Abstract
We develop an approach to coupling between viscous flows of the two phases in porous media, based on the Maxwell–Stefan formalism. Two versions of the formalism are presented: the general form, and the form based on the interaction of the flowing phases with the interface between them. The last approach is supported by the description of the flow on the mesoscopic level, as coupled boundary problems for the Brinkmann or Stokes equations. It becomes possible, in some simplifying geometric assumptions, to derive exact expressions for the phenomenological coefficients in the Maxwell–Stefan transport equations. Sample computations show, among other, that apparent relative permeabilities are dependent on the viscosity ratio; that the overall mobility of the phases decreases compared to the standard Buckley–Leverett formalism; and that the effect is determined by the parameter determining the “degree of mixing” between the flowing phases. Comparison to the available experimental data on the steady-state two-phase relative permeabilities is presented.
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Abbreviations
- \(A\) :
-
Cross-sectional area
- \(\mathbf{D}\) :
-
Vector of pressure gradients
- \(I\!_P \) :
-
Fraction of the active jets
- \(F\) :
-
Fractional flow function
- \(G\) :
-
Force
- \(k\) :
-
Permeability
- \(K\) :
-
Mesoscopic permeability
- \(l\) :
-
Proportionality coefficients
- \(L\) :
-
Length
- \(M\) :
-
Dimensionless mobility
- \(P\) :
-
Pressure
- \(r\) :
-
Distance to the jet center
- \(r\!_j\) :
-
Inner radius in the jet model
- \(R\) :
-
Outer radius in the jet model
- \(s\) :
-
Saturation
- \(u\) :
-
Interstitial velocity
- \(U\) :
-
Superficial velocity
- \(V\) :
-
Velocity of the moving interface
- \(W\) :
-
Mesoscopic velocity
- \(x\) :
-
Coordinate in the flow direction
- \(y,z\) :
-
Coordinates orthogonal to the flow direction
- \(W\) :
-
Mesoscopic flow velocity
- \(Z\) :
-
Operator in the equation governing the mesoscopic flow velocity
- \(\alpha \) :
-
Friction coefficient
- \(\beta \) :
-
Multiplier transforming superficial to interstitial velocity
- \(\gamma \) :
-
Ratio of the effective Brinkman to the real phase viscosity
- \(\Gamma \) :
-
Boundary of a region
- \(\phi \) :
-
Porosity
- \(\kappa \) :
-
Inverse matrix of resistance coefficients
- \(\lambda \) :
-
Onsager phenomenological coefficient
- \(\Lambda \) :
-
Matrix of phenomenological Onsager coefficients
- \(\mu \) :
-
Viscosity or viscosity ratio
- \(\tau \) :
-
Tortuosity
- \(\xi \) :
-
Ratio of the characteristic jet size to the characteristic pore scale of the porous medium
- \(\omega \) :
-
Auxiliary function in the expression for mesoscopic velocity
- \(d\) :
-
Driving (pressure force)
- \(e\) :
-
Effective (viscosity in the Brinkman equation)
- \(j\) :
-
Jet
- \(o\) :
-
“Orange”
- \(r\) :
-
Relative
- \(s\) :
-
Solid (porous medium matrix)
- \(P\) :
-
Pressure
- \(V\) :
-
Interface
- \(wi,\;or\) :
-
Irreducible or residual
- \(w\) :
-
“White”
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Acknowledgments
This work has been carried out in the framework of the ADORE project sponsored by the Danish Council for Technology and Production (FTP). Application of the Maxwell–Stefan approach was inspired by long discussions with Professor Johannes Wesselingh. Professor Pavel Bedrikovetsky (University of Adelaide, Australia) is kindly acknowledged for multiple discussions and useful advices.
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Appendix: Solution of the Brinkmann Problems for the Jet Model
Appendix: Solution of the Brinkmann Problems for the Jet Model
The solutions for the jet model should be obtained for four different cases (cf. Eqs. 29, 30). There are solutions for the outer and for the inner jet. The solutions should be obtained for \(s<s^{*}\) and for \(s>s^{*}\). If \(s<s^{*}\), the outer jet is orange, and the inner jet is white. For the case of \(s>s^{*}\), the colors exchange.
We will consider in detail the solution for the outer jet problem and for \(s<s^{*}\), so that the phase is orange. Other solutions will be briefly described.
The governing Brinkmann equation is
With the boundary conditions at the inner and outer boundaries of the jet,
These boundary conditions correspond to the case where all the inner jets are active (\(I_P =0)\). For the case where some jets are passive, the first boundary condition should be substituted by \(W_o (r_j )=0\) for fraction \(I_P \) of the jets. This is a particular case of the first condition (37), with \(V=0\).
Let us first consider the case with no passive inner jets, \(I_P =0\). The effect of passive jets will be added later.
By substitutions
the equation considered is reduced to the zero-order modified Bessel equation as:
Solving it and making back-substitution, we express \(W_0 \) in the general form of
Here, \({I}_0 ,\;{K}_0 \) are modified Bessel functions of the first and second kind, \(C_i \) are the constants to be determined from the boundary conditions (37). Substitution of the values \(r_j ,\;R\) into the solution and resolving with regard to these constants results in
The first-order Bessel functions arise from the differentiation of the zero-order functions, as required by the second boundary condition (37).
The average velocity \(U_o \) is found as (cf. Eq. 21):
Substitution of the solution \(W_0 \) and rather elaborate, but straightforward integration with application of the tabulated integrals of the type of \(\int {xI_0 (x)dx,\;\int {xK_0 (x)dx} } \) results in
This expression is equivalent to the first expression (29), with account of Eq. (26). It may be shown by manipulation with the Bessel functions that
Thus, the expression for coefficient \(L_{oV} \) has the form of
Equation (38) has the form similar to Eq. (25). Comparison shows that for the case of no passive jets, \(L_{oV} =l_{oV} \). This proves the first of Eq. (29).
We have considered the case where all the inner jets are active \((I_P =0)\). If, on the contrary, all the inner jets would be passive \((I_P =1)\), the solution would be given by Eq. (38) with \(V=0\). The complete solution is the linear combination of the solutions with active and with passive inner jets
Comparison with Eq. (25) results in
The first equation provides the connection between the meso- and macroscale permeabilities for oil. It is not used for computations in the present work, but may be important for experimental studies. The second equation is the result mentioned at the end of Sect. 4.2.
The flow in the active inner part of the jet at \(s<s^{*}\) is described by the Brinkmann Eq. (27) with boundary conditions (28). Averaging is performed as above. The passive jets form the fraction of the volume where the flow velocity is zero. The resulting expression for the flow velocity is
where \(L_{wV} \) is given by the formula equivalent to the second Eq. (29)
Comparison with Eq. (25) recovers equations
The case of \(s>s^{*}\) is considered in a similar way.
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Shapiro, A.A. Two-Phase Immiscible Flows in Porous Media: The Mesocopic Maxwell–Stefan Approach. Transp Porous Med 107, 335–363 (2015). https://doi.org/10.1007/s11242-014-0442-0
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DOI: https://doi.org/10.1007/s11242-014-0442-0