Two-phase flow equations for a dilute dispersion of gas bubbles in liquid

Author:

Biesheuvel A.,Wijngaarden L. Van

Abstract

Equations of motion correct to the first order of the gas concentration by volume are derived for a dispersion of gas bubbles in liquid through systematic averaging of the equations on the microlevel. First, by ensemble averaging, an expression for the average stress tensor is obtained, which is non-isotropic although the local stress tensors in the constituent phases are isotropic (viscosity is neglected). Next, by applying the same technique, the momentum-flux tensor of the entire mixture is obtained. An equation expressing the fact that the average force on a massless bubble is zero leads to a third relation. Complemented with mass-conservation equations for liquid and gas, these equations appear to constitute a completely hyperbolic system, unlike the systems with complex characteristics found previously. The characteristic speeds are calculated and shown to be related to the propagation speeds of acoustic waves and concentration waves.

Publisher

Cambridge University Press (CUP)

Subject

Mechanical Engineering,Mechanics of Materials,Condensed Matter Physics

Reference23 articles.

1. Drew, D. A. & Lahey, R. T. 1979 Application of general constitutive principles to the derivation of multidimensional two-phase flow equations.Intl J. Multiphase Flow 5,243–264.

2. Lauterborn, W. (ed.)1980 Cavitation and Inhomogeneities in Underwater Acoustics .Springer.

3. van Wijngaarden, L. 1976b Hydrodynamic interaction between gas bubbles in liquid.J. Fluid Mech. 77,27–44.

4. Moore, D. W. 1963 The boundary layer on a spherical gas bubble.J. Fluid Mech. 16,161–176.

5. van Wijngaarden, L. 1972 One-dimensional flow of liquids containing small gas bubbles.Ann. Rev. Fluid Mech. 4,369–396.

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