基于离散元法−体积法的螺旋溜槽多颗粒分选机理研究

Multi−Particle Separation Mechanism of Spiral Chute Based on DEM−VOF

  • 摘要: 为更精确地研究重力分选过程中螺旋溜槽内颗粒参数、入口流速和距径比对多相流流动特性及颗粒分选的影响机理,采用离散元法−体积法(DEM−VOF)数值模拟方法进行了系统性研究。研究表明:在多物理场如重力、离心力、流体阻力等的共同作用下,高密度和大粒径颗粒由于重力较大,表现出较高的流动速度,同时其回转半径较小,因此更倾向于向螺旋溜槽的内侧区域流动。溜槽内的多相流在进入第三圈时流体速度、颗粒速度、颗粒流动轨迹趋于稳定。提高入口流速可增强流体对颗粒的推动力,减少颗粒间相互作用,从而提升分选效率。在颗粒直径为2mm、距径比为0.4的条件下,入口流速从0.10 m/s增至0.20 m/s时,颗粒接触次数减少了95%以上。随着距径比增大,溜槽前三圈内颗粒的接触次数增加,而后两圈颗粒流带宽度减小、相对集中,有助于提升分离效率。因此,适当提高入口流速和距径比可有效提升复杂颗粒的分选效率。

     

    Abstract: A systematic study was conducted using the discrete element method combined with the volume of fluid (DEM−VOF) numerical simulation method to investigate the effects of particle parameters, inlet velocity and the ratio of distance (H) to diameter (D) on the multiphase flow characteristics and particle separation mechanisms in a spiral chute during the gravity separation process. The results show that the velocity of particles with high density and large particles increase due to their significant inertia under the influence of multiple physical fields, including gravity, centrifugal force, and fluid resistance. The average speeds of particles with densities of 1200 kg/m³ and 3000 kg/m³are 0.19 m/s and 0.34 m/s, respectively. This illustrates that the particles with a density of 1200 kg/m³increases by 78.94%. On the other hand, the average velocities of particles with a diameter of 4mm is 0.40m/s, which is 11.11% higher than that of particles with a diameter of 2 mm. In addition, these particles show a small turning radius. Thus, the particles are more inclined to flow towards the inner area of spiral chute. The fluid velocity, particle velocity, and particle flow track tend to stabilize when the multiphase flow in the spiral chute enteres the third circle. The increase in the inlet flow velocity enhances the fluid's driving force on particles and reduced interparticle interactions, thereby improving separation efficiency. Contact frequency of particle decreases by over 95% when the inlet velocity increases from 0.10m/s to 0.20m/s while the particle diameter and H/D ratio is fixed at 2mm and 0.4, respectively. Particle contact frequency increases within the first three circles and then decreases in the flow zone width of particle in the last two circles, which made the particles more concentrated. So the separation efficiency of particles is enhanced. In summary, the separation efficiency of complex particles improves when both the inlet flow velocity and H/D ratio increase.

     

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