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    A NON-ISOTHERMAL FLOW AND

    TRANSPORT MODEL

    FOR A SINGLE FRACTURE IN A POROUSMEDIUM AT CORE SCALE

    Martn Daz-Viera1 and Rafael Cabrera-Gutierrez1

    1)Instituto Mexicano del Petrleo

    [email protected]

    9th North American Workshop on

    Applications of the Physics of Porous

    Media, 2011

    October 26-29, 2011, CICESE, Ensenada, Mxico

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    Outline

    Background

    MotivationIntroduction

    Review of discrete fracture models

    General Methodology

    Conceptual Model

    Mathematical Model

    Numerical Model

    Computational Model

    Numerical Implementation in COMSOL

    Water Coreflooding Case Study

    Remarks and Future Work

    References

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    Background

    Naturally fractured reservoirs containa significant portion of proved reserves

    worldwide.

    In Mexico historically such oil fieldshave contributed with the greatest

    percentage to the total oil production in

    the country.

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    Background

    Currently, several of these reservoirshave entered in a declination period of

    its production because they have

    exhausted the natural energy they

    possessed during their primary stage.

    The application of secondary recovery

    methods, such as gas injection, have evenbecome ineffective to restore or maintain

    the production pressure.

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    Background

    However, the reservoirs still containconsiderable reserves that could be

    recovered through application of

    enhanced oil recovery (EOR) methods.

    For these purposes, at the present time

    it is being considered the application of

    thermal methods such as air injectioninto the reservoir for an in situ

    combustion recovery process.

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    Motivation

    The application of EOR methodsrequire highly sophisticated laboratory

    studies

    to obtain the optimal parameters that

    control the recovery process

    to establish the optimal design strategyfor its implementation in each specific oil

    field.

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    Motivation

    In this regard, the models that describeflow and transport in fractured

    reservoirs become a fundamental

    research tool to take the mostappropriate decisions

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    Introduction

    In recent years there is a growinginterest in modeling enhanced recovery

    processes in greater detail and accuracy

    for fractured reservoirs[1-4].

    A series of alternative models which,

    unlike the classic models of dual porosity

    [5],fractures are modeled explicitly [6-7]

    have been proposed .

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    Introduction

    These models are called discretefracture models.

    Here, starting from a review of

    previously published discrete fracture

    approaches the main issues and

    challenges are presented

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    Introduction

    A general non-isothermal flow and transportmodel for a single fracture in porous media is

    derived, considering the fracture as an

    interface betweenA numerical implementation is proposed

    using a standard finite element formulation.

    An application for a simple recoveryexperiment at core scale and laboratory

    conditions is discussed

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    Review of discrete fracture models

    The discrete fracture model is a geometrical simplified,

    single porosity model.In the discrete fracture model, fractures are representedusually by (n-l)-dimensional elements in n-dimensionaldomain.

    For example, the line elements are used to representfracture in 2-D while two-dimensional elements or surfacesare used in 3-D.

    One of the earliest papers using the discrete fracture modelto examine fluid flow in a fractured porous medium was

    published by Wilson and Witherspoon (1974). They studiedthe steady-state seepage in a fracture system beneath a damusing two finite element models.

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    Review of discrete fracture models

    Gureghian (1975) presented a finite element model for

    three-dimensional fluid flow in a fractured porousmedium. In his work the triangles that represent thefractures are made to correspond to the faces of aselected matrix element, represented by tetrahedrons.

    Noorishad et al. (1982) studied two-dimensionaltransient flow in a fractured medium using an upstreamfinite element method to avoid oscillations inconvective dominated flow.

    A similar approach was also used by Baca et al. (1984)in the study of two-dimensional single phase flow withheat and solute transport.

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    Review of discrete fracture models

    For multiphase flow, Bourbiaux et al. (1999)introduced a discrete fracture model based on a finitevolume discretization method. They applied a joint-element technique to represent the fracture networks in

    a two-dimensional problem.Kim et al. (2000) used an approach similar to that ofNoorishad et al. and Baca et al. to develop a paralleltwo-phase black oil model.

    Karimi-Fard et al. (2001) adopted the same concept todevelop an IMPES two-phase black oil model, whereasKim et al. used the fully implicit method.

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    Review of discrete fracture models

    Yang (2003) and Fu (2005) developed a control-

    volume finite element based discrete fracture model fortwo-phase, two-dimensional and two-phase, three-dimensional block oil simulation, respectively. Both ofthem used flux-based upstream schemes to ensure local

    flux continuity.Several finite difference-based unstructured discretefracture models have also been proposed. For example,Karimi-Fard et al. (2004) used two point flux

    approximation and introduced a connectivitytransformation called "star-delta" to eliminate controlvolume at the fracture intersection, which causesnumerical instability and small time step.

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    General Methodology

    The general procedure for a model development includes the

    following four stages:

    Conceptual Model: The hypothesis, postulations andconditions to be satisfied by the model.

    Mathematical Model: The mathematical formulation of theconceptual model in terms of equations.

    Numerical Model: The discretization of the mathematicalmodel by the application of the appropriate numerical methods.

    Computational Model: The computational implementation of

    the numerical model.

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    Conceptual Model

    Fractures are considered as

    Case A: n-dimensional porous subregions (including aperture)

    Case B: (n-1)-dimensional porous subregions (excludingaperture)

    Figure A Figure B

    Porous medium

    Porous medium

    Fracture

    1

    2

    1

    mp

    2

    mp

    f a 1n n 2n

    1mp

    Porous medium

    2

    mp

    Porous medium

    Fracture

    1n n

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    Mathematical Model

    Case A: The same mathematical continuous model is applied tomatrix and fracture, but with different properties

    Case B: A specific (n-1) dimensional model for fractures isderived from the n dimensional model for the matrix

    Case A and B: Additional interface (boundary) conditionsbetween fracture and matrix are considered

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    Mathematical ModelFluid flow model in a homogeneous porous medium with discontinuities

    B t

    M t d x (1)

    where poro tot alV V is the porosity and is the fluid density.

    Global balance equation

    ( ) ( , ) ( , ) ( , ) B t B t t

    d M t g x t d x x t nd x g x t d x

    dt

    (2)

    Local balance equation

    ;t u g x B t (3) v ;u n g x t (4)

    Where vu - is the Darcy velocity

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    Mathematical Model

    If we consider that there is no diffusion ( 0 ) and that the interface is still ( v 0 )

    in the case when the fluid and porous media are slightly compressible the above

    equations can be rewritten as follows

    ;tp

    c u g x B t t

    (1)

    ;u n g x (2)Where tc - is the total compressibility

    For constant density results

    ;t pc u g q x B t t

    (3)

    ;u n g q x (4)

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    Mathematical Model

    Figure A Figure B

    Porous medium

    Porous medium

    Fracture

    1

    2

    1

    mp

    2

    mp

    f

    a

    1

    n n 2n

    1

    mp

    Porous medium

    2

    mp

    Porous medium

    Fracture

    1n n

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    Mathematical Model

    Mass balance equations for porous regions (MP)

    ; 1,2i

    ii i i mp

    t i

    pc u q x i

    t

    (1)

    ; 1,2i

    i i

    iu n q x i (2)

    where ; 1,2

    i

    i i mp

    iku p x i

    (3)

    Mass balance equations for fracture region (F)

    ;

    ff f f f f

    t

    pc u q x

    t

    (4)

    where ;

    f

    f f fk

    u p x

    (5)

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    Mathematical Model

    The following additional conditions are considered:

    a) Continuity of the flow through interfaces

    0; ; 1,2f ii

    iq x u n u n i (1)

    b) Continuity of pressure through interfaces

    ; 1,2f i p p i (2)

    The equation for fracture can be rewritten as

    ;f

    f f f f f f

    t n

    pc u u q x

    t

    (3)

    Where n

    and

    are the normal and tangential divergence operators, respectively.

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    Mathematical Model

    If we integrate the last equation in the normal direction of the fracture, it is

    2 1

    ;f

    f f f f f f

    t

    Pa c u n u n U Q x

    t

    (1)

    where2

    1

    2

    af f

    aa

    P p d n

    ,2

    2

    af f

    aU u d n

    y2

    2

    af f

    aQ q d n

    We can rewrite velocity in the fracture in terms of the normal and tangentialcomponents:

    f f f

    nu u u (2)

    where

    f

    f fnn n

    ku p

    normal and

    f

    f fk

    u p

    tangencial velocities (3)

    Integrating tangential velocity in the fracture in the normal direction the Darcy law

    for a fracture in (n-1) dimensions is obtained ;

    f

    f fk

    U a P x

    (4)

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    Mathematical ModelSummary of single-phase flow through a fracture

    ; 1,2i

    ii i i mp

    t i

    pc u q x it

    (1)

    ; 1,2

    mp

    i i mpii

    ku p x i

    (2)

    1 2 ;f

    f f f f

    t

    Pa c U u u n aq x

    t

    (3)

    ;

    f

    f fk

    U a P x

    (4)

    11 2

    1 21

    1 2

    1 1;

    2 2

    f f f u n p u n P x

    (5)

    22 1

    2 12

    2 1

    1 1;

    2 2

    f f f u n p u n P x

    (6)

    ; \ 1,2i i mp

    i p p x i (7)

    ;f fP P x (8)

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    Numerical Model

    Case A: Structured (SDFM) or unstructured (UDFM) mesh

    refinement in the fracture region

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    Numerical Model

    Case B: Structured discretization (SDFM) using finite

    difference method. For example, Lee et al. (2001) presented ahierarchical modeling of flow in fractured formations.

    Case B: Unstructured discretizations (UDFM), there are twomain approaches: finite-element, Baca et al. (1984) and finite-volume (or control volume finite-difference) methods, Karimi-Fard et al. (2004).

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    Computational Model

    Case A: The same code could be used for both the matrix and

    the fracture regions, but additional coding for coupling fractureand matrix interactions are required.

    Case B (SDFM): the code for matrix simulation could bemodified to include the fracture effects as source term similar tothe concept of the wellbore productivity index (PI) introduced by

    Peaceman (1978) to derive the transport index between matrixand fractures in a grid cell.

    Fluid flow is formulated as a well-like equation inside thefracture and a source/sink term between fracture and matrix.

    The source/sink term allows for coupling multiphase flowequations in fractures and matrix.

    The pressure is assumed to vary linearly in the normal directionto each fracture.

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    Computational Model

    Case B (UDFM): The USDFM uses the discretization approach

    proposed by Karimi-Fard et al. (2004).The method is based on unstructured gridding and employs theso-called lower dimensional approach to DFM gridding wherethe rock matrix is modeled by 3D polyhedral cells and thefracture network is represented by a subset of the 2D interfaces

    separating grid cells.The material balance for each control volume requires theknowledge of neighboring control volumes (a connectivity list)and the transmissibility associated with each connection in orderto compute fluid exchange between neighboring control

    volumes.A two-point flux approximation is applied in the transmissibilitycalculations.

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    Numerical Implementation in COMSOL

    Biphasic oil-water flow model:

    Two nonlinear coupled equations.

    Pressure Equation (elliptic)

    Saturation Equation (degenerate parabolic in general or

    hyperbolic of first order, whenpcow=0)

    ;cow

    w w w o

    w

    dp

    k p k S q qdS

    ;w coww w w w

    w

    S dpk S k p q

    t dS

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    Numerical Simulations

    Water Coreflooding Case Study

    Water flooding experiment through a sandstone

    core under laboratory conditions.

    in

    pg

    outp

    0.25 m

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    Numerical Simulations

    Water flooding experiment through a sandstone

    core under laboratory conditions.Modified Brooks-Corey model for relative permeabilities

    Corey model for capillary pressure

    where characterizes the pore size distribution.

    1

    1

    w rw

    cow w t

    rw ro

    S S p S p

    S S

    0 0; ;1w on n

    rw w rw e ro w ro ek S k S k S k S

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    Data for Numerical Simulations

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    Data for Numerical Simulations

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    Property Value Description

    L 0.25 [m] Core length

    d 0.04 [m] Core diameter

    muw 1e-3 [Pa*s] Water viscosity

    muo 7.5e-3 [Pa*s] Oil viscosity

    rho_w 1.0 [g/cm^3] Water densityrho_o 0.872 [g/cm^3] Oil density

    p_out 10 [kPa] Outlet pressure

    u_w_in 25 [cm/h] Inlet velocity

    phi_M 0.2295 [1] Matrix porosity

    k_M 326 [milidarcy] Matrix permeability

    Swr_M 0.2 [m^3/m^3] Residual water saturation (matrix)

    Sor_M 0.15 [m^3/m^3] Residual oil saturation (matrix)

    p_t_M 0.1*1e5 [Pa] Entry pressure for Brooks-Corey Pc model (matrix)theta_M 2 Exponent for Brooks-Corey Pc model (matrix)

    nw_M 4 Corey exponent for water (matrix)

    no_M 6 Corey exponent for oil (matrix)

    krw_0_M 0.1 End point Kr to water at residual oil saturation (matrix)

    kro_0_M 1.0 End point Kr to oil at residual water saturation (matrix)

    phi_F 1.0 Porosity (fracture)

    k_F 1000 [milidarcy] Permeability (fracture)

    Swr_F 0.0 [m^3/m^3] Residual water saturation (fracture)Sor_F 0.0 [m^3/m^3] Residual oil saturation (fracture)

    p_t_F 0.0 [Pa] Entry pressure for Corey Pc model (fracture)

    theta_F 2 Exponent for Brooks-Corey Pc model (fracture)

    nw_F 1 Corey exponent for water (fracture)

    no_F 1 Corey exponent for oil (fracture)

    krw_0_F 1.0 End point Kr to water at residual oil saturation (fracture)

    kro_0_F 1.0 End point Kr to oil at residual water saturation (fracture)

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    Numerical Simulations: the mesh

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    Numerical Simulations: a zoom of the mesh

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    Numerical Simulations: k_F=1000 mD

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    Numerical Simulations: k_F=10,000 mD

    S

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    Numerical Simulations: k_F=100,000 mD

    R f

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    References1. Alboin, C., Jaffr, J., Roberts, J. and Serres, Ch., Modeling fractures as

    interfaces for flow and transport in porous media, Research Report N 4390, INRIA,2002.

    2. Bogdanov, I. I., Mourzenko, V. V., Thovert, J.F. and Adler, M., Pressuredrawdown well tests in fractured porous media, Water Resources Research, Vol. 39,No. 1, 1021, doi:10.1029/2000WR000080, 2003.

    3. Hoteit, H. and A. Firoozabadi, Multicomponent fluid flow by DiscontinuousGalerkin and Mixed methods in Unfractured and Fractured Media, Water ResourcesResearch, Vol. 41, 2005.

    4. Huang, Chung-Kan, Development of a general thermal oil reservoir simulatorunder a modularized framework, PhD dissertation, Department of ChemicalEngineering, The University of Utah, May 2009.

    5. Lemonnier, P. and Bourbiaux, B. Simulation of Naturally Fractured Reservoirs.State of the Art. Part 2: Matrix-Fracture Transfers and Typical Features of NumericalStudies. Oil & Gas Science and Technology Rev. IFP, Vol. 65 , No. 2, pp. 263-286,2010.

    6. Martin, V. , Jaffre, J. and Roberts J., Modeling fractures and barriers as interfacesfor flow in porous media, SIAM J. Sci. Comput.,Vol. 26, No. 5, pp. 16671691, 2005.

    7. Tatomir, Alexandru-Bogdan, Numerical Investigations of Flow through FracturedPorous Media, Master's Thesis, Master of Science Program, Universitt Stuttgart,November 29, 2007.

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    Thank you

    for your attention!