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Local void fraction and velocity field description in horizontal bubbly flow

机译:水平气泡流中的局部空隙率和速度场描述

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The internal phase distribution of concurrent, air--water bubbly flow in a 50.3-mm i.d. transparent horizontal pipeline has been experimentally investigated using the hot-film anemometry technique. Liquid and gas volumetric superficial velocities ranged from 3.8 to 5.0 m s~-1 and 0.25 to 0.8 m s~-1, respectively. The time-averaged local values of the void fraction, bubble-passing frequency, the mean liquid velocity, and the liquid turbulence fluctuations were measured. The experimental results indicate that the void fraction and bubble-passing frequency have local maxima near the upper pipe wall, and the profiles tend to flatten with increasing liquid flow rate. For the horizontal bubbly flow, the observed time-averaged local void fraction can reach 65/100, whereas the bubble frequency may reach a value of 1400 s~-1. The fact that the local peak void fraction in all cases never exceeds 65/100, indicates that the maximum bubble packing exists within the channel. It was found that increasing the gas flow rate at fixed liquid flow rate would increase the local void fraction and bubble-passing frequency. The axial liquid mean velocity showed a relatively uniform distribution except near the upper pipe wall, where a sharp reduction in velocity was noticed. The local mean liquid velocity and turbulence fluctuations increased with gas flow rate. An interesting feature of the liquid velocity distribution is that it tends to form a fully-developed turbulent pipe-flow profile at the lower part of the pipe irrespective of the liquid and gas superficial velocities. At very low local void fractions, the turbulent intensity consistently tended to be slightly lower than the single-phase. However, at high void fraction, i.e. high bubble population, introduction of gas strongly enhances the turbulence level as characterized by the turbulent velocity fluctuation and turbulent intensity. In general, it was concluded that the local turbulence intensity is mainly affected by the local void fraction distribution.
机译:空气-水同时气泡流的内相分布为50.3毫米内径。透明水平管道已通过热膜风速技术进行了实验研究。液体和气体的表观速度分别为3.8至5.0 m s〜-1和0.25至0.8 m s〜-1。测量了空隙率,气泡通过频率,平均液体速度和液体湍流波动的时间平均局部值。实验结果表明,空隙率和气泡通过频率在上管壁附近具有局部最大值,并且随着液体流速的增加,轮廓趋于平坦。对于水平气泡流,观测到的时间平均局部空隙率可以达到65/100,而气泡频率可以达到1400 s〜-1。在所有情况下,局部峰值空隙率从未超过65/100的事实表明,通道内存在最大气泡堆积。发现以固定的液体流量增加气体流量将增加局部空隙率和气泡通过频率。轴向液体平均速度显示出相对均匀的分布,除了在上管壁附近,那里的速度急剧下降。局部平均液体速度和湍流波动随气体流速增加。液体速度分布的一个有趣特征是,无论液体和气体的表观速度如何,它都倾向于在管道的下部形成完全发展的湍流管道。在非常低的局部空隙率下,湍流强度始终趋于略低于单相。然而,在高空隙率,即高气泡数下,引入气体强烈地增强了湍流水平,其特征在于湍流速度波动和湍流强度。总的来说,得出的结论是局部湍流强度主要受局部空隙率分布的影响。

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