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首页> 外文期刊>International Journal of Multiphase Flow >Effects of the liquid viscosity on the phase distributions in horizontal gas-liquid slug flow
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Effects of the liquid viscosity on the phase distributions in horizontal gas-liquid slug flow

机译:液体黏度对水平气液弹团流相分布的影响

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摘要

In the present paper, experimental results of the investigations of the effect of liquid viscosity on the phase distribution in two-phase air-liquid slug flow in horizontal pipes are represented. As the liquid phases, oil with viscosities in the range from 14 to 37 mPas and water are used. The experimental investigations are conducted in a horizontal pipe with an inner diameter of 59 mm. The superficial liquid viscosities and the superficial air velocities in the test section are varied in a range from 0.15 to 1.5 m/s and from 0.1 to 13.5 m/s, respectively. The liquid hold-up within the liquid slug zone, the liquid holdup in the elongated bubble zone and the flow averaged liquid holdup are measured by means of a multibeam r-ray densitometer. The results indicate that there are significant differences in the distribution of liquid and gas when oil and air or water and air are used in the experiments. By increasing the liquid viscosity, increasing values for the flow averaged liquid holdup and the volume averaged liquid holdup inside the liquid slug and the elongated bubble zone are obtained.
机译:本文给出了研究液体粘度对水平管中两相气液弹团流相分布影响的实验结果。作为液相,使用粘度为14至37 mPas的油和水。实验研究是在内径为59 mm的水平管中进行的。测试部分的表观液体粘度和表观空气速度分别在0.15至1.5m / s和0.1至13.5m / s的范围内变化。借助于多束r射线密度计测量液体团块区域内的液体滞留量,细长气泡区域内的液体滞留量和流动平均液体滞留量。结果表明,在实验中使用石油和空气或水和空气时,液体和气体的分布存在显着差异。通过增加液体粘度,获得了在液体块和细长气泡区域内的流动平均液体滞留量和体积平均液体滞留量的增加值。

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