首页> 外文会议>日本実験力学会講演論文集 (2017年度年次講演会) >環状流路における垂直上昇気液二相流の流動特性
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環状流路における垂直上昇気液二相流の流動特性

机译:垂直上升的气液两相流在环形通道中的流动特性

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摘要

地熱あるいは高温廃熱を回収する方法の一つと して,二重管熱交換器が考えられる.これは內管と 外管の間(環状流路)に水を流し,水が熱交換器外 部の熱を吸収して外部の熱を回収するものである. この時,環状流路内で水蒸気と水の二相流が発生す ることから,二重管熱交換器の設計には,環状流路 内気液二相流の流動特性を理解する必要がある.%Flow characteristics of gas-liquid two-phase flows in annular channel was conducted to obtain detail data for heat exchanger design. The test section was a double-tube, and the two-phase flows flowed upward in the gap between them. Inner diameter of the outer tube was 25mm and outer diameters of the inner tubes were 20mm and 15.4mm. Flow pattern was investigated in both flow channels, and it was compared with the flow pattern in circular tubes. The effects of the annular channel on the flow pattern were remarkable in bubbly and annular flows. Liquid lump velocity was also measured, and the velocity of liquid slugs in the annular channel was found to be higher than that in the circular channel. The velocity of a single gas-slug was measured and it was clarified that voia fraction of gas slug in the annular channel was smaller than that in the circular channel, so that it caused the velocity difference between those channels.
机译:双管式换热器可以认为是回收地热或高温废热的方法之一,其中水在内管和外管之间流动(环形流动路径),水流到热交换器的外部。它吸收零件的热量并从外部回收热量,这时,由于在环形流路中产生水蒸气和水的两相流,因此双管热交换器的设计是进行了环形通道中气液两相流的%流量特性研究,以获取热交换器设计的详细数据。两相流在它们之间的间隙中向上流动,外管的内径为25mm,内管的外径分别为20mm和15.4mm。在圆管和环形流中,环形通道对流型的影响是显着的,并且还测量了液体团块速度,发现环形通道中的液体团块的速度高于环形通道。测量了单个气体团块的速度,并澄清了环形通道中气体团块的体积分数较小。 r大于圆形通道中的r,因此它引起了那些通道之间的速度差异。

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