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Aggregation and breakage processes in Taylor-Couette Flow

机译:Taylor-Couette流中的聚集和破坏过程

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A non-intrusive technique has been developed for measuring aggregation particle size distribution in a Taylor-Couette device, which is consisted of two concentric cylinders with the outer one at rest. A mono-dispersed particulate suspension with a mean particle diameter, d, of 9.6μm was introduced in a transparent cylindrical flow device. The suspension was illuminated by a fiber optic illuminator and captured with a CCD camera. The recorded images were analyzed by a line to determine the particle size information and two-dimensional floc structure fractal dimension, Dpf . Mean particle size increases slowly in the beginning, then undergoes an exponential growth stage; with the breakup becoming more significant, d43 grows slower and finally levels off. Similarly, the Dpf increases in the early stage due to the formation of more open flocs. Later on, it declines due to the reconstructuring process because of the formation of the more compact flocs and finally reaches a steady-state.
机译:已经开发出一种非侵入性技术,用于测量泰勒-库埃特装置中的聚集粒径分布,该装置由两个同心圆柱体组成,外部同心圆柱体处于静止状态。将平均粒径为9.6μm的单分散颗粒悬浮液引入透明的圆柱形流动装置中。悬浮液由光纤照明器照明,并由CCD相机捕获。用一条线对记录的图像进行分析,以确定粒度信息和二维絮凝结构分形维数Dpf。平均粒度在开始时缓慢增加,然后进入指数增长阶段;随着分手变得越来越重要,d43的生长速度变慢,最终趋于平稳。同样,由于形成了更多的疏松絮状物,Dpf在早期就增加了。后来,由于形成更致密的絮状物,它由于重建过程而下降,最终达到稳态。

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