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Chaotic mixing of granular materials in two-dimensional tumbling mixers

机译:二维翻滚混合机中颗粒物料的混沌混合

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摘要

We consider the mixing of similar, cohesionless granular materials in quasi-two-dimensional rotating containers by means of theory and experiment. A mathematical model is presented for the flow in containers of arbitrary shape but which are symmetric with respect to rotation by 180 deg and half-filled with solids. The flow comprises a thin cascading layer at the flat free surface, and a fixed bed which rotates as a solid body. The layer thickness and length change slowly with mixer rotation, but the layer geometry remains similar at all orientations. Flow visualization experiments using glass beads in an elliptical mixer show good agreement with model predictions. Studies of mixing are presented for circular, elliptical, and square containers. The flow in circular containers is steady, and computations involving advection alone (no particle diffusion generated by interparticle collisions)show poor mixing. In contrast, the flow in elliptical and square mixers is time periodic and results in chaotic advection and rapid mixing. Computational evidence for chaos in noncircular mixers is presented in terms of Poincare sections and blob deformation. Poincare sections show regions of regular and chaotic motion, and blobs deform into homoclinic tendrils with an exponential growth of the perimeter length with time. In contrast, in circular mixers, the motion is regular everywhere and the perimeter length increases linearly with time. Including particle diffusion obliterates the typical chaotic structures formed on mixing; predictions of the mixing model including diffusion are in good qualitative and quantitative(in terms of the intensity of segregation variation with time) agreement with experimental results for mixing of an initially circular blob in elliptical and square mixers. Scaling analysis and computations show that mixing in noncircular mixers is faster than that in circular mixers, and the difference in mixing times increases with mixer size.
机译:通过理论和实验,我们考虑在准二维旋转容器中混合类似,无内聚的颗粒材料。对于在任意形状的容器中的流动,提出了一个数学模型,该容器相对于旋转180度对称,并且一半填充了固体。该流包括在平坦的自由表面上的薄级联层,以及作为固体旋转的固定床。层的厚度和长度随着搅拌器的旋转而缓慢变化,但是层的几何形状在所有方向上都保持相似。在椭圆形混合器中使用玻璃珠的流动可视化实验与模型预测显示出良好的一致性。提出了对圆形,椭圆形和正方形容器进行混合的研究。圆形容器中的流量稳定,仅涉及对流的计算(粒子间碰撞不会产生粒子扩散)显示出不良的混合。相反,椭圆和方形混合器中的流动是周期性的,并导致混乱的对流和快速混合。非圆形混合器中的混沌的计算证据以庞加莱截面和斑点变形的形式给出。 Poincare切片显示规则运动和混沌运动,并且斑点变形为同斜肌卷须,其周长随时间呈指数增长。相反,在圆形混合器中,运动在任何地方都是规则的,并且周长随时间线性增加。包括粒子扩散,消除了混合时形成的典型混沌结构;包括扩散在内的混合模型的预测在定性和定量上(就随时间变化的偏析强度而言)与在椭圆形和方形混合器中混合初始圆形斑点的实验结果一致。标度分析和计算表明,在非圆形混合器中混合比在圆形混合器中混合快,并且混合时间的差异随着混合器尺寸的增加而增加。

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