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首页> 外文期刊>Desalination and water treatment >Simulation and experimental validation of Taylor-Couette flow in square cross-section container for water treatment reactor
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Simulation and experimental validation of Taylor-Couette flow in square cross-section container for water treatment reactor

机译:水处理反应器方形截面容器中泰勒-库埃特流的模拟和实验验证

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摘要

A vortex flow developed by a rotational cylindrical rod centrally placed in a container of square cross section was investigated experimentally and numerically. This configuration was analyzed given its potential use in water treatment. We focused the analysis on a relation of inner radius and side length L/r = 7.33. This ratio represents a warranty for vortex flow stability. Large ratios have the advantage of handling larger volumes with a sustained control of residence. The study was based on measuring velocity using particle image velocimetry, PIV and modelling the flow by computational fluid dynamics (CFD). Taylor-Couette cells on laminar-turbulent regimes developed for all the rotating conditions examined with Reynolds numbers between 2750 and 4950. The measurements revealed that turbulence intensity Tu increases in the radial direction towards the corners. This is by interaction fluid-walls, where corners act as natural baffles. Numerical simulations showed that secondary flows develop in the corners, with high levels of turbulence, which is important for mixing. It is shown that present configuration consumes less energy than a Taylor-Couette flow from classical concentric-cylinder systems. Heat transfer rate produced by imposed temperature conditions on the walls of the container affect vortex size and position modifying the flow structure observed in the pure dynamics case. The results indicate that configurations like square container-rotating cylinder may enhance water treatment.
机译:实验和数值研究了由旋转圆柱杆产生的涡流,该圆柱杆居中放置在方形横截面的容器中。考虑到其在水处理中的潜在用途,对该结构进行了分析。我们将分析重点放在内半径和边长L / r = 7.33的关系上。该比率表示涡流稳定性的保证。大比例的优点是可以在控制住所的情况下处理更大的体积。该研究基于使用粒子图像测速仪,PIV测量速度并通过计算流体力学(CFD)对流进行建模。在2750至4950年间的雷诺数检验的所有旋转条件下,层流湍流状态下的Taylor-Couette细胞得以发展。测量结果表明,湍流强度Tu在径向上朝向拐角沿径向增加。这是通过交互作用的流体墙进行的,其中角充当自然的挡板。数值模拟表明,二次流在拐角处发展,湍流程度很高,这对于混合很重要。结果表明,与传统的同心圆柱体系统的泰勒-库埃特流相比,当前配置消耗的能量更少。通过在容器壁上施加温度条件而产生的传热速率会影响涡流的大小和位置,从而改变纯动态情况下观察到的流动结构。结果表明,类似方形容器旋转缸的配置可以增强水处理能力。

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