Mass transfer from a bubble in a vertical pipe

被引:61
作者
Hosoda, Shogo [1 ]
Abe, Satoru [1 ]
Hosokawa, Shigeo [1 ]
Tomiyama, Akio [1 ]
机构
[1] Kobe Univ, Grad Sch Engn, Kobe, Hyogo 6578501, Japan
关键词
Bubble; Mass transfer; Carbon dioxide; Dissolution; COEFFICIENTS; LIQUID;
D O I
10.1016/j.ijheatmasstransfer.2013.10.031
中图分类号
O414.1 [热力学];
学科分类号
摘要
Mass transfer from single carbon dioxide bubbles in vertical pipes is measured using a stereoscopic image processing method to develop a mass transfer correlation applicable to a wide range of bubble diameters in standard pipe sizes. The diameters of pipes used are 12.5, 18.2, and 25.0 mm and the bubble diameter ranges from 5 to 26 mm. The ratio, lambda, of the bubble diameter to the pipe diameter is varied from 0.2 to 1.8, which covers various bubble shapes such as spheroidal, wobbling, cap, and Taylor bubbles. Measured Sherwood numbers, Sh, strongly depend on bubble shape, i.e., Sh of Taylor bubbles differs from that of spheroidal and wobbling bubbles. The Sherwood numbers are correlated in terms of the Peclet number Pe and lambda. The applicability of the proposed correlation to long-term bubble dissolution process is examined through comparisons between measured and predicted dissolution processes. The predictions are carried out by solving mass conservation equations not only for carbon dioxide but also for nitrogen and oxygen. Good agreements are obtained in the dissolution processes for various bubble sizes and the three pipe diameters. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:215 / 222
页数:8
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