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首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >Scalar mixing in a turbulent stirred tank with pitched blade turbine: Role of impeller speed perturbation
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Scalar mixing in a turbulent stirred tank with pitched blade turbine: Role of impeller speed perturbation

机译:带有桨叶式涡轮的湍流搅拌罐中的标量混合:叶轮速度扰动的作用

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摘要

Mixing of a passive scalar inside a pitched blade turbine (PBT) impeller stirred tank (STR) is studied using large-eddy simulation (LES) coupled with the immersed boundary method (IBM) for resolving moving interfaces. Mixing time is calculated based on the 95% homogenization of the scalar over the entire tank volume. Growth rate of the unmixed tracer volume is observed in order to identify the effects of low frequency macroinstability (MI) oscillations. Mixing time is significantly reduced when the STR flow is perturbed using a step-change in the impeller speed with a specific MI frequency. The enhancement in turbulent kinetic energy and changes in mean flow field due to the perturbation is observed. The spatio-temporal behavior of the large-scale mixing structures for the fixed" impeller-speed case and the perturbed case are compared. The mechanism of mixing enhancement is further explored by observing dynamic changes in the concentration distribution and the velocity field over a perturbation cycle. Penalty in power requirement due to perturbation is calculated.
机译:使用大涡模拟(LES)和浸入边界方法(IBM)来研究变桨叶轮(PBT)叶轮搅拌罐(STR)内无源标量的混合,以解决运动界面的问题。混合时间是基于标量在整个储罐容积中的95%均质化计算的。观察未混合示踪剂体积的生长速率,以确定低频宏观不稳定性(MI)振荡的影响。当使用特定MI频率的叶轮速度的阶跃变化来扰动STR流量时,可大大减少混合时间。观察到湍流动能的增加和由于扰动引起的平均流场的变化。比较了固定“叶轮转速”情况和扰动情况下大型混合结构的时空行为。通过观察扰动下浓度分布和速度场的动态变化,进一步探讨了混合增强的机理。计算由于扰动引起的功率需求的损失。

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