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Density-based separation in a vibrated Reflux Classifier with an air-sand dense-medium: Tracer studies with simultaneous underflow and overflow removal

机译:基于振动的反流分级机中基于密度的分离,采用空气沙稠介质:示踪剂研究,同时去除下溢和溢流

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摘要

The continuous separation of tracer particles in the air-sand dense-medium Reflux Classifier was investigated. The Reflux Classifier consisted of a 1 m long vertical fluidized bed section with a 2 m long channel inclined at 70° to the horizontal mounted above, both with a 20 × 100 mm cross section. Silica sand of 220 lm average diameter (-355 + 125 lm) was used as the dense medium. The Reflux Classifier produced good density separations for tracer particles ranging in size from 6.35 down to 1.0 mm. The density cut-point could be varied from 1418 to 2130 kg/m~3 by varying the underflow rate and the Ep was within the range of 0.06–0.46 × 103 kg/m~3 depending on particle size and gas rate. At certain gas flowrate and underflow conditions the density cut point ranged between 1534 and 1619 kg/m~3 across six particle sizes, suppressing the effects of particle size on the density cut point. As air rates increased from 4.03 to 5.64 × 10~(-4) m~3/s the density cut-point increased, as did the Ep. The results were compared with separations in a vertical fluidized bed of the same total length. Ep values in the vertical fluidized bed ranged between 0.07 and 1.49 × 10~3 kg/m~3 over the same experimental conditions as the inclined bed and the density cut point showed more variability with the conditions. The addition of an incline above the fluidized bed provides a more stable system allowing for greater separation efficiency and minimizing the effect of changing conditions. Increasing the flow of sand medium to the underflow decreased the density cut point while raising the gas rate increased the density cut point. Raising the gas rate also increased the variability of the system which resulted in a lower separation efficiency.
机译:研究了气砂重介质回流分级机中示踪剂颗粒的连续分离。回流分级机由一个1 m长的垂直流化床段和一个2 m长的通道组成,该通道相对于上方安装的水平方向倾斜70°,且横截面均为20×100 mm。使用平均直径为220 lm(-355 + 125 lm)的硅砂作为致密介质。 Reflux分类机可对示踪颗粒(尺寸从6.35到1.0 mm)进行良好的密度分离。通过改变底流速率,密度的临界点可以在1418至2130 kg / m〜3之间变化,Ep在0.06-0.46×103 kg / m〜3的范围内,具体取决于颗粒大小和气体速率。在一定的气体流量和下溢条件下,六种粒径的密度切点介于1534和1619 kg / m〜3之间,从而抑制了粒径对密度切点的影响。随着空气速率从4.03增加到5.64×10〜(-4)m〜3 / s,Ep。将结果与在相同总长度的垂直流化床中的分离进行了比较。在与倾斜床相同的实验条件下,垂直流化床的Ep值在0.07至1.49×10〜3 kg / m〜3的范围内,并且密度切点随条件的变化更大。在流化床上方增加倾斜度可提供更稳定的系统,从而提高分离效率,并将变化条件的影响降至最低。增加砂介质向底流的流量会降低密度极限,而提高气体流量会提高密度极限。提高气体速率也增加了系统的可变性,导致分离效率降低。

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