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Analysis of slurry flow regimes downstream of a pipe bend

机译:分析弯管下游的泥浆流态

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The influence of the pipe bend between downward and horizontal flows on transition velocities between slurry flow regimes in a horizontal pipe has been characterized using electrical resistance tomography. The experiments have been carried out using a pipe loop of diameter 0.076 and 10 m long. The slurry mixture consisted of water and 100 μm diameter glass beads. The influence of solids concentration and the distance from the bend outlet on transition velocities have been studied. Two transition velocities have been determined: the transition between a pseudo-homogenous flow and a heterogeneous flow and the limit deposit velocities at the onset of solid particle bed. Results have shown that the bend significantly contributes to the suspension of the solids particles and to the decrease in the transition velocities between the slurry flow regimes occurring in a horizontal pipe. The distance from the bend outlet where these transitions take place increases with the velocity. Furthermore, the solids concentration influences these transitions at low concentration while there is little influence at high concentration. These observations have been compared with correlations for the transition velocities in a horizontal pipe.
机译:利用电阻层析成像技术已经表征了向下和水平流之间的弯管对水平管中泥浆流态之间的过渡速度的影响。实验是使用直径为0.076且长度为10 m的管环进行的。浆料混合物由水和直径为100μm的玻璃珠组成。研究了固体浓度和到弯曲出口的距离对过渡速度的影响。已经确定了两个过渡速度:在固体颗粒床开始时,假均质流和非均质流之间的过渡以及极限沉积速度。结果表明,弯曲显着地促进了固体颗粒的悬浮,并降低了水平管中发生的浆料流动状态之间的转变速度。这些过渡发生的地方与弯曲出口的距离随着速度的增加而增加。此外,固体浓度在低浓度下影响这些转变,而在高浓度下影响很小。这些观察结果已与水平管中的过渡速度相关性进行了比较。

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