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Separation of Solid Particles by Density Difference in a Liquid–Solid Fluidized Bed

机译:通过液固流化床密度差分离固体颗粒

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References(14) Cited-By(6) To examine the separation characteristics of solid materials in the liquid-solid fluidized bed, the motion of one solid material immersed in the fluidized bed was examined. The fluidizing particles were put in the column and fluidized by the liquid flow. To reduce the effects of size and shape of a sample, the liquid velocity was set at a low value, i.e., relatively small particles were used as the fluidizing particles. The glass beads (ρp = 2500 kg/m3) whose diameters were 60, 100, 200 and 500 μm and the zirconia beads (ρp = 6000 kg/m3) whose diameters were 60 and 100 μm were used as the fluidizing particles. Tap water was used as the fluidizing liquid. One sample, whose density was adjusted, was immersed in the bed, and the existing height of the sample in the bed was examined for different liquid velocities, fluidizing particle diameters and densities, experimentally.When the liquid velocity is low and the apparent density of the particle bed is higher than that of the sample, the sample floats on the bed (floating region). As the liquid velocity increases, the apparent density of the bed decreases and the sample becomes to suspend in the bed (suspending region). Further increments of liquid velocity makes the sample settle at the bottom of the bed (settling region). As the liquid velocity increases, the apparent density of the particle bed decreases and the sample sinks in turn. The range of the non-dimensional sample existing height in the suspending region is affected by the diameter of the fluidizing particle, but is not affected by the density of the fluidizing particles.
机译:参考文献(14)引用(6)检查液体固体流化床中固体材料的分离特性,检查浸没在流化床中的一种固体材料的运动。将流化颗粒放入柱中并通过液体流动流化。为了减少样品的尺寸和形状的效果,液体速度设定为低值,即,使用相对较小的颗粒作为流化颗粒。玻璃珠(ρp= 2500kg / m3),其直径为60,100,200和500μm,其直径为60和100μm的氧化锆珠(ρp= 6000kg / m 3)作为流化颗粒。自来水用作流化液体。调节密度的一个样品浸入床中,并检查床中样品的现有高度,用于不同的液体速度,流化粒径和密度,实验。当液体速度低并且表观密度颗粒床高于样品的样品,样品浮在床上(浮动区域)。随着液体速度增加,床的表观密度降低,样品变为悬浮在床(悬浮区域)中。液体速度的进一步增量使得样品沉降在床的底部(沉降区域)。随着液体速度的增加,颗粒床的表观密度减小,并依次下水槽。悬浮区域中的非尺寸样品的存在高度的范围受流化颗粒的直径的影响,但不受流化颗粒的密度的影响。

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