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Direct Numerical Simulation of the Flow Fields in a Medium Reynolds Number Non-Baffled Stirred Tank (Re = 4,500) and Experimental Verification

机译:雷诺数无挡板搅拌槽(Re = 4,500)中流场的直接数值模拟和实验验证

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摘要

The fourth-order central finite difference scheme was applied to the convection terms in three-dimensional Navier-Stokes equations to simulate directly the flow fields in a medium Reynolds number (Re = 4,500) non-baffled stirred tank. The multi-block method was used for the computation. The rotational cylindrical coordinates with a constant angular velocity were used for the flow region including impellers and a disc. The usual cylindrical coordinates were applied to the other flow regions. The calculation was performed tosimulate the phenomena occuring in the case of water in a period of 64 seconds, which is sufficient time for obtaining varius flow mechanisms and time averaged flow characteristics in a stirred tank. Visualization of the calculated results shows the mechanism of large scale vortices, their interactions and merger. The calculated results are in good agreement with the measured data. This means that the simulation well describes the fluid motion in a real stirred tank with impellrs of complex geometry.
机译:将四阶中心有限差分方案应用于三维Navier-Stokes方程中的对流项,以直接模拟中等雷诺数(Re = 4,500)无挡板搅拌槽中的流场。多块方法用于计算。具有恒定角速度的旋转圆柱坐标用于包括叶轮和圆盘的流动区域。将通常的圆柱坐标应用于其他流动区域。进行计算以模拟在水的情况下在64秒内发生的现象,这对于在搅拌釜中获得可变流量机制和时间平均流量特性而言是足够的时间。计算结果的可视化显示了大型旋涡的机理,它们的相互作用和合并。计算结果与实测数据吻合良好。这意味着模拟可以很好地描述带有复杂几何形状叶轮的真实搅拌釜中的流体运动。

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