocity at the onset of slugging regime.
基于欧拉-欧拉法的鼓泡流化床一维模型模拟
流化床的行为可以基于欧拉-欧拉方法建模。该方法已在三维(3D)和二维(2D)系统中得到充分利用,例如,用于获得流化床特性的轴向和径向分布。然而,床层性质,如沿流动方向的空隙率分布,对于设计目的来说是非常有趣的。为了节省计算成本,可以采用合适的一维模型来计算流化床沿垂直轴的平均床层性质。本文提出了一种基于欧拉-欧拉法的一维模型。结果表明,该模型可以用来描述流化床的行为。结果还表明,一维模型可以在合理的精度下预测段塞流化状态开始时的最小流化速度和表面气速。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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