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Two-phase frictional pressure drop measurements in U-type wavy tubes subject to horizontal and vertical arrangements

机译:水平和垂直排列的U型波浪管中的两相摩擦压降测量

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Two-phase frictional pressure gradient is significantly affected by the flow patterns. Though most of the U-type wavy tubes are commonly vertically installed in the air-conditioning and refrigerating systems, yet none investigations had reported the two-phase frictional pressure loss in vertical U-type wavy tubes. This study presents the measurements of R- 134a two-phase frictional pressure gradient subject to vertical and horizontal arrangements of a U-type wavy tube with inner diameter of 5.07 mm and a curvature ratio of 5. The ratio between two-phase pressure gradients of U-bend and straight tube is about 2.5-3.5. For the straight tube, the frictional two-phase pressure gradient ratio between the vertical and horizontal arrangements is marginally higher (1.0-1.2) for annular flow pattern at x > 0.5, and is 1.0-1.4 for the U-bend in the wavy tube. The higher resistance in the vertical arrangement is due to the buoyancy force against the flow inertia. However, for x < 0.5, this ratio is gradually increased due to the difference of flow pattern. The ratio is increased to 1.8 in the straight tube. For the U-bend, the ratio is 2.1 for flow entering the upper tube and is 1.5 for flow entering the lower tube at x = 0.1 and G = 200 kg/m{sup}2 s. For the vertical wavy tube, additional effects like the flow pattern transition, liquid flow reversal, and freezing slug may cause additional pressure drops.
机译:两相摩擦压力梯度受流型的影响很大。尽管大多数U型波浪管通常垂直安装在空调和制冷系统中,但是没有研究报告垂直U型波浪管的两相摩擦压力损失。这项研究提出了在垂直和水平排列的U型波浪管(内径为5.07 mm,曲率比为5)的情况下,R- 134a两相摩擦压力梯度的测量结果。 U型弯和直管约为2.5-3.5。对于直管,在x> 0.5的情况下,垂直和水平布置之间的摩擦两相压力梯度比对于环形流型略高(1.0-1.2),对于波浪形管中的U型弯则为1.0-1.4 。垂直布置中的较高阻力归因于针对流动惯性的浮力。但是,对于x <0.5,由于流型的不同,该比率逐渐增加。直管中的比率增加到1.8。对于U型弯,在x = 0.1和G = 200 kg / m {sup} 2 s时,进入上管的流量的比率为2.1,进入下管的流量的比率为1.5。对于垂直波浪管,流型转换,液体流逆转和结冰等附加影响可能会导致附加压降。

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