Liquid Taylor Bubbles Rising in a Vertical Column of a Heavier Liquid: An Approximate Analysis

被引:8
|
作者
Mandal, T. K. [1 ]
Das, G. [2 ]
Das, P. K. [3 ]
机构
[1] Natl Inst Technol, Dept Chem Engn, Durgapur 713209, WB, India
[2] Indian Inst Technol, Dept Chem Engn, Kharagpur 721302, W Bengal, India
[3] Indian Inst Technol, Dept Mech Engn, Kharagpur 721302, W Bengal, India
关键词
bubbles; density; flow visualisation; viscosity; LARGE GAS BUBBLE; LONG BUBBLES; SURFACE-TENSION; RISE VELOCITY; FLOW PATTERNS; MOTION; TUBES; SHAPE; ENTRAINMENT; INCLINATION;
D O I
10.1115/1.3026730
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
It has been noted that a volume of lighter liquid when injected into a stationary column of a heavier liquid, it rises up as a simple elongated Taylor bubble. In the present study, experimental and theoretical analyses have been performed to understand the rise of liquid Taylor bubbles. The experiments have been performed with different liquid pairs with their viscosities ranging from 0.71 mPa s to 1.75 mPa s and conduit sizes ranging from 0.012 m to 0.0461 m. The bubble shape has been predicted using a potential flow analysis and validated from photographic measurements. This analysis has been further modified to predict the rise velocity. The modified analysis accounts for the density difference between the two liquids, viscosity effects of the primary liquid, and interfacial tension of two fluids. A semi-empirical equation has been developed, which gives satisfactory results for most of the cases.
引用
收藏
页码:0113031 / 0113037
页数:7
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