Experimental Studies of Interfacial Area in a Horizontal Slug Flow

J. Riznic, S. Lewis, G. Kojasoy
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Abstract

The internal flow structure of horizontal slug flow has been experimentally investigated by measuring the local interfacial area concentration, void fraction and interfacial velocity distribution. The four-sensor electroresistivity probe was used to detect the instantaneous interface velocities and interfacial area. Experimental studies were performed on the plug/slug flow regimes with an air-water system. Data were acquired at the axial location of L/D = 253 from the mixing chamber. Four different liquid flow rates in combination with five different gas injection rates were studied. The superficial liquid velocity was varied between 0.55 and 2.20 m/s and gas velocity between 0.27 and 2.20 m/s. With these experimental conditions, the total void fraction, including contributions from small and large slug bubbles, ranged from 10 to 70%. The void fraction measurements were checked against the raw signal data, high speed video recordings, and measurements obtained by the hot film anemometer probe. The agreement between the data was very good, confirming that the four-sensor probe measurements can be performed with a high degree of confidence. In the region of transition between plug and slug flow regime, with an increase in the gas flow rate, the number and contribution of the small follow-up bubbles increased. The increase in the liquid flow rate produced similar effects. The slug bubble frequency also increased with an increase in the gas velocity and also slugs are longer at higher gas flow rates. Total interfacial area concentration profile includes the contribution from both slugs and small follow-up bubbles. Experimental data showed higher interfacial area concentration in the lower part of a slug bubble, with a larger curvature of interface. This is expected, since along the steeper curvature a ratio of local surface area to volume is increasing. Radial profiles of interfacial area concentration for slug bubbles show almost a flat profile in the upper part of slug bubble. The larger values of the total interfacial area concentration indicates that the contribution from the small bubbles is increasing. Experiments showed that in the plug/slug flow regime, contribution from the increasing number of small bubbles to the interfacial area concentration is substantial in upper part of the horizontal channel.
水平段塞流界面面积的实验研究
通过测量局部界面面积浓度、空隙率和界面速度分布,对水平段塞流的内部流动结构进行了实验研究。采用四传感器电阻率探头检测界面瞬时速度和界面面积。实验研究了在空气-水系统下的塞/段塞流态。在混合室L/D = 253的轴向位置获取数据。研究了四种不同的液体流速和五种不同的注气速率。液面流速为0.55 ~ 2.20 m/s,气面流速为0.27 ~ 2.20 m/s。在这些实验条件下,总空隙率(包括大小段塞气泡的贡献)从10%到70%不等。空隙率测量结果与原始信号数据、高速视频记录和热膜风速计探头获得的测量结果进行了比对。数据之间的一致性非常好,证实了四传感器探头测量可以进行高度置信。在塞塞流型与段塞流型的过渡区,随着气体流量的增加,后续小气泡的数量和贡献增加。液体流速的增加也产生了类似的效果。随着气速的增加,段塞流的气泡频率也随之增加,而且在较高的气速下,段塞流的长度更长。总界面面积浓度分布包括段塞和后续小气泡的贡献。实验数据表明,段塞流泡下部的界面面积浓度较高,界面曲率较大。这是预料之中的,因为沿着更陡的曲率,局部表面积与体积的比率在增加。段塞流气泡界面浓度的径向分布在段塞流气泡上部几乎呈平坦分布。总界面面积浓度越大,表明小气泡的贡献在增加。实验表明,在塞塞/段塞流状态下,水平通道上部小气泡数量的增加对界面面积浓度的贡献很大。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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