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Bubble size distribution in laboratory scale flotation cells

机译:实验室规模浮选池中的气泡尺寸分布

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Bubble size was measured in two lab scale cells using the HUT bubble size analyzer. The influence of operating conditions on bubble size was investigated. The Sauter mean bubble size was found to vary over the range of 1.2-2.9 mm. The experimental bubble size distributions were satisfactorily represented by the upper-limit distributions. The frothers were found to have a profound impact on bubble size. It seems that frothers not only prevent bubble coalescence, but they also, affect the bubble break-up process. The air flow rate was also found to have a strong influence on bubble size. The Sauter mean bubble diameter increased as the air flow rate increased. The Sauter mean bubble diameter was found to decrease with increasing impeller speed. The addition of quartz on the other hand was found to increase the size of bubbles, this effect was more evident at solid concentration exceeding 20 percent (kg/kg). The size of bubbles generated with the multi-mix and free-flow mechanisms were different at similar operating conditions, in a non-coalescing environment. The free-flow design generated broader bubble size distributions than the multi-mix mechanism.
机译:使用HUT气泡尺寸分析仪在两个实验室规模的样品池中测量气泡尺寸。研究了操作条件对气泡尺寸的影响。发现Sauter平均气泡大小在1.2-2.9 mm的范围内变化。实验气泡尺寸分布令人满意地由上限分布表示。发现起泡剂对气泡尺寸有深远的影响。似乎起泡剂不仅防止气泡聚结,而且还影响气泡破裂过程。还发现空气流速对气泡尺寸有很大的影响。 Sauter平均气泡直径随空气流速的增加而增加。发现Sauter平均气泡直径随叶轮速度的增加而减小。另一方面,发现添加石英会增加气泡的尺寸,当固体浓度超过20%(kg / kg)时,这种效果更加明显。在非结块环境中,在类似的操作条件下,由多重混合和自由流动机制产生的气泡大小不同。与多重混合机构相比,自由流动设计产生的气泡尺寸分布更宽。

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