Misiulia Dzmitry, Lidén Göran, Antonyuk Sergiy
Institute of Particle Process Engineering, University of Kaiserslautern-Landau, Gottlieb-Daimler-Straße 44, 67663 Kaiserslautern, Rhineland-Palatinate Germany.
Department of Environmental Science, Stockholm University, Svante Arrhenius väg 8, 10691 Stockholm, Stockholm County Sweden.
Flow Turbul Combust. 2023;110(3):581-600. doi: 10.1007/s10494-023-00395-5. Epub 2023 Jan 24.
Three secondary flows, namely the inward radial flow along the cyclone lid, the downward axial flow along the external surface of the vortex finder, and the radial inward flow below the vortex finder (lip flow) have been studied at a wide range of flow rate 0.22-7.54 LPM using the LES simulations. To evaluate these flows the corresponding methods were originally proposed. The highly significant effect of the Reynolds number on these secondary flows has been described by equations. The main finding is that the magnitude of all secondary flows decrease with increasing Reynolds number. The secondary inward radial flow along the cyclone lid is not constant and reaches its maximum value at the central radial position between the vortex finder external wall and the cyclone wall. The secondary downward axial flow along the external surface of the vortex finder significantly increases at the lowest part of the vortex finder and it is much larger than the secondary flow along the cyclone lid. The lip flow is much larger than the secondary inward radial flow along the cyclone lid, which was assumed in cyclone models to be equal to the lip flow, and the ratio of these two secondary flows is practically independent of the Reynolds number.
利用大涡模拟(LES)在0.22 - 7.54升/分钟的宽流量范围内研究了三种二次流,即沿旋风分离器顶盖的径向向内流、沿旋风分离器排气管外表面的轴向向下流以及旋风分离器排气管下方的径向向内流(边缘流)。为了评估这些流动,最初提出了相应的方法。通过公式描述了雷诺数对这些二次流的高度显著影响。主要发现是所有二次流的大小都随雷诺数的增加而减小。沿旋风分离器顶盖的二次径向向内流并不恒定,在旋风分离器排气管外壁与旋风分离器壁之间的中心径向位置达到最大值。沿旋风分离器排气管外表面的二次轴向向下流在旋风分离器排气管的最下部显著增加,并且远大于沿旋风分离器顶盖的二次流。边缘流远大于沿旋风分离器顶盖的二次径向向内流,在旋风分离器模型中曾假定二者相等,并且这两种二次流的比值实际上与雷诺数无关。