脉冲波形对JIG设备高密度颗粒分层的影响

TecnoLogicas Pub Date : 2016-01-30 DOI:10.22430/22565337.585
M. Ospina-Alarcón, Arturo B. Barientos-Ríos, M. Bustamante-Rúa
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引用次数: 4

摘要

对脉动流化床跳汰选厂在四种不同脉动工况下的颗粒运动进行了研究。仿真中采用的波形有-正弦、三角形、锯齿形后向和锯齿形前向。利用CFD技术实现SIMPLE算法,从连续性方程和动量方程计算了水流场的二维局部速度。粒子的运动是用牛顿第二运动定律的力平衡来模拟的。将数学欧拉-拉格朗日模型推广到具有宽尺寸和密度分布的颗粒悬浮液中,计算了液固相互作用力。为了分析跳汰机中质点的运动,推导了包含虚质量、重力、压力梯度、阻力和巴塞特力在内的质点响应时间轨迹方程。研究表明,在跳模腔入口边界条件下,不同脉动剖面的粒子运动轨迹存在显著差异。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Influencia de la forma de onda de pulsación en la estratificación de partículas de alta densidad en un equipo JIG
A study of particle motion subjected to four different pulsation profiles on a pulsated fluidized bed jig concentrator was carried out. The profiles used in the simulation were – sinusoidal, triangle, sawtooth-backward and sawtooth-forward. Two-dimensional local velocities of the water flow field were calculated from the continuity and momentum equations by CFD techniques implementing SIMPLE algorithm. The particle motion is modeled by a forces balance applying the Newton’s second law of motion. Liquid-solid interactions forces are calculated by the mathematical Euler-Lagrangian model extended to a particle suspension having a wide size and density distribution. To analyze the particle motion in jig, we derived a trajectory equation for the response time of particle that include virtual mass, gravity, pressure gradient, drag and Basset forces. The study demonstrates significant differences in the particle trajectories for various pulsation profiles applied to the boundary condition at the inlet to the jig chamber.
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