离心风机及其下游管道内非定常流动的分离涡模拟数值研究

J. Cai, Jiaqing Zhang, Can Yang
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引用次数: 1

摘要

利用计算流体力学(CFD)软件ANSYS FLUENT,研究了离心风机及其下游管道在最佳效率点(BEP)流量下的三维非定常湍流。出口直径为400mm的叶轮有12个前弯叶片。计算域包括四个部分:进口部分、叶轮、蜗壳和下游管道。在ANSYS ICEM-CFD中采用结构化六面体单元进行流域网格划分,共使用了近900万个单元。采用分离涡模拟(DES)湍流建模方法,采用了足够精细的网格格式。将叶轮设置为转速为2900 rpm的旋转区域。采用滑动网格技术处理叶轮与静止部件之间的非定常相互作用;非定常相互作用在离心风机内部产生压力波动。一次叶轮旋转被划分为2048个时间步长,以便高分辨率地捕捉瞬态流动现象。沿蜗壳剖面和下游管道中心线设置监测点。当数值模拟在叶轮转数稳定后,开始对非定常流场进行统计,总共有16384个时间步长(8个叶轮转数)数据。保存各监测点压力和速度幅值的时程数据,应用傅里叶变换得到其频谱。时间平均流场清楚地表明,静压在叶轮内逐渐上升,并从蜗壳内的速度进一步恢复,沿下游管道由于摩擦而逐渐降低。叶轮叶片压力侧的平均压力大于吸力侧的平均压力,形成了周向非均匀流型。由于叶片前弯,叶轮出口周围存在较大的速度区,尾缘附近的最大速度可达1.5u2,其中u2为叶轮出口的周向速度。压力波动的均方根值分布表明,离心风机内部大部分部位存在较大的压力波动,波动幅度约为参考动压pref = 0.5ρu22的10%;沿出口管道压力波动幅度迅速减小,5D后(D为出口管径)为pref的0.5%。蜗壳内各监测点的压力和速度波动谱在过叶频率及其二、三次谐波处呈现出明显的离散分量。BPF分量在舌部区域的值最大,为pref的15%,在5D距离后,BPF分量沿下游管道急剧减小,幅度小于pref的0.2%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Numerical Study of the Unsteady Flow Inside a Centrifugal Fan and its Downstream Pipe Using Detached Eddy Simulation
The 3-D unsteady turbulent flow inside a centrifugal fan and its downstream pipe is investigated at the best efficiency point (BEP) flow rate using the computational fluid dynamics (CFD) package ANSYS FLUENT. The impeller with an outlet diameter of 400 mm has 12 forward curved blades. The computational domain comprises four parts: the inlet part, the impeller, the volute, and the downstream pipe. The flow domain was meshed in ANSYS ICEM-CFD with structured hexahedron cells, and nearly 9 million cells were used. The Detached Eddy Simulation (DES) turbulence modelling approach was employed with this fine enough mesh scheme. The impeller was set as the rotating domain at a speed of 2900 rpm. A sliding mesh technique was applied to the interfaces in order to allow unsteady interactions between the rotating impeller and the stationary parts; the unsteady interactions generate pressure fluctuations inside the centrifugal fan. One impeller revolution is divided into 2048 time steps, in order to capture the transient flow phenomena with high resolution. Monitoring points were set along the volute casing profile, and along the downstream pipe centerline. When the numerical simulation became stable after several impeller revolutions, the statistics of the unsteady flow was initiated with a total of 16384 time steps (8 impeller revolutions) data. The time history data of the pressure and velocity magnitude at the monitoring points were saved and with Fourier transform applied to obtain the frequency spectra. The time-averaged flow fields show clearly the static pressure rises gradually through the impeller, and further recovers from the velocity in the volute, and decreases gradually along the downstream pipe due to the friction. The mean pressure at the pressure side of the impeller blade is larger than it at the suction side, forming the circumferential nonuniform flow pattern. Owing to the forward-curved blades, large velocity region exists around the impellor exit, and the maximum velocity near the trailing edge can reach 1.5u2, where u2 is the circumferential velocity at the impeller outlet. The root mean square (rms) value distribution of pressure fluctuations show that most parts inside the centrifugal fan undergo large pressure fluctuation with the magnitude about 10% of the reference dynamic pressure pref = 0.5ρu22; the maximum value locating at the tongue tip can reach 30% of pref. The pressure fluctuation magnitude decreases quickly along the outlet pipe: after 5D (D is the outlet pipe diameter) the magnitude is 0.5% of pref. The pressure and velocity fluctuation spectra at the monitoring points in the volute show striking discrete components at the blade-passing frequency (BPF) and its 2nd, 3rd harmonics. The BPF component has the maximum value of 15% of pref in the tongue region, and it decreases dramatically along the downstream pipe with the amplitude less than 0.2% of pref after 5D distance.
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