Hostname: page-component-76fb5796d-dfsvx Total loading time: 0 Render date: 2024-04-28T14:03:59.559Z Has data issue: false hasContentIssue false

Turbulent fountains in an open chamber

Published online by Cambridge University Press:  26 April 2006

W. D. Baines
Affiliation:
Department of Mechanical Engineering, University of Toronto, Ontario. M5S 1A4, Canada
J. S. Turner
Affiliation:
Research School of Earth Sciences, The Australian National University. GPO Box 4, Canberra, ACT 2601, Australia
I. H. Campbell
Affiliation:
Research School of Earth Sciences, The Australian National University. GPO Box 4, Canberra, ACT 2601, Australia

Abstract

The flow and density distribution produced by injecting dense fluid upwards at the bottom of a homogeneous fluid have been investigated experimentally and theoretically. Both axisymmetric and line sources have been studied using small-scale laboratory experiments in which salt water is injected into a tank of fresh water. The turbulent fountain formed in this way rises to a maximum height which can be related to the Froude number of the inflow, and then falls back and spreads out along the floor. Continuing the inflow builds up a stable stratification in a similar manner to that discussed earlier for the ‘plume filling box model’ of Baines & Turner (1969) which is complementary to the present work. The fountain flows considered here have the important new feature that the volume of the inflow is significant, so the total volume of fluid in the ‘open’ container increases with time. The evolution is determined by the rate of entrainment into the fountain from its surroundings, which is found directly by experiment. Re-entrainment of fluid into the fountain continually changes the density profile in the mixed fluid collecting at the bottom of the chamber below the level of the fountain top, and controls the rate of rise of a ‘front’ of marked fluid. The top of the fountain rises linearly in time, at a rate which, for axisymmetric fountains, has been shown both experimentally and theoretically to be close to half the rate of rise of the free surface due to the inflow. Thus at a certain time the front rises above the top of the fountain. Once the mixed fluid at the bottom of the chamber has risen above the fountain its density profile remains unchanged. The front velocity, the fountain height and the density profile have all been obtained as functions of time using a theory which is in good agreement with the experimental results for a large range of input Froude numbers. For line fountains the results are less precise owing to an instability which causes the flow to switch irregularly from a symmetrical state to one in which the downflow occurs on one side only, and with a smaller maximum height. In concluding we discuss the applications which motivated the work, particularly the development of a stratified hybrid layer in magma chambers replenished from below, and the dynamically identical, but inverted problem of heating large buildings through ducts located near the roof.

Type
Research Article
Copyright
© 1990 Cambridge University Press

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)

References

Albertson, M. L., Dai, Y.-B., Jensen, R. A. & Rouse, H., 1950 Diffusion of submerged jets. Trans. ASCE 115, 639697.Google Scholar
Baines, W. D.: 1975 Entrainment by a plume or jet at a density interface. J. Fluid Mech. 68, 309320.Google Scholar
Baines, W. D.: 1983 A technique for the direct measurement of volume flux in a plume. J. Fluid Mech. 132, 247256.Google Scholar
Baines, W. D. & Murphy, T. M., 1986 The temperature distribution in an enclosure produced by a forced plume. In Proc. 8th Intl Heat Transfer Conf., pp. 15071512. Hemisphere.
Baines, W. D. & Reedman, T. J., 1990 The negative buoyant jet in a closed container. J. Hyd. Engng, ASCE (submitted).Google Scholar
Baines, W. D. & Turner, J. S., 1969 Turbulent buoyant convection from a source in a confined region. J. Fluid Mech. 37, 5180.Google Scholar
Batchelor, G. K.: 1954 Heat convection and buoyancy effects in fluids. Q. J. R. Met. Soc. 80, 339358.Google Scholar
Campbell, I. H. & Turner, J. S., 1985 Turbulent mixing between fluids with different viscosities. Nature 313, 3942.Google Scholar
Campbell, I. H. & Turner, J. S., 1989 Fountains in magma chambers. J. Petrol 30, 885923.Google Scholar
Crapper, P. F.: 1977 A note on the characteristics of a two-dimensional jet produced by a series of co-planar three-dimensional jets. J. Indust. Aero. 2, 181183.Google Scholar
Goldman, D. & Jaluria, Y., 1986 Effect of opposing buoyancy on the flow in free and wall jets. J. Fluid Mech. 166, 4156.Google Scholar
Kotsovinos, N. E. & List, E. J., 1977 Plane turbulent buoyant jets. Part 1. Integral properties. J. Fluid Mech. 81, 2544.Google Scholar
Kumagai, M.: 1984 Turbulent buoyant convection from a source in a confined two-layered region. J. Fluid Mech. 147, 105131.Google Scholar
Morton, B. R.: 1959 Forced plumes. J. Fluid Mech. 5, 151163.Google Scholar
Morton, B. R., Taylor, G. I. & Turner, J. S., 1956 Turbulent gravitational convection from maintained and instantaneous sources. Proc. R. Soc. Lond. A 234, 123.Google Scholar
Seban, R. A., Behnia, M. M. & Abreau, K. E., 1978 Temperatures in a heated jet discharged downward. Intl J. Heat Mass Transfer 21, 14531458.Google Scholar
Turner, J. S.: 1966 Jets and plumes with negative or reversing buoyancy. J. Fluid Mech. 26, 779792.Google Scholar
Turner, J. S.: 1973 Buoyancy Effects in Fluids. Cambridge University Press, 367 pp.
Turner, J. S.: 1986 Turbulent entrainment: the development of the entrainment assumption and its application to geophysical flows. J. Fluid Mech. 173, 431471.Google Scholar