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Effect of the 6PBT stirrer eccentricity and off-bottom clearance on mixing of pseudoplastic fluid in a stirred tank

机译:6PBT搅拌器偏心距和底部间隙对搅拌槽中假塑性流体混合的影响

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The aim of this work is to investigate the effect of the shaft eccentricity on the flow field and mixing characteristics in a stirred tank with the novel stirrer composed of perturbed six-bent-bladed turbine (6PBT). The difference between coaxial and eccentric agitations is studied using computational fluid dynamics (CFD) simulations combined with standard k?ε turbulent equations, that offer a complete image of the three-dimensional flow field. In order to determine the capability of CFD to forecast the mixing process, particle image velocimetry (PIV), which provide an accurate representation of the time-averaged velocity, was used to measure fluid velocity. The test liquid used was 1.25%(wt) xanthan gum solution, a pseudoplastic fluid with a yield stress. The comparison of the experimental and simulated mean flow fields has demonstrated that calculations based on Reynolds-averaged Navier-Stokes equations are suitable for obtaining accurate results. The effects of the shaft eccentricity and the stirrer off-bottom distance on the flow model, mixing time and mixing efficiency were extensively analyzed. It is observed that the microstructure of the flow field has a significant effect on the tracer mixing process. The eccentric agitation can lead to the flow model change and the non-symmetric flow structure, which would possess an obvious superiority of mixing behavior. Moreover, the mixing rate and mixing efficiency are dependent on the shaft eccentricity and the stirrer off-bottom distance, showing the corresponding increase of the eccentricity with the off-bottom distance. The efficient mixing process of pseudoplastic fluid stirred by 6PBT impeller is obtained with the considerably low mixing energy per unit volume when the stirrer off-bottom distance, C , is T /3 and the eccentricity, e , is 0.2. The research results provide valuable references for the improvement of pseudoplastic fluid agitation technology.
机译:这项工作的目的是研究带有偏心六弯叶轮式涡轮机(6PBT)的新型搅拌器在搅拌槽中轴偏心率对流场和混合特性的影响。使用计算流体动力学(CFD)模拟与标准k?ε湍流方程相结合,研究了同轴搅拌和偏心搅拌之间的差异,从而提供了三维流场的完整图像。为了确定CFD预测混合过程的能力,使用了颗粒图像测速仪(PIV)(可提供时间平均速度的准确表示)来测量流体速度。使用的测试液体是1.25%(wt)的黄原胶溶液,一种具有屈服应力的假塑性流体。实验和模拟平均流场的比较表明,基于雷诺平均Navier-Stokes方程的计算适合获得准确的结果。广泛分析了轴的偏心距和搅拌器的底部距离对流动模型,混合时间和混合效率的影响。可以观察到,流场的微观结构对示踪剂混合过程具有重要影响。偏心搅动会导致流动模型的变化和非对称流动结构,从而具有明显的混合行为优势。而且,混合速率和混合效率取决于轴的偏心距和搅拌器的底下距离,表明偏心度随着底下距离的增加而增加。当搅拌器的底下距离C为T / 3且偏心率e为0​​.2时,可以用6PBT叶轮搅拌的假塑性流体进行有效的混合,而单位体积的混合能量却非常低。研究结果为伪塑性流体搅拌技术的改进提供了有价值的参考。

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