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    气固分选流化床中二元混合物的表观黏度特性及其对分选过程影响

    Apparent viscosity characteristics of binary mixture in gas-solid separation fluidized bed and its influence on separation process

    • 摘要: 表观黏度是流体的基本属性,也是影响气固流态化干法分选过程颗粒运动行为的重要因素。通过落球法研究了磁铁矿粉和不同含量煤粉所形成的二元混合加重质的表观黏度,并通过分选试验探究了不同黏度条件下煤炭的分选效率和效果。试验结果表明流化床的表观黏度随着二元混合加重质中磁铁矿粉的质量分数降低而减小,煤粉质量分数每提升2%,床层表观黏度平均下降0.12 Pa·s;随着操作气速从9.5 cm/s提升到12.2 cm/s,表观黏度下降约55%。基于试验结果修正了二元混合加重质表观黏度模型。在床层密度一定的情况下,不同操作条件下的表观黏度存在差异,表观黏度的增加不仅使各粒径煤炭沉降时间增加,且分选的可能偏差也随表观黏度的增加而增大。综上,在气固流化床分选过程中通过调控二元加重质黏度特性可以提升分选效果和效率,实现矿物的高效干法分选。

       

      Abstract: Apparent viscosity is a fundamental property of fluids and a crucial factor influencing particle motion behavior in gas-solid fluidized dry separation processes. The apparent viscosity of binary mixed heavy media formed by magnetite powder and coal powder with varying content was studied using the falling sphere method. Furthermore, separation experiments were conducted to explore the coal separation efficiency and effectiveness under different viscosity conditions. The results indicate that the apparent viscosity of the fluidized bed decreases as the mass fraction of magnetite powder in the binary mixed heavy media decreases, with an average reduction of 0.12 Pa·s for every 2% increase in coal powder content. As the operating gas velocity increases from 9.5 cm/s to 12.2 cm/s, the apparent viscosity drops by approximately 55%. Based on the experimental results, the apparent viscosity model for binary mixed heavy media was modified. At a constant bed density, differences in apparent viscosity exist under various operating conditions. An increase in apparent viscosity not only prolongs the settling time of coal particles of various sizes but also enlarges the potential deviation in separation. In summary, regulating the viscosity characteristics of binary heavy media during gas-solid fluidized bed separation can enhance separation effectiveness and efficiency, achieving efficient dry separation of minerals.

       

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