Experiments and a model of turbulent exchange flow in a vertical pipe

被引:26
作者
Cholemari, MR [1 ]
Arakeri, JH [1 ]
机构
[1] Indian Inst Sci, Dept Mech Engn, Bangalore 560012, Karnataka, India
关键词
turbulent mixing; exchange flow; mixing length model;
D O I
10.1016/j.ijheatmasstransfer.2005.04.025
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this paper we present experimental measurements of buoyancy driven turbulent exchange flow in a vertical pipe (L/d ratios of 9-12). The flow is driven by an unstable density difference across the ends of the pipe, created using brine and distilled water. Away from either end, a fully developed region of turbulence exists with a linear density gradient. Using a mixing length model that accounts for the end effects, we obtain the turbulent scales and flux. The Nusselt number scales like the square root of the Rayleigh number (Nu similar to Ra-1/2). We give an empirical relation to quantify the end effects and hence calculate the flux of the salt (NaCl) given the aspect ratio of the pipe and the overall density difference across it. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4467 / 4473
页数:7
相关论文
共 10 条
[1]  
Arakeri JH, 2000, CURR SCI INDIA, V79, P859
[2]  
ARAKERI JH, 2002, P 9 AS C FLUID MECH
[3]  
Brown W.G., 1962, INT J HEAT MASS TRAN, V5, P869
[4]  
CHOLEMARI MR, 2004, THESIS INDIAN I SCI
[5]   BUOYANCY-DRIVEN EXCHANGE FLOW THROUGH SMALL OPENINGS IN HORIZONTAL PARTITIONS [J].
EPSTEIN, M .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1988, 110 (4A) :885-893
[6]  
GARDNER GC, 1977, INT J MULTIPHASE FLO, V3, P305
[7]  
Globe S., 1959, J Heat Transf, V81, P24
[8]   TURBULENT THERMAL CONVECTION AT ARBITRARY PRANDTL NUMBER [J].
KRAICHNAN, RH .
PHYSICS OF FLUIDS, 1962, 5 (11) :1374-1389
[9]   Turbulent convection at very high Rayleigh numbers [J].
Niemela, JJ ;
Skrbek, L ;
Sreenivasan, KR ;
Donnelly, RJ .
NATURE, 2000, 404 (6780) :837-840
[10]   Mass flow through a horizontal vent in an enclosure due to pressure and density differences [J].
Tan, Q ;
Jaluria, Y .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2001, 44 (08) :1543-1553