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DETACHMENT OF PARTICLES FROM BUBBLES IN A STIRRED CELL

机译:在搅拌的细胞中的泡沫脱离颗粒

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It has been conjectured that a reason for the poor recovery of coarse particles in flotation, is the detachment of large particles from bubbles in the turbulent shear flow that is present in mechanical flotation cells. The aim of this study is to observe the behaviour of particle-laden bubbles in a turbulent shear flow. An agitated vessel was constructed in which particle-laden bubbles could be introduced beneath the impeller. The bubbles were generated in a liquid-fluidised bed in a special compartment beneath the cell. The bed was composed of fine silica particles 110 to 250 μm in diameter, with an upflow of water containing DDA as collector. Bubbles were formed at the tip of a capillary tube within the bed, and particles were collected as the individual bubbles rose through the fluidised bed. These bubbles then rose one by one into the base of the flotation cell, into the path of the rotating impeller. Some of the particles became detached by the action of the impeller and settled to the base of the cell. Others remained attached to the bubble and rose to the top of the cell, where they were collected as the product. The detached particles, which settled in the base of the cell, and the particles that flowed over the lip of the cell, were collected and weighed. Experiments were conducted at various impeller speeds. Observed values of the fractional detachment were related to the mechanical energy dissipation rate in the region swept by the impeller, in the light of the classical theory of Schulze. According to this theory, a particle will become detached from a bubble in the centre of a rotating eddy, when the centrifugal force due to the rotation exceeds the capillary force holding the particle to the bubble. The theory predicts that a particle of given diameter will detach from a bubble of a given size, when Bo >1, where Bo is the Bond number. It was found that the theory overpredicts the Bond number for detachment by an order of magnitude. Approximately 80 per cent of the particles will detach at a Bond number of 0.08.
机译:据推测,浮选中粗颗粒释放差的原因是从机械浮选细胞中存在的湍流剪切流中的气泡中的大颗粒的分离。本研究的目的是在湍流剪切流中观察粒子上泡泡的行为。构建搅拌容器,其中可以在叶轮下引入颗粒上气泡。在细胞下方的特殊隔室中的液体流化床中产生气泡。床上由直径的细二氧化硅颗粒110至250μm组成,含有DDA的水溢为收集器。在床内的毛细管的尖端形成气泡,并且当各个气泡通过流化床上升时,收集颗粒。然后将这些气泡逐一升至浮选单元的底部,进入旋转叶轮的路径。一些颗粒通过叶轮的作用而脱离并沉淀到细胞基部。其他人仍然附着在泡沫上并升到细胞的顶部,在那里他们被收集为产品。收集并称重在细胞碱中沉降的分离的颗粒和流过细胞唇部的颗粒。实验以各种叶轮速度进行。鉴于Schulze的经典理论,观察到的分馏的数值与叶轮扫过的区域中的机械能量耗散速率有关。根据该理论,当由于旋转引起的离心力超过将颗粒保持在气泡中的离心力超过旋转涡流的中心,颗粒将从旋转涡流的中心脱离。该理论预测给定直径的粒子将从给定尺寸的气泡脱离,当BO> 1时,其中BO是键合数。结果发现,该理论通过数量级的阶数估计脱离的键合号。大约80%的颗粒将以0.08的粘合数分离。

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