Experimental study on interfacial area transport in bubbly two-phase flows

被引：143
作者：
Hibiki, T
Ishii, M [1 ]
机构：
[1] Purdue Univ, Sch Nucl Engn, W Lafayette, IN 47907 USA
[2] Kyoto Univ, Inst Res Reactor, Osaka 5900494, Japan
来源：
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER | 1999年 / 42卷 / 16期
关键词：
interfacial area transport; two-fluid model; void fraction; interfacial area concentration; bubble size; turbulence; local measurement; resistivity probe; hotfilm anemometry; gas-liquid flow; pipe flow; bubbly flow; multiphase flow;
D O I：
10.1016/S0017-9310(99)00014-9
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
In relation to the development of the interfacial area transport equation, local measurements of the void fraction, interfacial area concentration, interfacial velocity, and Sauter mean diameter using the double sensor probe method as well as the liquid velocity and turbulence intensity using hotfilm anemometry, were performed extensively for vertical upward bubbly air-water flows in a round tube with an inner diameter of 25.4 mm at three axial locations of L/D=12.0, 65.0 and 125, and fifteen radial locations from r/R=0 to 6.95. The liquid flow rate and the void fraction ranged from 0.292 m/s to 3.49 m/s and from 3% to 27%, respectively. The data set obtained in this study will eventually be used for the development of reliable constitutive relations which reflect the true transfer mechanisms in bubbly flow systems. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码：3019 / 3035
页数：17
相关论文
共 34 条
[1]  
Bertodano M.L.de, 1992, THESIS RENSSELAER PO
[2]  
Clift R, 1978, Bubbles, drops, and particles, DOI 10.1080/07373939308916817
[3]  
GROSSETETE C, 1995, P 2 INT C MULT FLOW, V2
[4]  
HIBIKI T, 1997, PUNE972 PURD U
[5]  
HIBIKI T, 1997, PUNE976 PURD U
[6]  
HIBIKI T, 1997, PUNE975 PURD U
[7]  
HIBIKI T, 1997, IN PRESS NUCL ENG DE
[8]  
HIBIKI T, 1998, P 3 INT C MULT FLOW
[9]  
HILGERT W, 1986, GER CHEM ENG, V9, P180
[10]  
Ishii M., 1975, J NASA STIRECON TE A, V75, P29657
1234