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首页> 外文期刊>Chemical Engineering Science >Hydrodynamics and scale-up of bubble columns in the heterogeneous regime: Comparison of bubble size, gas holdup and liquid velocity measured in 4 bubble columns from 0.15 m to 3 m in diameter
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Hydrodynamics and scale-up of bubble columns in the heterogeneous regime: Comparison of bubble size, gas holdup and liquid velocity measured in 4 bubble columns from 0.15 m to 3 m in diameter

机译:异质制度中的水动力学和泡沫柱扩大:在直径为0.15μm至3米的4个气泡塔中测量的气泡尺寸,气体堆积和液体速度的比较

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The development of CFD models coupled with Population Balance is a very promising topic concerning multiphase reactors. In the case of bubbly flows and bubble columns, a serious lack of local hydrodynamic characterizations still harms development and validation of relevant models. To fill partially this gap, a new bubble size measurement technique, previously introduced by Maximiano Raimundo et al. (2016), has been applied on a very wide range of bubble column diameters (from 0.15 m to 3 m) and superficial gas velocities (from 0.06 m/s to 0.35 m/s). Size measurements have been coupled with others concerning gas holdup and axial liquid velocity, in order to provide an experimental database allowing to clarify the scale-up rules and to assist future modelling works. Average bubble sizes have been measured as globally similar at every scale. Measured holdup and average liquid velocity confirm already reported behaviours at lower column diameters. Liquid velocity fluctuations also follow self-similar radial profiles and are proportional to the average liquid velocity at the centre of the column leading to a strong turbulence intensity. The fact that the quantity (gD)(1/2) appears as a natural velocity scale and the presence of strong gas-holdup gradients underline the similarity between bubble columns operated heterogeneous regime and free thermal convection in pipes. (C) 2019 Elsevier Ltd. All rights reserved.
机译:CFD模型的开发与人口平衡相结合是一个非常有前景的关于多相反应器的话题。在气泡流动和泡沫柱的情况下,严重缺乏局部流体动力学特征仍然损害了相关模型的发展和验证。为了填充部分这种差距,一种新的泡沫尺寸测量技术,以前由Maximiano Raimundo等人引入。 (2016)已应用于非常宽的泡泡柱直径(0.15米至3米)和浅表气体速度(0.06 m / s至0.35 m / s)。为了提供实验数据库,可以与其他有关气体储存和轴向液体速度的其他测量进行耦合。平均气泡尺寸已经在每个等级的全球相似的情况下被测量。测量的保持和平均液体速度确认在较低柱直径下已经报告的行为。液体速度波动也遵循自相似的径向型材,并且与柱中心的平均液体速度成比例,导致强大的湍流强度。数量(GD)(1/2)看起来作为自然速度刻度的事实,并且强的气体储存梯度的存在在泡沫柱之间的相似性下划线,在管道中的气泡柱之间的相似性和管道中的自由热对流。 (c)2019年elestvier有限公司保留所有权利。

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