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Flow in porous media I: A theoretical derivation of Darcy's law
Authors:Stephen Whitaker
Affiliation:(1) Department of Chemical Engineering, University of California, 95616 Davis, CA, USA
Abstract:Stokes flow through a rigid porous medium is analyzed in terms of the method of volume averaging. The traditional averaging procedure leads to an equation of motion and a continuity equation expressed in terms of the volume-averaged pressure and velocity. The equation of motion contains integrals involving spatial deviations of the pressure and velocity, the Brinkman correction, and other lower-order terms. The analysis clearly indicates why the Brinkman correction should not be used to accommodate ano slip condition at an interface between a porous medium and a bounding solid surface.The presence of spatial deviations of the pressure and velocity in the volume-averaged equations of motion gives rise to aclosure problem, and representations for the spatial deviations are derived that lead to Darcy's law. The theoretical development is not restricted to either homogeneous or spatially periodic porous media; however, the problem ofabrupt changes in the structure of a porous medium is not considered.Roman Letters Abetasgr interfacial area of the beta-sgr interface contained within the macroscopic system, m2 - Abetae area of entrances and exits for the beta-phase contained within the macroscopic system, m2 - Abetasgr interfacial area of the beta-sgr interface contained within the averaging volume, m2 - Abeta*sgr interfacial area of the beta-sgr interface contained within a unit cell, m2 - Abetae area of entrances and exits for the beta-phase contained within a unit cell, m2 - B second order tensor used to represent the velocity deviation (see Equation (3.30)) - b vector used to represent the pressure deviation (see Equation (3.31)), m–1 - d distance between two points at which the pressure is measured, m - g gravity vector, m/s2 - K Darcy's law permeability tensor, m2 - L characteristic length scale for volume averaged quantities, m - ellbeta characteristic length scale for the beta-phase (see Figure 2), m - ellsgr characteristic length scale for the sgr-phase (see Figure 2), m - nbetasgr unit normal vector pointing from the beta-phase toward the sgr-phase (nbetasgr=–nsgrbeta) - nbetae unit normal vector for the entrances and exits of the beta-phase contained within a unit cell - pbeta pressure in the beta-phase, N/m2 - langpbetarangbeta intrinsic phase average pressure for the beta-phase, N/m2 - 
$$tilde p_beta  $$
pbetalangpbetarangbeta, spatial deviation of the pressure in the beta-phase, N/m2 - r0 radius of the averaging volume and radius of a capillary tube, m - vbeta velocity vector for the beta-phase, m/s - langvbetarang phase average velocity vector for the beta-phase, m/s - langvbetarangbeta intrinsic phase average velocity vector for the beta-phase, m/s - 
$$tilde v_beta  $$
vbetalangvbetarangbeta, spatial deviation of the velocity vector for the beta-phase, m/s - V averaging volume, m3 - Vbeta volume of the beta-phase contained within the averaging volume, m3Greek Letters isinbeta Vbeta/V, volume fraction of the beta-phase - rgrbeta mass density of the beta-phase, kg/m3 - mgrbeta viscosity of the beta-phase, Nt/m2 - psgr arbitrary function used in the representation of the velocity deviation (see Equations (3.11) and (B1)), m/s - xgr arbitrary function used in the representation of the pressure deviation (see Equations (3.12) and (B2)), s–1
Keywords:Volume averaging  Brinkman  correction  closure
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