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The Investigation of Back-mixing Particles near dust outlet in cyclone separator with Tangential inlet

机译:带切口入口旋风分离器尘埃出口附近的背部混合颗粒的研究

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Based on experimental and computational fluid dynamics analysis, the phenomenon of particle back-mixing near the dust outlet in cyclone separator with tangential inlet was studied. The results show that particle back-mixing appears near the dust outlet geometry. Particle back-mixing can be divided into dust hopper back-mixing and discharge cone back-mixing for different generation mechanism. The upward flow coming from dust hopper, which occupies 17.7% of the inlet gas, can induce dust hopper back-mixing. The particle mass flow rate that caused by dust hopper back-mixing occupies 46.6% of total inlet particle mass flow rate. Precessing vortex core, bias flow and high turbulent intensity near the dust outlet can induce discharge cone back-mixing. For both dust hopper back-mixing and discharge cone back-mixing, particle back-mixing is serious near the dust outlet geometry, which occupies 56.8% of total inlet particle mass flow rate. Particle which is smaller than 18μm can mix backward. The axial distribution of particle concentration decreases sharply in a range of 1.5 D (cyclone diameter) height above the dust discharge port. At last, only 2.6% of back-mixing particles with diameter no bigger than 13 μm escape from vortex finder. This effect on separator efficiency increases with the particle diameter decreases.
机译:基于实验和计算流体动力学分析,研究了旋风出口附近旋风分出口与切向入口的尘埃出口附近的现象。结果表明,颗粒反混出现在尘埃出口几何形状附近。颗粒背部混合可分为除尘料斗后混合和排出锥体反混用于不同的产生机制。来自除尘器的向上流动,占据入口气体的17.7%,可以诱导尘埃料斗后搅拌。由料斗背部混合引起的颗粒质量流量占总入口粒子质量流量的46.6%。在尘埃出口附近的偏置涡旋核心,偏置流量和高湍流强度可以引起放电锥体背部混合。对于灰尘料斗背部混合和排出锥体背部混合,颗粒背部混合靠近尘埃出口几何形状,占总入口粒子质量流量的56.8%。小于18μm的粒子可以向后混合。颗粒浓度的轴向分布在排尘口上方的1.5d(旋风直径)高度的范围内急剧下降。最后,只有2.6%的背部混合颗粒的直径没有大于13μm的蒸煮器。这种对分离器效率的影响随粒径的增加而增加。

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