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Size Distributions of Micro-bubbles Generated by a Pressurized Dissolution Method

机译:加压溶解法产生的微气泡的尺寸分布

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Size of micro-bubbles is widely distributed in the range of one to several hundreds micrometers and depends on generation methods, flow conditions and elapsed times after the bubble generation. Although a size distribution of micro-bubbles should be taken into account to improve accuracy in numerical simulations of flows with micro-bubbles, a variety of the size distribution makes it difficult to introduce the size distribution in the simulations. On the other hand, several models such as the Rosin-Rammlcr equation and the Nukiyama-Tanazawa equation have been proposed to represent the size distribution of particles or droplets. Applicability of these models to the size distribution of micro-bubbles has not been examined yet. In this study, we therefore measure size distribution of micro-bubbles generated by a pressurized dissolution method by using a phase Doppler anemometry (PDA), and investigate the applicability of the available models to the size distributions of micro-bubbles. Experimental apparatus consists of a pressurized tank in which air is dissolved in liquid under high pressure condition, a decompression nozzle in which micro-bubbles are generated due to pressure reduction, a rectangular duct and an upper tank. Experiments are conducted for several liquid volumetric fluxes in the decompression nozzle. Measurements are carried out at the downstream region of the decompression nozzle and in the upper tank. The experimental results indicate that (1) the Nukiyama-Tanasawa equation well represents the size distribution of micro-bubbles generated by the pressurized dissolution method, whereas the Rosin-Rammler equation fails in the representation, (2) the bubble size distribution of micro-bubbles can be evaluated by using the NukiyamaTanasawa equation without individual bubble diameters, when mean bubble diameter and skewness of the bubble distribution are given, and (3) an evaluation method of visibility based on the bubble size distribution and bubble number density is proposed, and the evaluated visibility agrees well with the visibility measured in the upper tank.
机译:微气泡的尺寸广泛地分布在一到几百微米的范围内,并且取决于气泡产生后的产生方法,流动条件和经过时间。尽管在微气泡流动的数值模拟中应考虑微气泡的尺寸分布以提高精度,但是各种尺寸分布使得难以在仿真中引入尺寸分布。另一方面,已经提出了几种模型,例如,Rosin-Rammlcr方程和Nukiyama-Tanazawa方程来表示颗粒或液滴的尺寸分布。这些模型对微气泡尺寸分布的适用性尚未研究。因此,在这项研究中,我们通过使用相位多普勒风速计(PDA)测量通过加压溶解法产生的微气泡的尺寸分布,并研究可用模型对微气泡尺寸分布的适用性。实验装置由在高压条件下将空气溶解在液体中的加压罐,减压引起的微气泡的减压喷嘴,矩形导管和上部罐组成。对减压喷嘴中的几种液体体积通量进行了实验。在减压喷嘴的下游区域和上部储罐中进行测量。实验结果表明:(1)Nukiyama-Tanasawa方程很好地表示了加压溶解法产生的微气泡的尺寸分布,而Rosin-Rammler方程则无法表示,(2)当给出平均气泡直径和气泡分布的偏斜度时,可以通过使用NukiyamaTanasawa方程来评估气泡,而无需给出单个气泡直径,并且(3)提出了一种基于气泡尺寸分布和气泡数密度的可见度评估方法,并且评估的可见度与在上部水箱中测得的可见度非常吻合。

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