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Air-Water Two-Phase Pressure Drop in U-Type Wavy Tubes

机译:U型波浪管中的空气-水两相压降

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Two-phase frictional performance of air-water mixture flow in six horizontal U-type wavy tubes is presented. The inner diameters of the wavy tubes are 5.07 and 8.29 mm, whereas the curvature ratios span from 3.94 to ~7.87. The two-phase superficial velocities for air and water are in the range of U_(L,S) = 0.02-0.7 m/s and V_(G,S) = 0.15-60 m/s. The measured pressure loss in bend included the loss in U bends and the loss caused by the distorted flow in the downstream straight tube. This leads to the definition of the equivalent frictional two-phase pressure gradient in the U bend. The ratio between the two-phase pressure gradient in the U-bend and the two-phase pressure gradient in the upstream straight tube is found in the range of 1.5-3 for most of the data. The ratios increase with gas quality due to consecutive accelerating/deaccelerating phenomenon caused by the wavy tube. The frictional two-phase multiplier in the U bend can be correlated by the use of the Chisholm correlation. By introduction of the Martinelli parameter and the liquid Froude number to the Chisholm correlation, a new correlation is proposed that can describe the present φ_(B,L)~2 data with a mean deviation of 13.9%.
机译:给出了六个水平U型波浪管中空气-水混合物流的两相摩擦性能。波浪管的内径为5.07和8.29 mm,曲率比为3.94至〜7.87。空气和水的两相表面速度在U_(L,S)= 0.02-0.7 m / s和V_(G,S)= 0.15-60 m / s的范围内。测得的弯头压力损失包括U形弯头的损失和下游直管中流量畸变引起的损失。这导致了U形弯曲中等效摩擦两相压力梯度的定义。对于大多数数据,U型弯管中的两相压力梯度与上游直管中的两相压力梯度之间的比率在1.5-3的范围内。由于波状管引起的连续的加速/减速现象,比率随气体质量而增加。 U弯中的摩擦两相乘数可以通过Chisholm相关性进行关联。通过将马丁内利参数和液态弗洛德数引入奇斯霍尔姆相关性,提出了一种新的相关性,可以描述当前的φ_(B,L)〜2数据,平均偏差为13.9%。

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