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3 Definition of the Model

[681.1.8.1] In this section, a brief summary of the mathematical model is given. [681.1.8.2] The following equations are based on volume, mass and momentum balance equations analogous to the foundations of the traditional theory (see e.g. [9] for a succinct but detailed parallel development). [681.1.8.3] It is assumed that both fluids are incompressible and immiscible and that the lateral dimensions of the column are small with respect to the capillary fringe. [681.1.8.4] Hence, a one dimensional description is an appropriate approximation. [681.1.8.5] The mass balances for the four fluid phases (percolating water is identified by the index 1, non-percolating water by 2, percolating oil by 3 and non-percolating oil by 4) read as

ϱWϕS1t+ϱWq1x=M1,(1a)
ϱWϕS2t+ϱWq2x=M2=-M1,(1b)
ϱOϕS3t+ϱOq3x=M3,(1c)
ϱOϕS4t+ϱOq4x=M4=-M3,(1d)

where t denotes time, x denotes position or height along the column, ϕ denotes porosity, ϱW,ϱO denote the density of water, respectively air, Si the saturation, qi the volume flux and Mi the mass exchange term of the phase i. [681.1.8.6] The mass exchange term accounts for the fact that percolating and non-percolating phases of the same fluid exchange mass by break-up and coalescence. [681.1.8.7] The mass exchange terms take the form

M1=η2ϕϱWS2-S2*SW*-SWSWt,(2a)
M3=η4ϕϱOS4-S4*SW*-SWSWt.(2b)

with the parameter functions

SW*=1-minSOim,1-ϵMSOΘtSW+minSWdr,1-ϵMSW1-ΘtSW,(3a)
S2*=minSWdr,1-ϵMSW1-ΘtSW,(3b)
S4*=minSOim,1-ϵMSO1-ΘtSO,(3c)

where the parameter SOim is a limiting saturation for the non-percolating air, SWdr a limiting saturation for non-percolating water and Θ() denotes the Heaviside step function. [681.1.8.8] Water saturation is given by SW=S1+S2 and the air saturation by SO=S3+S4. [681.1.8.9] The parameter ϵM0 is a mathematical regularization parameter. [681.1.8.10] It allows to simulate also primary processes. [681.1.8.11] The volume fluxes of the phases take the form

q1q2q3q4=Λ-xP1-ϱWg-xP3-γP2*S2γ-1-ϱWg+PaxS1-α-xP3-ϱOg-xP1-δP4*S4δ-1-ϱOg+PbxS3-β,(4)

where P1,P3 denote the averaged pressures of the percolating phases, g the gravity acceleration, α, β, γ, δ, Pa, Pb, P2*, P4*, are constitutive parameters. [681.1.8.12] The parameters α,β,Pa,Pb are associated with capillary potentials and γ,δ,P2*,P4* with the energy stored in the interface between the non-percolating phases and the surrounding percolating phases of the other fluid [9]. [681.1.8.13] A generalized mobility matrix is denoted by Λ with the coefficients

Λij=ϕ2SiSjR~-1ij,(5)

where R~-1ij denote the components of the inverse of the viscous coupling parameter matrix. [681.1.8.14] A comparison with the classical two-phase Darcy equations yields that R~11μW/k and R~33μO/k, where k denotes the permeability of the porous medium. [681.1.8.15] The system of equations is closed with the volume conservation for incompressible fluids and incompressible porous media

S1+S2+S3+S4=1(6)

plus a special form of the general self-consistent closure condition [11, 5]

P3=P1+12PaS1-α-PbS3-β+γP2*S2γ-1-δP4*S4δ-1(7)

for the pressures of the percolating phases.