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Bubble column fluid dynamics, flow structures in slender columns with large-diameter ring-spargers

机译:气泡塔的流体动力学,带有大口径环流器的细长塔中的流动结构

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Bubble columns, when operated at higher superficial gas velocities, depict a chaotic flow behavior. However, it is generally observed that the long time average of its flow velocity pattern depicts a simple structure: The dispersion is rising close to the column axis and, by continuity, it is coming down again near the wall. Long columns, equipped with larger-diameter ring-spargers, depict an average flow pattern that deviates from this behavior. In the lower part of the column, the flow is moving downwards near the axis and rising close to the wall, while in the upper part of the column quite the opposite is observed. This phenomenon, already observed by Lapin et al. (Chem. Eng. Sci. 56 (2000) 239) in large industrial reactors, is examined in detail on the pilot scale. Experimental results are compared with numerical simulations based on the Euler-Lagrange representation of the Navier-Stokes equation system. (C) 2002 Published by Elsevier Science Ltd. [References: 12]
机译:当以较高的表观气体速度进行操作时,气泡塔显示出混乱的流动行为。但是,通常观察到其流速模式的长时间平均值描绘了一个简单的结构:色散在靠近色谱柱轴线的位置上升,并且由于连续性,它在壁附近再次下降。配备了较大直径的环状分布器的长柱形成偏离此行为的平均流态。在塔的下部,流体在轴附近向下移动并靠近壁上升,而在塔的上部,观察到相反的情况。 Lapin等人已经观察到这种现象。 (Chem.Eng.Sci.56(2000)239)在大型工业反应器中以中试规模进行了详细研究。将实验结果与基于Navier-Stokes方程系统的Euler-Lagrange表示的数值模拟进行比较。 (C)2002由Elsevier Science Ltd.发布[参考:12]

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