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Flow Regime of Mineral Suspensions with Preserved Structure of Floes

机译:矿物悬浮液的流量

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The breakage mechanism of flocs in mineral suspensions under shearing is considered. The relationship of limiting dynamic shear stress, diameter of particles and flocculant consumption is determined. It is calculated that for the floc structure to be preserved, it is required that the maximum allowable flow velocity of suspensions in pipelines 0.2-0.6 m in diameter is on average 1.8, 2.6 and 3.9 m/s at flocculant consumptions of 50, 100 and 200 g/t, respectively. The inverse problem on minimum allowable diameters of pipelines is solved. At the suspension flow rates of 100-1000 m~3/h and flocculant consumption of 50-200 g/t, these values range from 0.1 to 0.4 m. The increase in the flocculant consumption by 2 times, all other things being equal, conditions reduction in the allowable diameter of pipelines by 20%.
机译:考虑了剪切下矿物悬浮液中絮凝物的破损机制。 确定了限制动态剪切应力,粒子直径和絮凝剂消耗的关系。 计算出用于保留的絮凝结构,需要在50,100和50,100和50,100和50,100和50,100和50,100和 分别为200克/吨。 解决了管道最小允许直径的反问题。 在100-1000 m〜3 / h的悬浮流速和50-200g / t的絮凝剂消耗,这些值范围为0.1至0.4米。 絮凝剂消耗的增加2次,所有其他内容相等,条件降低了管道的允许直径20%。

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