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首页> 外文期刊>International Journal of Heat and Mass Transfer >Experimental study on the hydrodynamic behavior of gas-liquid air-water two-phase flow near the transition to slug flow in horizontal pipes
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Experimental study on the hydrodynamic behavior of gas-liquid air-water two-phase flow near the transition to slug flow in horizontal pipes

机译:水平管过渡到团状流附近气液气-水两相流水动力行为的实验研究

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摘要

The knowledge of the slug flow is essential the design safety of hydrocarbon transportation in the pipeline system of petroleum industries. However, the suitable models to predict the transition condition to slug flow are limited due to insufficient availability of experimental data. In the present study, the hydrodynamic characteristics of the near the transition to slug flow of air-water two-phase flow in horizontal pipes were investigated experimentally for inner pipe diameters of 16 mm, 26 mm, and 50 mm. The superficial velocities of water and air ranged from JL = 0.03 to 0.30 m/s and JG = 0.7 to 10.0 m/s. The hydrodynamic behavior was obtained from the combination of the visualization detected by using a high-speed video camera, the pressure gradient, and instantaneousvolumetric liquid fractionmeasurements.The experimental results indicate that the wave growth and the wave coalescence are involved in the mechanism of the slug flow formation. Both gas and liquid superficial velocities have a significant effect also of those mechanisms. The averagevolumetric liquid fractionnear the transition to slug flow is not affected by superficial gas velocities. Next, under a constant superficial gas velocity, an increase in the inner pipe diameter requires a larger superficial liquid velocity to change the flow patterns from stratified smooth to slug flow, and from pseudo-slug to slug flow.
机译:团塞流的知识对于石油工业管道系统中烃类运输的设计安全至关重要。但是,由于实验数据的可用性不足,用于预测向团状流过渡条件的合适模型受到限制。在本研究中,通过实验研究了内径分别为16 mm,26 mm和50 mm的空气-水两相流在水平管中过渡到团状流附近的水动力特性。水和空气的表面速度范围从JL = 0.03至0.30 m / s和JG = 0.7至10.0 m / s。通过高速摄像机的可视化,压力梯度和瞬时体积液体分数的测量相结合,获得了流体动力学行为。实验结果表明,水流的增长和水流的聚结参与了的形成机理。流形成。气体和液体的表面速度都对这些机理也有重要影响。向团状流过渡附近的平均体积液体分数不受表观气体速度的影响。接下来,在恒定的表观气体速度下,内管直径的增加需要较大的表观液体速度,以将流型从分层的平滑流转换为弹状流,并从假弹状流转换为弹状流。

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