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Flow in porous media II: The governing equations for immiscible,two-phase flow
Authors:Stephen Whitaker
Institution:(1) Department of Chemical Engineering, University of California, 95616 Davis, CA, USA
Abstract:The Stokes flow of two immiscible fluids through a rigid porous medium is analyzed using the method of volume averaging. The volume-averaged momentum equations, in terms of averaged quantities and spatial deviations, are identical in form to that obtained for single phase flow; however, the solution of the closure problem gives rise to additional terms not found in the traditional treatment of two-phase flow. Qualitative arguments suggest that the nontraditional terms may be important whenmgr beta /mgr gamma is of order one, and order of magnitude analysis indicates that they may be significant in terms of the motion of a fluid at very low volume fractions. The theory contains features that could give rise to hysteresis effects, but in the present form it is restricted to static contact line phenomena.Roman Letters (ohgr, eegr = beta, gamma, sgr and ohgr ne eegr) A ohgreegr interfacial area of theohgr-eegr interface contained within the macroscopic system, m2 - A ohgre area of entrances and exits for the ohgr-phase contained within the macroscopic system, m2 - A ohgreegr interfacial area of theohgr-eegr interface contained within the averaging volume, m2 - A ohgreegr * interfacial area of theohgr-eegr interface contained within a unit cell, m2 - A ohgre * area of entrances and exits for theohgr-phase contained within a unit cell, m2 - g gravity vector, m2/s - H mean curvature of thebeta-gamma interface, m–1 - langHrang betagamma area average of the mean curvature, m–1 - 
$$\tilde H$$
HlangHrang betagamma , deviation of the mean curvature, m–1 - I unit tensor - K Darcy's law permeability tensor, m2 - K ohgr permeability tensor for theohgr-phase, m2 - K betagamma viscous drag tensor for thebeta-phase equation of motion - K gammabeta viscous drag tensor for thegamma-phase equation of motion - L characteristic length scale for volume averaged quantities, m - ell ohgr characteristic length scale for theohgr-phase, m - n ohgreegr unit normal vector pointing from theohgr-phase toward theeegr-phase (n ohgreegr = –n eegrohgr ) - p c langp eegrrangeegrlangP betarangbeta, capillary pressure, N/m2 - p ohgr pressure in theohgr-phase, N/m2 - langp ohgrrangohgr intrinsic phase average pressure for theohgr-phase, N/m2 - 
$$\tilde p$$
ohgr p ohgrlangp ohgrrangohgr, spatial deviation of the pressure in theohgr-phase, N/m2 - r 0 radius of the averaging volume, m - t time, s - v ohgr velocity vector for theohgr-phase, m/s - langv ohgr rang phase average velocity vector for theohgr-phase, m/s - langv ohgr rang ohgr intrinsic phase average velocity vector for theohgr-phase, m/s - 
$$\tilde v_\omega  $$
v ohgrlangv ohgrrangohgr, spatial deviation of the velocity vector for theohgr-phase, m/s - V averaging volume, m3 - V ohgr volume of theohgr-phase contained within the averaging volume, m3 Greek Letters isinohgr V ohgr/V, volume fraction of theohgr-phase - rgr ohgr mass density of theohgr-phase, kg/m3 - mgr ohgr viscosity of theohgr-phase, Nt/m2 - sgr surface tension of thebeta-gamma interface, N/m - tauohgr viscous stress tensor for theohgr-phase, N/m2 - mgr/rhov kinematic viscosity, m2/s
Keywords:Volume averaging  interfacial phenomena  closure
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