Theoretical stability analysis of mixed finite element model of shale-gas flow with geomechanical effect
Energy Research Laboratory, College of Engineering, Effat University, 21478 Jeddah, Kingdom of Saudi Arabia
2 Department of Mathematics, Faculty of Science, Aswan University, 81528 Aswan, Egypt
3 School of Mathematics and Statistics, Hubei Engineering University, Xiaogan, 432000 Hubei, PR China
4 Division of Physical Sciences and Engineering (PSE), King Abdullah University of Science and Technology (KAUST), Thuwal, 23955-6900 Jeddah, Kingdom of Saudi Arabia
* Corresponding author: email@example.com
Accepted: 6 April 2020
In this work, we introduce a theoretical foundation of the stability analysis of the mixed finite element solution to the problem of shale-gas transport in fractured porous media with geomechanical effects. The differential system was solved numerically by the Mixed Finite Element Method (MFEM). The results include seven lemmas and a theorem with rigorous mathematical proofs. The stability analysis presents the boundedness condition of the MFE solution.
© M.F. El-Amin et al., published by IFP Energies nouvelles, 2020
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Finite Element Methods (FEMs) are effective numerical techniques for solving the complex engineering problems. FEMs appeared in the middle of the last century and were widely used in solid mechanical applications . The FEM has been extensively investigated and developed in the last five decades , and now is used for highly nonlinear problems . However, the standard FEM faced certain instabilities for solving elliptic problem that describe the flow in porous media [4, 5]. On the other hand, the Mixed Finite Element Methods (MFEMs) have succeeded in eliminating such instabilities [6, 7] as it may be extended to higher-order approximations as well as it is a locally conservative method . Different physical variables can be treated differently in the MFEM from other variables. For example, the enhanced linear Brezzi-Douglas-Marini (BDM1) space is used for speed approximation, which requires more precision, while the piece-wise constant space is used for pressure approximation. The models of shale-gas transport were mainly developed by adapting the traditional models of flow in fractured porous media. Warren and Root  have developed an idealized geometric model to investigate the behavioral flow in fractured porous media. The dual porosity model including stress of fracture was used to investigate the flow of gas in the shale [10, 11], while, the dual-continuum model was used to describe gas flow Kerogen shale [12, 13]. Several versions of the dual-continuum model have been developed to include, for instance, adsorption, heat, deformation and Knudsen diffusion [14–17]. Several authors presented research work in shale gas reservoirs with geomechanical effects, such as Wang et al. , Lin et al. , and Yang et al. . Wang et al.  developed a general model including embedded discrete fractures, multiple interacting continua and geomechanics in shale gas reservoirs with multi-scale fractures. In , authors provide insights on fracture propagation using reservoir flow simulation integrated with geomechanics in unconventional tight reservoirs. Effects of multicomponent adsorption and geomechanics are investigated in a shale condensate reservoir . Girault et al.  have introduced a priori error estimates for a discretized poro-elastic-elastic system, in which the flow pressure equation is discretized by either a continuous Galerkin scheme or a mixed scheme, while, elastic displacement equations are discretized by a continuous Galerkin scheme. El-Amin et al.  have used the MFEM with stability analysis to simulate the problem of natural gas transport in a low-permeability reservoir without considering fractures. The authors  extended their work to cover fractured porous media and the rock stress-sensitivity with considered stability analysis of the MFEM. In this work, we present a theoretical basis with proofs of the stability analysis of the MFEM (in Ref. ) including the necessary lemmas and theorem.
In this section, the mathematical model of the problem under consideration is developed. The Dual Porosity Dual Permeability (DPDP) model is employed to describe the gas transport in fractured porous media which consists of matrix blocks and fractures. The absorbed gas and the free gas coexist in the matrix blocks, however, the free gas exists in fractures only. The mass of free gas accumulation is , and the adsorbed gas accumulation (Langmuir isotherm model) is [24, 25],(1)
The gas compressibility factor, which is given by Peng-Robinson equation of state ,(3)(4)(5)
Moreover, based on the following definitions, and are treated as constants ,(12)and(13)
The coefficient of crossflow between the matrix and fracture domains is defined as ,(18)such that is given by,(19)
As the porosity increases the difference becomes positive and vice versa. Also, the coefficient becomes small based on the change in the porosity, and it becomes positive if porosity increases and negative if porosity decreases.
The MFEM contains two spaces for a scalar variable and it’s flux. The MFEM was developed to approximate both variables simultaneously and to give a higher order approximation for the flux. A compatibility condition must hold for the two spaces to insure stability, consistency and convergence of the mixed method and by considering more constraints to the numerical discretization.
Now, let us define the inner product in as,(27)and the inner product on as,(28)Given,(29)is the largest Hilbert space, such that and are well defined, therefore, . It is needed that and . The Hilbert space with norm given by,(30)(31)
Thus, the normal component is continuous across the inter-element boundaries.
Moreover, it is useful to present the elements that are designed to approximate , which satisfies,(35)and,(36)where is discontinuous piecewise constant and is piecewise linear.
Let and are, respectively, the matrix and fracture in a polygonal/polyhedral Lipschitz domain (on which we define the standard space such that ), with the boundaries, and . One may write the above dual-porosity model in the following general form,(37)(38)(39)(40)where(41)and(42)
The functions and are moved to the left hand side to avoid discontinuity when we integrate and by parts. Selecting any and , the mixed finite element weak formulation can be written in the following form,(43)(44)(45)(46)
Now, let the approximating subspace duality and be the -th order () Raviart–Thomas space (RTr) on the partition . The mixed finite element formulations are stated as below: find and such that,(47)(48)(49)(50)for any and .
In order to obtain an explicit formulation for the flux, we employ a quadrature rule along with the MFE method to . The total time interval is divided into time steps with length . The superscript denotes for the current time step, while denotes for the previous one. We use a backward Euler semi-implicit discretization for the time derivative terms. The following scheme has been developed,(51)(52)(53)(54)Given and , the numerical procedure to calculate pressure and velocity is presented here,
Update the thermodynamical variables explicitly.
In this section, we carry out the stability analysis of the proposed MFE method, which ensures that the discrete solutions are bounded in a physically reasonable range. The key issue encountered in the stability analysis is the nonlinearity of the matrix and fracture pressures. In order to resolve this issue, we need to define some auxiliary functions and analyze their boundedness. Now let us define the following functions,(55)(56)
is a special function called the exponent integral function. As stated above in the model formulation that the coefficient is positive in the case of increasing porosity and negative in the case of decreasing porosity.
Proof. Note that the value of the exponent integral function is negative and (small for big values of ), therefore the quantity, has always a positive value which has lower and upper bounds, namely,(63)where . On the other hand, in shale reservoir, it is well known that the initial pressure has the maximum value, i.e., , while, the pressure of the well has the minimum value, i.e., . Therefore, we have,(64)(65)and,(66)where . Therefore, for the case of increasing matrix porosity, , and sufficiently large , and holding (63)–(66), the following coefficient is positive, i.e.,(67)(68)Therefore,(69)and this completes Lemma 5.1 proof.
Proof. It is clear that, , so,we always have, . Holding the assumptions (75) and (76), therefore we find, , and integrate (58) over for the case of decreasing porosity, , which proves (74), and this completes the proof.
As stated above, for the case of the decreasing porosity, , the coefficient remains positive, then the above inequality holds. This completes the lemma proof.
Proof. Similar to the previous proofs.
Proof. Since is bounded by and , i.e., , then, , such that is positive number. Holding the conditions (84), one may find that,(85)
Integrating (92) from 0 to () yields,(93)
Remark 5.1. In Lemma 5.6, if we do not use the coefficient, , and just use the coefficient, , then the coefficient of the term, in will be moved from into . Thus, the definitions of both and will be slightly changed without loss of the stability concept.
In this work, stability analysis of the MFE solution of the gas transport in a low-permeability fractured reservoir with stress-sensitivity effect has been considered. The dual-porosity dual permeability model with the slippage effect and the apparent permeability have been used to describe the flow in a low-permeability fractured porous media. Stability analysis of the MFEM is presented theoretically and numerically. We proved a seven lemmas and a theorem on the stability of the MFEM. Stability conditions are stated and estimated. Variation in the porosity is correlated to the stress-sensitivity effect and depends on the values of the corresponding physical parameters. For example, the coefficient is relatively small depending on the variation of the porosity. It has a positive value in the case of porosity increasing while it has a negative value in the case of porosity decreasing. Lemmas 5.1 and 5.3 discuss the positive case, while Lemmas 5.2 and 5.4 discuss the positive case. Lemmas 5.5 and 5.6 discuss the two cases.
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