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Turbulent mixing of fluids with different densities flowing through a pipe
Authors:V I Maron
Affiliation:(1) I. M. Gubkin Institute of the Petrochemical and Natural Gas Industry, Moscow
Abstract:A one-dimensional model of a disperse mixture in a turbulent stream is constructed, with the mutual effect of mixture concentration and turbulence intensity taken into account.Notation rgr 0 mean-over-the-section density - p pressure - ngr t turbulent viscosity - U average longitudinal velocity - g acceleration of gravity - ohgr angle of pipe inclination from the horizontal - x, r cylindrical coordinates - t time - V average radial velocity - C average concentration - Dt turbulent diffusivity - c0 mean-over-the-section concentration - K effective turbulent diffusivity - U0 mean flow velocity - X distance, in the moving system of coordinates - a pipe radius - tau 0 frictional stress at the inside surface of the pipe - u* transient turbulent velocity - b turbulence intensity - l linear scale factor - mgr chemical potential of mixture - rgr density of mixture - d1, d2 densities of homogeneous fluids - y+ thickness of laminar layer - y distance from the inside pipe surface - PSgr+ derivative of velocity at the layer boundary on the turbulent side - lambda hydraulic drag - Gr Grashof number - Re Reynolds number - Gamma1, Gamma2, Lambda coefficients in the equation for K* - K* dimensionless effective diffusivity - tau=U0t/2a dimensionless time - xgr=X/2a dimensionless distance Translated from Inzhenerno-Fizicheskii Zhurnal, Vol. 22, No. 6, pp. 992–998, June, 1972.
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