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On the numerical study of isothermal vertical bubbly flow using two population balance approaches

机译:两种人口平衡方法对等温垂直气泡流的数值研究

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Two population balance approaches based on the MUltiple-SIze-Group (MUSIG) model and one-group average bubble number density (ABND) model for handling the bubble size distribution of gas-liquid bubbly flows under isothermal conditions are assessed. Three forms of coalescence and breakage mechanisms by Wu et al. [1998. One-group interfacial area transport in vertical bubbly flow. International Journal of Heat Mass Transfer 41, 1103-1112], Hibiki and Ishii [2002. Development of one-group interfacial area transport equation in bubbly flow systems. International Journal of Heat Mass Transfer 45, 2351-2372] and Yao and Morel [2004. Volumetric interfacial area prediction in upwards bubbly two-phase flow. International Journal of Heat Mass Transfer 47, 307-328] are incorporated in the ABND model. To examine the relative merits of both approaches, local radial distributions of five primitive variables in bubbly flows: void fraction, Sauter mean bubble diameter, interfacial area concentration, and gas and liquid velocities, are compared against the experimental data of Liu and Bankoff [1993a. Structure of air-water bubbly flow in a vertical pipe-I. Liquid mean velocity and turbulence measurements. International Journal of Heat Mass Transfer 36, 1049-1060; 1993b. Structure of air-water bubbly flow in a vertical pipe-II. Void fraction, bubble velocity and bubble size distribution. International Journal of Heat Mass Transfer 36, 1061-1072] and Hibiki et al. [2001. Axial interfacial area transport of vertical bubble flows. International Journal of Heat Mass Transfer 44, 1869-1888]. In general, both of the ABND model and MUSIG model predictions yield close agreement with experimental results. To account for the range of different bubble sizes in the gas-liquid bubbly flows; the resolution required is achieved through the application of the MUSIG model. Nevertheless, computational times increase by a factor of two when compared to applying the simpler ABND model. To further exploit the models' capabilities, investigations are carried out by extending the two population approaches beyond the bubbly flow regime of higher void fraction, particularly in the transition regime. The numerical results are found to be grossly over-predicted, which expose the inherent limitations of the models. It is known that bubbles in this regime are generally highly distorted and closely packed instead of spherical shape and allowed to move freely in bubbly flow regime. (C) 2007 Elsevier Ltd. All rights reserved.
机译:评估了两种基于等温群模型(MUSIGi-SIze-Group,MUSIG)和一组平均气泡数密度(ABND)的人口平衡方法,用于处理等温条件下气液气泡流的气泡尺寸分布。 Wu等人的三种形式的聚结和断裂机制。 [1998。垂直气泡流中的一组界面区域传输。国际传热传质杂志41,1103-1112],Hibiki and Ishii [2002。气泡流系统中一组界面面积输运方程的建立。国际热质传递杂志45,2351-2372]和Yao and Morel [2004。气泡状两相流向上的体积界面面积预测。 ABND模型中纳入了国际热传质杂志47,307-328]。为了检验两种方法的相对优点,将气泡中五个原始变量的局部径向分布:空隙率,Sauter平均气泡直径,界面面积浓度以及气体和液体速度与Liu和Bankoff [1993a 。垂直管Ⅰ中空气水气泡流的结构。液体平均速度和湍流测量。国际热质传递杂志36,1049-1060; 1993b。垂直管中的空气-气泡水流结构-II。空隙率,气泡速度和气泡尺寸分布。国际热传质杂志36,1061-1072]和Hibiki等。 [2001。垂直气泡流的轴向界面区域传输。国际热传质杂志44,1869-1888]。通常,ABND模型和MUSIG模型的预测都与实验结果密切相关。考虑到气液气泡流中不同气泡大小的范围;通过使用MUSIG模型可以实现所需的分辨率。但是,与应用更简单的ABND模型相比,计算时间增加了两倍。为了进一步利用模型的功能,通过将两种总体方法扩展到孔隙率较高的气泡流态之外,特别是在过渡态下,进行了研究。发现数值结果被严重高估了,这暴露了模型的固有局限性。众所周知,在这种状态下的气泡通常高度扭曲并且紧密堆积而不是球形,并且允许其在气泡流动状态下自由移动。 (C)2007 Elsevier Ltd.保留所有权利。

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