典型的空气流动模式,空气和水+甘油(G20)的空气混合物,以及水合物+丁醇+的460%的空气在一个微型水平管道中混合

F. Jayadi, Sudarja Sudarja, Eli Komolosari
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摘要

本研究旨在获得水-空气流动、甘油+水(G20)-空气混合物和Aquadest+丁醇4%-空气混合物的流动特性信息。微型管道中的两相流动特性与常规管道中的两相流动特性存在显著差异,因此会影响传热过程等涉及两相流的流体分布过程。因此,有必要对小尺寸管道内的两相流进行进一步的研究。本研究在水平位置采用直径为1.6 mm的玻璃管形式的试验段中进行。所用的液体为水,表面张力(σ)为71 mN/m,甘油+水(G20)的混合物表面张力(σ)为62.5 mN/m,蒸馏水+ 4%丁醇的混合物表面张力(σ)为36.50 mN/m。气体表面速度(JG)= 0.033-4.935 m/s,液体表面速度(JL)= 0.025-66.3 m/s。结果表明,在小通道内没有常规管道中存在的分层流动现象。检测到的流型有:气泡流、段塞流、段塞环空流、搅拌流和环空流。与Triplett et al . (1999a)、Chung and Kawaji(2004)、Sudarja et al .(2014)、Aqli et al .(2015)的流型图比较,流型图的结果表明,粘度越高,环形搅拌段塞流过渡线越高。当环空段塞环空过渡线趋于倾斜时减小。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Karakteristik Pola Aliran Air-Udara, Campuran Air+Gliserin (G20)-Udara, dan Campuran Akuades+Butanol 4%-Udara Pada Pipa Horizontal Berukuran Mini
This study aims to obtain information about the flow characteristics of Water-Air Flow, Mixture of Glycerin+Water(G20)-Air, and Mixture of Aquadest+Butanol 4%-Air. The two-phase flow characteristics in mini-sized pipes have significant differences with the two-phase flow characteristics in conventional pipes, so it will affect fluid distribution processes involving two-phase flow such as heat transfer processes. Therefore, it is necessary to conduct further studies on the two-phase flow pattern in mini-sized pipes. This research was conducted in a test section in the form of a glass pipe with a diameter of 1.6 mm in a horizontal position. The liquid fluid used is water which has a surface tension (σ) of 71 mN/m, a mixture of glycerin+water (G20) has a surface tension (σ) of 62.5 mN/m, and a mixture of distilled water+butanol 4% has a surface tension (σ) of 36.50 mN/m. Superficial velocity of gas (JG)=0.033–4.935 m/s, and superficial velocity of liquid (JL)=0.025–66.3 m/s. The results showed that stratified flow was not observed in the mini channel as can be found in conventional pipes. The detected flow patterns are: bubbly, slug, slug-annular, churn, and annular. The results of flow pattern maps compared with flow pattern maps from Triplett et al (1999a), Chung and Kawaji (2004) and Sudarja et al (2014), and Aqli et al (2015) show that the higher the viscosity, the higher the annular churn-slug flow transition line will be. decreases while the annular – slug annular transition line tends to be more sloping. 
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