1. Introduction
In this paper, we are interested in the study of a system modeling two-phase flow, immiscible and incompressible, wetting and non-wetting fluids, with dynamic capillary pressure. Firstly, we describe a nonlinear problem modeling the displacement of two incompressible and immiscible fluids in a porous media.
The functional capillary pressure models that define the 
 relation are determined by well-defined laboratory experiments using samples of the porous medium, see [
1,
2,
3]. In these experiments, 
 is calculated by measuring the difference between the average pressures of non-wetting 
 and wetting 
 liquids. By expressing this difference as a function of saturation of the wetting phase 
,
      
      these models define the capillary pressure under equilibrium conditions 
. However, fluids do not necessarily flow under equilibrium conditions, especially for short durations when the variation of 
 with respect to time is fast, which implies that the derivative of the saturation in time 
 can be large. Under these circumstances, the relationship 
 strongly depends on the two quantities 
 and 
. The goal of this work, considering the dynamic capillary pressure is a function of variables 
 and 
,
      
      where the function 
 is increasing and stands for classical static capillary pressure, and we define the damping coefficient 
 as a function of variable 
. In this work, we generalize the problem for 
 as a function of 
s, where we previously observed that the problem for the damping coefficient 
 is a positive real constant, see [
4]. Next, we mathematically analyze the existence of weak solutions in the model.
In this dimension, to better adapt to the conditions of equilibrium (interface), it is necessary to develop equilibrium laws at the macroscopic level, and the appropriate constitutive relations for the correct calculation of the interfacial equilibrium, as well as the properties of the phases, flow in the porous medium.
Accordingly, a thermodynamic theory for two-phase flow in a porous medium has been worked out in detail. The main constitutive assumption in this theory is the dependence of Helmholtz free energy functions for phases and interfaces on state variables, such as the density, mass, temperature, saturation, porosity, interfacial surface density, and solid-phase stress tensor. Certainly, the explicit inclusion of “interface effects” and “surface properties” at the two-phase flow level is an essential feature of this new approach. It is well recognized in the literature [
5,
6] that interfaces play an important role in determining the thermodynamic state of the whole system. In this way, in the case of two-phase flow in a porous medium, the three phases and three interfaces are also involved in the context of this new theory. The need for studies on the dynamic effects of the 
 relationship has been demonstrated through several experimental studies. The articles [
7,
8] present a review of this experimental work. Water and air are combined into one system in most previous studies and research. In summary, it can be seen that for a given saturation, a transient drainage process (
) exhibits higher capillary pressure than under equilibrium conditions, and a transient imbibition process (
) exhibits lower capillary pressure. In [
9], a review of some experimental studies and also of existing approaches in the literature for models that seek to give dynamic effects a theoretical basis is presented.
We insist on the model of Hassanizadeh and Gray [
10]. Likewise, Kalaydjian [
11] provides a good and concise description that combines fluids and interfaces, and this leads to the classical or microscopic extension of capillary pressure. The same can be said for Stover, for example [
12], who gave a different expression for dynamic capillary pressure, somewhat similar to what Hassan Zabdeh, Gray, and Klaydjian proposed in their work. In the same context, this model is the first to reflect dynamic capillary pressure in a quantitative manner, as it is based solely on experimental results. On the other hand, the Barenblatt model [
13] is cited, which looks at another form of modeling dynamic effects on capillary pressure, which simultaneously concerns relative dynamic permeability. As part of the experimental studies, in [
14], two liquids of the same viscosity were used, unlike the most commonly used water–air system, to study the pressure dependence of the interface discontinuity of an imbibition process.
A similar work by Kalaydjian [
11] will be briefly described since his model constitutes the interfaces between fluids. Both approaches lead to an extension of classical (macroscopic) capillary pressure by a non-equilibrium term consisting of the rate of change in saturation. Stauffer [
15] found another expression for dynamic capillary pressure similar to those of Hassanizadeh, Gray, and Kalaydjian. This model, based solely on experimental results, was the first model to attempt to produce dynamic capillary pressure quantitatively. Finally, the Barenblatt model [
13] is cited, which looks at another form of modeling dynamic effects on capillary pressure, which simultaneously concerns relative dynamic permeability. As part of the experimental studies, in [
14], two liquids of the same viscosity were used, in contrast to the most commonly used water–air system, to study the pressure dependence of the interface discontinuity of an imbibition process. A capillary pressure threshold of 
 is required for the movement of the interface, and from this threshold, a nonlinear dependence of 
 and the velocity of l interface are revealed. At very high speeds, even an inversion of the interface leading to a concave curvature with respect to the wetting phase is observed. Models that take dynamic capillary pressure into account are also called [
9] extended models.
We symbolize with () the classical or so-called macroscopic capillary pressure, also called the equilibrium capillary pressure, and it represents the difference between the phase pressures  in thermodynamic equilibrium. One of the results that can be obtained is to find  using classical patterns .
Among the works that examine static drainage experiments in different vertical columns, we mention what was done by the researcher Stauffer in 1978 [
15], where he plotted the relevant capillary differences against the rates of change, then Stauffer decided to take the linear dependence into account and, in turn, determined the dynamic capillary pressure 
 as follows:
      where 
 represents the dynamic effect and is also given by
      
In most of Stauffer’s work, the value of  belongs to the field . We recall that () are coefficients of the dimensionless scale and capillary pressure, respectively, while  represents the equilibrium capillary pressure. As directed by Brooks-Corey , Stauffer implemented .
Also, supposing the density of water is constant, we define new 
 as follows:
	  
Using (
1), the model 
 is described as follows:
We supposing that Newtonian fluids exist immiscible and incompressible in the displacement process with a rigid porous medium and a spherical fluid/fluid interface. In [
11,
16], the following model for dynamic capillary pressure is suggested:
Here, 
 and 
 represent the equilibrium capillary pressure defined by the equation of Laplace, the surface tension between the two phases, wetting and non-wetting, the spherical interface radius, and the non-equilibrium effects. As in [
15], the capillary pressure differential at equilibrium is given by the rate of change in saturation of the wetting phase.
In a series of articles, Hassanizadeh and Gray [
10,
12,
17] developed a theory of multiphase flow in porous media based on thermodynamics. They constructed balance equations for mass, motion, and energy. These equilibrium equations were first formulated at the microscopic scale and then extended to the macroscopic scale. In sequence, the equilibrium equations are superseded in the second law of thermodynamics. Thus, new expressions can be obtained for effective parameters such as relative permeability and capillary pressure, which are based on deep physical considerations. Thus, by means of the general conservation equations at the microscopic scale and the second law of thermodynamics, and taking into account the continuity of the interface, the following inequality was obtained:
Based on this inequality, we can deduce that if (
), then (
). On the other hand, if (
), then (
0). Considering a linear relation between 
 and 
, which by hypothesis remains close to thermodynamic equilibrium states, we obtain the following:
In this case, the non-negative coefficient of delay 
, defined by Hassanizadeh and Gray, is given by the linear expression (
6).
Another model that takes into account dynamic effects on capillary pressure has been proposed by Barenblatt in [
13]. Specifically, this alternative approach refers to dynamic models for both capillary pressure and relative permeabilities, considering non-equilibrium effects related to the phase distribution in the porous medium. In this model, it is suggested that, in a process with rapid changes in the phase saturations, the time required to modify the phase arrangement, defined as the redistribution time 
, must be taken into account. In [
13], it is postulated that the relative permeabilities, 
 and 
, and the capillary pressure, 
, can be obtained by the usual parametrizations obtained at a steady state, but calculating these quantities from an “apparent saturation” 
, which is the saturation imbalance, can be seen as the actual saturation in a future state. Estimating 
 is proposed as a simplified empirical model:
      where the capillary dynamic pressure becomes,
      
      recalling that 
 is a monotone decreasing function. Thus, the pair of imbibition processes (
) and capillary pressure during fast procedures are less than for slow processes, which agrees with the model mentioned above. Considering the dynamic effects of capillary pressure, we can make a relation, from a formal point of view, between the Barenblatt model (
7) and (
8) and the models mentioned above, in particular, the Hassanizadeh–Gray model (
6). Here, we make an extension of the Taylor series of (
8),
      
Here, it is considered that 
 is much smaller than the characteristic timescale of the [
13] process, while we make the following approximation,
      
      where we have identified the dynamic effect coefficient,
      
Thus, a relationship can be established between the dynamic effect coefficient and the phase redistribution time, and a link between the different empirical and theoretical models can also be drawn.
  2. Mathematical Model
This is a non-linear partial differential equation describing the motion of a fluid 
i. It is written as follows:
      where 
, 
, 
, and 
 represent, respectively, the porosity, density, saturation, and velocity of the 
 phase. We apply Equation (
12) to the wetting 
 and non-wetting phases 
; moreover, the two fluids are assumed to be incompressible, so the density 
 remains constant in space and time. We divide each equation of the system (
12) by 
 in order to obtain the following system:
For Darcy’s law in the two-phase case, see [
18], it is always expressed as a function of a pressure gradient 
 and the permeability term 
K. However, this time, the permeability coefficient is weighted by the absolute permeability and the relative permeability:
      where 
 is the permeability tensor of the porous medium, 
 is the relative permeability of phase 
i, 
 is the viscosity, 
 is the pressure, 
 is the density of phase 
i, and 
 is the gravity term. We define the mobility of phase 
i by 
 with 
. Suppose that the two phases occupy all the pores of the medium; then, the saturations verify the following:
The overall pressure design for static capillary pressure is given in [
19,
20,
21,
22]. We define the same concept for dynamic capillary pressure, considering that
      
      where the function 
 is increasing and stands for classical static capillary pressure, and 
 is the damping coefficient. This global pressure 
p can be written as follows:
      where the artificial pressures are denoted by 
 and 
 and are defined by the following:
      where 
 is the total mobility, and 
 is the mobility of phase 
. The term capillary is also defined by
      
Now, when we write the expression of the velocity of each phase respecting the global pressure and the capillary term, we find that
      
We denote 
, and using the velocity expressions (
20), we obtain the following:
To obtain the pressure equation, we take the difference between the two previous equations, and we find
      
      with 
. We assume that the flow takes place in the time interval 
. We can write the system obtained above in the following form:
The reservoir is denoted as 
, a bounded open set of 
. We set 
, 
, where 
 denotes the boundary of 
. The first equation of 
 is called the saturation equation, and the second is the pressure equation. We define the functions 
 and 
 as following 
, with 
 and 
. Next, 
, where 
 and 
 for all 
. After that, 
; hence, 
 Finally, 
; therefore, 
 If the total mobility is a convex function and
      
      we use the previous notations. As a result, we can write
      
 The boundary conditions 
 are written as folows:
      where 
 is the outward unit normal to 
, and the positive measure of 
 is not equal to zero. The initial condition 
 is written as follows:
The preceding considerations lead us to adapt the following strategy for proving the existence of a weak solution for the problem  with conditions  and :
First step: Replace the non-regular problem with a regularized problem, replacing  by  with , a constant. Here, for  to be fixed, we will study the regular nonlinear problem. Here, we will prove the existence of a solution.
Second step: Study the non-regular problem. By letting the  veer toward zero, we will try to obtain a solution to this problem.