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Aggregation and breakage processes in Taylor-Couette Flow

机译:泰勒汤流量的聚集和破损过程

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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:已经开发了一种非侵入式技术,用于测量泰勒 - 耦合装置中的聚集粒度分布,其由两个在静止的外部圆柱体组成。在透明的圆柱形流量装置中引入具有平均粒径D的单分散颗粒状悬浮液,为9.6μm。悬浮液由光纤照明器照射并用CCD相机捕获。通过线路分析记录的图像以确定粒度信息和二维絮状结构分形维数DPF。在开始时平均粒度慢慢增加,然后经历指数增长阶段;随着分手变得更加重要,D43增长较慢,最终休息。同样,由于形成更多开放的絮状物,DPF在早期增加。后来,由于形成更紧凑的絮状物并且最终达到稳态,因此由于重建过程而导致的过程下降。

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