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首页> 外文期刊>Chemical Engineering Science >Design of novel hydrocyclone for improving fine particle separation using computational fluid dynamics
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Design of novel hydrocyclone for improving fine particle separation using computational fluid dynamics

机译:利用计算流体动力学设计改进细颗粒分离的新型水力旋流器

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摘要

Several novel hydrocyclones are designed to improve fine particle separation using computational fluid dynamics. The effects of inlet size, number of inlets and top-plate types on the particle separation efficiency and cut-size sharpness are discussed based on the same feed flow rates. The fluid and particle flows are simulated using a segregated, steady-state, 3-dimensional implicit numerical solver supplied by FLUENT software. The governing equations are coupled using the SIMPLE algorithm, while the Reynolds stress model is employed for the hydrocyclone turbulent model due to its' anisotropic nature. Particle trajectories are simulated based on a Lagrangian frame considering the continuous phase interactions. The simulated particle separation efficiencies approximately agree with the available experimental data. The results show that increasing the inlet number and narrowing the inlet width are effective ways to improve the particle separation efficiency due to the increase in fluid velocity in the cylindrical parts of hydrocyclone. A cone-shaped top-plate reduces the fine particle circulation area near the outer surface of overflow conduit, significantly improving the separation efficiency of fine particles. However, increasing the cone angle has a contrary effect because of the decrease in particle residence time. Although installing an extra guide-channel from the inlet may also improve the fine particle separation efficiency, it is not effective for particle classification because of reduced particle cut-size sharpness.
机译:设计了几种新型水力旋流器,以利用计算流体动力学来改善细颗粒的分离。基于相同的进料流速,讨论了进料口尺寸,进料口数量和顶板类型对颗粒分离效率和切粒锐度的影响。使用FLUENT软件提供的分离的稳态3维隐式数值求解器模拟流体和颗粒流。控制方程使用SIMPLE算法进行耦合,而雷诺应力模型由于其各向异性特性而被用于水力旋流器湍流模型。考虑连续相位相互作用,基于拉格朗日框架模拟粒子轨迹。模拟的颗粒分离效率与现有的实验数据大致吻合。结果表明,由于水力旋流器圆柱部分流体速度的增加,增加进口数量和缩小进口宽度是提高颗粒分离效率的有效途径。锥形顶板减小了溢流导管外表面附近的细颗粒循环面积,大大提高了细颗粒的分离效率。然而,由于减少了颗粒停留时间,增加锥角具有相反的效果。尽管从入口安装额外的引导通道也可以提高细颗粒的分离效率,但由于降低了颗粒切割尺寸的清晰度,因此对颗粒分类无效。

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