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Three dimensional CFD modelling of the effect of some operating parameters on particle trajectories in a rotating fluidised bed combustors

机译:旋转流化床燃烧器中某些运行参数对颗粒轨迹影响的三维CFD建模

摘要

The objective of the research was to investigate the trajectories of particles in a horizontal rotating fluidised bed (RFB) combustor. Due to the conservation of momentum, the gases in a RFB are imparted a tangential velocity component which accelerates as they converge to the exit. Dependent upon the type and size of particle, this unique feature causes particles in the RFB to be returned to be bed, be captured and remained in circular orbit in the freeboard region of the primary chamber or be blown out of the combustor. Hence, computational fluid dynamics (CFD) modelling had been performed using the FLUENT program code to chart the trajectory of rice husk ash particles of various sizes in a RFB operated at different rotating speeds and air feed rates. It was found that, in general, particles of size less than 5um were rapidly blown out of the combustor while particles in the range of 10-50um were retained in the primary chamber. Larger-sized particles (>50um) tended to move towards the distributor due to higher momentum.
机译:该研究的目的是研究水平旋转流化床(RFB)燃烧器中颗粒的轨迹。由于动量守恒,RFB中的气体被赋予了切向速度分量,当它们收敛到出口时会加速。根据颗粒的类型和大小,此独特的功能会导致RFB中的颗粒返回到床中,被捕获并保留在主腔室干舷区域的圆形轨道中或吹出燃烧室。因此,已经使用FLUENT程序代码执行了计算流体动力学(CFD)建模,以绘制以不同转速和空气进给速率运行的RFB中各种尺寸的稻壳灰颗粒的轨迹。已发现,通常,尺寸小于5微米的颗粒会迅速从燃烧室中吹出,而10至50微米范围内的颗粒会保留在主室中。由于动量较大,较大的颗粒(> 50um)倾向于朝分配器移动。

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