A simplified model of bubble-driven flow in an axisymmetric container
β Scribed by Kunda, W. ;Poots, G.
- Publisher
- Springer
- Year
- 1987
- Tongue
- English
- Weight
- 489 KB
- Volume
- 44
- Category
- Article
- ISSN
- 0003-6994
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β¦ Synopsis
A simplified mathematical model simulating a gas bubble agitation system is here examined for the case when the orifice is located at the centre of the base of a cylindrical vessel. The two phase flow which is confined to a cone region is approximated by the drift flux model. The governing equations for the recirculating liquid flow are quai-lineafized and the flow domain is transformed by a simple transformation into a cylindrical region. Using standard finite difference techniques numerical solutions are obtained for Reynolds numbers in the range 0-104; Re = PUoR0//,tteff, where R 0 is the radius of the vessel, U 0 the velocity of injection of the gas, p the density of the liquid phase & #elf the constant effective turbulent viscosity. For large Re it is shown that the primary recirculating flow is confined to a narrow region adjacent to the two phase/liquid interface.
π SIMILAR VOLUMES
The complex fluid dynamics of two-phase bubbly flows in metallurgical reactors is modelled numerically by using a k-e turbulence model for the liquid phase, with a driving force determined by considering the motion of the bubbles. The latter are affected by the buoyancy forces and the drag caused by
Local miring due to bubbles rising in a liquid medium has been investigated. It is shown that mixing in the bulk fluid is largely influenced by liquid transport in the bubble wake in conformity with experimental observations. A stochastic model has been developed to explain this bubble wake phenomen