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CFD modeling and analysis of the multiphase flow and performance of dense medium cyclones

机译:稠密旋风分离器多相流和性能的CFD建模与分析

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摘要

A computational fluid dynamics (CFD) model is proposed to describe the multiphase flow in a dense-medium cyclone (DMC). In this model, the volume of fluid (VOF) multiphase model is first used to determine the initial shape and position of the air core, and then the so called mixture model is employed to describe the flows of the medium, coal particles and air, where the turbulence is described by the Reynolds stress model. The validity of the proposed approach is verified by the reasonably good agreement between the measured and calculated results in terms of separation efficiency. On this base, this model is used to quantify the effects of the ratios of spigot to vortex finder diameters (U:O) and medium to coal (M:C) on performance. The results are shown to be generally comparable to those reported in the literature. It reveals that when vortex finder or spigot diameter is varied at the same U:O ratio, the offset and medium split nearly remain the same, however, the coal feed rate and E_p are different under the conditions considered. It is also shown that the fish-hook phenomenon is observed when spigot diameter is equal to or slightly larger than vortex finder diameter, and a normal operation becomes less stable with decreasing U:O ratio. The key phenomena predicted are explained by the calculated inner flows.
机译:提出了一种计算流体动力学(CFD)模型来描述密相气旋(DMC)中的多相流。在此模型中,首先使用流体体积(VOF)多相模型确定空心的初始形状和位置,然后使用所谓的混合模型描述介质,煤颗粒和空气的流动,雷诺应力模型描述了湍流。所提方法的有效性通过测量结果和计算结果在分离效率方面的合理良好一致性来验证。在此基础上,该模型用于量化凸台与涡流探测器直径之比(U:O)和中煤与煤之比(M:C)对性能的影响。结果显示总体上可与文献报道的结果相媲美。结果表明,在相同的U:O比下,当涡旋探测器或凸台直径发生变化时,偏移量和介质分裂几乎保持不变,但是,在所考虑的条件下,煤的进料速度和E_p有所不同。还显示出,当插口直径等于或略大于涡旋仪直径时,会观察到鱼钩现象,并且随着U∶O比的降低,正常操作变得不稳定。预测的关键现象由计算出的内部流量解释。

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