22. SPE-13846-PA

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    x ct Solutions for Infinite-

    Conductivity Wells

    Paul Papatzacos

    SPE, Rogaland Research Inst.

    Summary. In pressure transient testing, the infinite-conductivity condition translates mathematically into a

    uniform-pressure (or uniform-potential) condition at the well. This means the flux at different points of the well

    should be determined in such a way that potential remains uniform at the well. The integral equation for

    accomplishing this

    is

    solved analytically to yield the Laplace-transformed potential. For fractured-well problems,

    this leads to a relatively fast algorithm for drawing type curves directly on a computer screen. For limited-flow

    entry problems, the analytical pressure expression can be used with the method of images to treat problems in

    reservoirs of finite thickness and/or areal extent.

    Introduction

    One traditionally thinks

    of

    a well as having infinite con

    ductivity in the direction parallel to its axis. This assump

    tion is also included as a standardoption inmost numerical

    reservoir simulators. In pressure transient testing, the con

    cept is important for wells with limited flow entry and

    for fractured wells.

    The infInite-conductivity condition translates mathemat

    ically into a uniform-pressure (or rather uniform-potential)

    condition at the well. This means that the flux at differ

    ent points of the well is unknown a priori and must be

    determined in such a way that potential is uniform at the

    well. Muskat 1 recognized that this amounts to solving an

    integral equation. Muskat and later Gringarten and

    Ramey

    2

    showed how to solve the integral equation for

    mulation numerically by dividing the source into small

    elements, each having uniform flux. To determine these

    elementary fluxes, two conditions must be applied: they

    must sum to the required total rate and they must produce

    a uniform potential at the well. This method was applied

    by Gringarten and Ramey 3 to the limited-flow-entry

    problem and by Gringarten et at. 4 to the fractured-well

    problem.

    In the present paper, this integral formulation is solved

    analytically

    to

    yield the Laplace-transformed potential.

    For

    the fractured-well problem, the purpose of this cal

    culation is to obtain an expression for the pressure that

    leads to a relatively fast algorithm for drawing type

    curves, both for single-well testing and for interference

    testing, directly on a screen. It is usually easier to obtain

    numerical results from analytical expressions than from

    their nonanalytical analogs.

    For the limited-flow-entry problem, on the other hand,

    the purpose

    of

    the calculation is different. Because the

    reservoir is considered to be infinite, both laterally and

    in thickness,

    type

    curveswould not have a direct reservoir

    engineering application. The interest in an analytical ex

    pression in this case lies in the possibilities it offers in

    conjunction with the method of images to treat problems

    in reservoirs

    of

    fmite thickness and/or finite areal extent.

    Copyright 1987 Society of Petroleum Engineers

    SPE

    Reservoir

    E m r i n f p r i n ~

    Mil

    One such problem

    of

    interest is the calculation

    of

    limited

    flow-entry pseudoskin

    5

    ; another is water coning.

    6

    Some

    details about the treatments of these problems will be

    given.

    Limited Flow Entry Problem

    Dimensionless Variables

    and

    Spheroidal Coordinates.

    .The situation considered is that of a line-sourcewell with

    limited flow entry in a reservoir that is infinite in all three

    dimensions. As shown in Fig. 1, the axes are chosen so

    that the perforated wellbore covers Interval -a , +a

    along the

    z

    axis. Note that, because of symmetry across

    the xy plane, one is also solving the problem of a semi

    infinite reservoir with a horizontal no-flow upper bound

    ary, anda line-source well perforated from the top down

    ward to the depth

    of

    a

    kH and k y are the permeabilities in the horizontal and

    vertical directions, respectively. Dimensionless coor

    dinates are defined as

    XD

    = ky/k

    H

    Ih x/a ,

    1a

    YD = ky/k

    H

    1h Y/a ,

    lb

    and

    ZD=z/a lc

    and dimensionless time as

    2.367 X

    1 ky t

    (2)

    .pl c

    t

    a

    2

    The pressure potential,

    .p=p P

    o

    zl144.0,

    (3)

    can easily be shown to obey the same diffusion equation

    as the pressure, p. An expression for.p can

    be

    written

    in terms of the appropriate Green function and of an

    unknown source function. 3 The latter must

    be

    determined

    217

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    x

    -a

    y

    a

    z

    Fig. 1-Limlted-flow-ent ry problem.

    The

    well Is perforated

    along Interval

    a, +a

    on the z axis thick line .

    Fig. 2-Limlted-flow-entry problem. Sections

    a plane

    containing

    ZD

    with

    ~ . c o n s t a n t

    and a-constant surfaces.

    The resulting ellipses and hyperbolas are labeled by the

    corresponding and

    a

    values

    a

    Is In degrees .

    in such a way that

    cI>

    does not vary with

    z

    at the wellbore.

    At this point, it

    is.

    important to choose a system

    of

    coor

    dinates that allows an easy representation

    of

    the line

    source well: prolate spheroidal coordinates,

    4

    ~ , a . , { j , re

    lated to the usual Cartesian coordinates by the following

    equations.

    x

    D =sinh sin

    a.

    cos

    {j, :

    (4a)

    YD = sinh sin

    a.

    sin

    {j,

    (4b)

    and

    ZD

    = cosh cos a. (4c)

    We can now write an expression for the dimensionless

    potential,

    D, in terms of the unknown dimensionless

    flux along the well,

    qwD

    (see Appendix A for a deriva

    tion and for the definition

    of q wD :

    r r ll

    D =

    J

    dtv

    J

    da. sin a.

    qwD a ,tD)

    o 0

    e _[ R

    2

    /4 I

    D

    -I h)]

    x , (6)

    4J;( tD

    - tv )

    where

    R

    2

    = (sinh sin

    a) 2

    +(cosh cos

    a cos a. )2.

    (8)

    e

    - [R ; /4 t

    D

    t h ]

    x

    4J;( tD - t v ) ; (9)

    Note that

    R

    2

    = rJ + ZD -Z V)2

    and that

    D

    depends on

    a., and tD By setting ~ O in Eq. 6, we obtain

    cID

    at the wellbore, which we denote by

    4>wD tD ,

    thus

    making explicit the fact that it is uniform along the well-

    Le., independent

    of

    the coordinate

    a.:

    ak

    H

    - - - 4 i -4 (7)

    4 2j tqt

    4>D

    and

    The sections

    of

    some

    c o n s t a n t - ~

    and constant-a. surfaces

    with an arbitrary rD,ZD plane are shown in Fig. 2. The

    ellipsoids become thinner as becomes smaller. The el

    lipsoid for = 0 has degenerated into Segment(

    - 1

    ,

    +

    1)

    on the

    ZD

    axis. In other words, the producing interval

    of

    the well, given by XD =0

    YD

    =0 - 1 ~

    ~

    +1 in

    Cartesian coordinates, is simply given by =0 in sphe

    roidal coordinates. An arbitrary point at the wellbore has

    a coordinate equal to zero and an

    a.

    coordinate in Inter-

    val

    (0, 11 ).

    _

    2

    2 ) 1 h _ n h t. . (C)

    r D - XD

    +

    YD - SI . c; SID

    a. . .

    . . . . . . . . . . . . . :J

    These new coordinates are restricted to .the intervals

    O ~ ~ ~ o O

    0 ~ a . ~ 1 I , and 0 ~ { j ~ 2 1 1 .

    The surfaces with constant are rotational ellipsoids,

    while the surfaces with

    a.

    constant are rotational hyper

    boloids (oftwo sheets). The axis

    of

    rotation for both these

    families is the ZD axis. The surfaces with {j constant are

    planes containing the

    ZD

    axis. Because

    of

    the rotational

    symmetry, it is useful to introduce

    218

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    In Eq. 9,

    R

    wis the expression obtained from Eq. 8 by

    setting

    =0.

    One must be careful, however, because

    w is known to be infinite f?r a

    l i n e - s o ~ r c e

    well. To

    avoid infinities in the calculatIons, we wnte

    2 . , 2

    R = sinh sin a + cosh cos a - c o s a

    10

    and let go to zero. This limiting process will be

    i ~ d ~

    cated at the proper place later. In other

    words lt

    IS

    assumed that the well is a thin ellipsoid that is forced to

    degenerate to a line. The question arises w ~ e t h e ~ it ~ o u l d

    be more realistic to model the well as a thm elbpsOld by

    choosing a ,small but nonzero v ~ u e . for w thus a ~ o ~ d

    ing the difficulties of taking the bmlt ThIS IS m

    deed possible, but it should be kept

    mmd that the

    solution given here is then only a p p r o X 1 m ~ t e . because an

    ellipsoidal well with w

    0 has a nonvamshmg surface,

    while the Green function used in Eq. 9 is correct for a

    reservoir with no boundaries at finite distances. ,

    We show in Appendix A that the flux,

    q wD,

    must

    satisfy

    d a

    sin qwD a,tD) =

    1 11

    o

    This is the analytical expression

    of

    the first condition

    imposed by Muskat

    and by Gringarten and R

    amey2

    on

    the elementary fluxes-i.e.

    that they add to the total rate.

    Th e

    second condition on qwD is expressed in Eq. 9: the

    flux rate must be such as to produce a uniform potential

    at the well.

    Statement of the Problem.

    is necessary to solve Eqs.

    9 and 11 for the two unknown functions

    w

    and q

    w

    .

    The time integration in Eq. 9 is a convolution, an

    obvious first step is to use the Laplace

    t r a n s f o r m a ~ l O n

    to

    eliminate one integration. Here

    [j t ]

    is the Laplace

    transform ofj t and S is the Laplace parameter. We first

    introduce the following notation:

    c C [ ~ D ~ , a , t D ] = 1 P ~ , a , s ,

    12

    c C [ ~ w D t

    D)] =1Pw S), 13

    and

    [qwD a,tD)]

    =

    U a,s).

    . 14

    One finds in Ref. 7 that

    exp[-

    R

    2

    / 4tD)]

    = exp -

    R.[;

    4 ;;t8

    R

    15

    so by taking the Laplace transform

    of

    Eqs. 6, 9, and 11,

    one obtains

    e -R

    1 P ~ , a , s = lh1d a

    sin a U a ,s) ,

    . .

    16

    o

    R

    SPE Reservoir Engineering,

    May

    1987

    e-

    Rw

    1Pw S) =

    lh

    dd

    sin

    a

    U a ,s) ,

    17

    o R

    w

    and

    da

    sin a U a,s) =

    lis,

    18

    o

    where

    R

    is given by Eq. 8 and

    R

    w

    by Eq. 10. Now the

    problem is to solve Eqs. 17

    and

    18

    for

    wand

    When

    the resultant expression for

    U

    is used in Eq.

    16

    and the

    integration performed, one obtains an

    e x p r e s s ~ o n

    for the

    Laplace transform

    of

    the dimensionless potential.

    Solution. Step

    1

    An analytical solution

    of

    the prob

    lem is made possible by the existence of an eigenfunction

    expansion

    of

    exp[- R:fi ]/R. This expansion is given in

    Refs. 8 and 9 for exp iTR /R and is written below for

    T=i.[; and for R given by Eq.

    8:

    R

    00

    1

    J

    = 2 [ ;

    --Son(i \lS, cos a )

    R

    n=O NOn

    XSon i.[;, cos a R b ~ i . [ ; , I R b ~ i.[;, cosh

    19

    In this expression,

    Smn

    is the angular spheroidal wave

    function while

    R

    and

    R

    are the radial spheroidal

    wave functions

    of

    the first and third kind, respectively

    see also Ref. 7 . In Eq. 19, only the

    f u ~ c t i o n s

    with

    f i ~ s t

    index equal to zero are involved. N

    mn

    IS the normalIZ

    ing constant; i .e. , for

    m=O,

    da sin a SOk k.[;, cos a)Soj i.[;, cos a)=okjN

    Ob

    o

    20

    where 0

    kj

    is the Kronecker delta.

    The following expression for SOn is needed:

    00

    SOn

    = d ~ ~ + r i . [ ;

    )P2k+r COS

    a) ,

    21

    k=O

    where P is a Legendre polynomial, and where

    r=O

    1 when

    m

    n

    is even odd . The diJn i:..{;) are expansion

    coefficients with known rules

    of

    calculation.

    9

    Step 2. The function U Laplace transformofthe flux,

    see Eq. 14 depends only on the angular coordinate

    ex

    and

    can be expanded in a series

    of

    eigenfunctions,

    SOn

    which

    form a complete set on Interval 0,1r . There is a sim

    plification because

    of

    the symmetry

    of

    the flux across the

    x D,YD plane; this implies that U is

    s y m m e t r i c a r o ~ n d

    a=1r/2-Le.

    that it is a function

    of

    cos

    2

    a. Accordmg

    to Eq.

    21

    and the properties

    of

    the Legendre polynomi

    als, one may then write

    00

    , U a,s)= 3kS02k i.[;, cos

    a),

    22

    k=O

    2 9

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    XD

    = cosh

    p

    cos

    v

    28a)

    Infinite onductivity Vertical-

    r cture

    Problem

    This problem s solution is exactly analogous to the

    one

    used previously.

    The reservoir is supposed to be isotropic, with constant

    p e r m e b i l i ~ k.

    The fracture is ,most easily represented

    in ellipticS, 1 coordinates p,v), which are related to the

    Cartesian coordinates

    xD YD

    by

    2.637

    x

    10

    4 kt

    - - - ~ - ~ - C - t X - f 2 - - - :

    27c)

    and

    Dimensionless Variables

    and

    Elliptical Coordinates.

    The situation is that

    of

    a vertical fracture. Flow is two

    dimensional. The axes are shown in Fig. 3 and the frac

    ture extends from f to xf along the x axis. We as

    sume .an isotropic reservoir and introduce

    XD =x/xf, 27a)

    YD =y/xf

    ;

    27b)

    sure in finite reservoirs in situations where it is known

    that such a steady-state solution exists. One case

    of

    in

    terest consists

    of

    an areally square reservoir

    of

    finite thick

    ness with a limited-flow-entry well in the middle

    of

    the

    square and a constant-pressure condition at the lateral

    boundaries. This situation arises in the calculation

    of

    the

    critical rate to water coiting first investigated by Muskat. 1

    The advantage

    of

    Eq.

    26 is that the infinite-conductivity

    condition is satisfied at the outset.

    An

    investigationof crit

    ical rates along these lines has been performed by

    Hoyland.

    6

    It

    is

    more

    surprisingthatEq

    26 more exactly , an

    asymptotic expansion obtained from Eq. 25 for large t

    D

    can be used to obtain an expression for the pseudoskin

    for a limited-flow-entry well in an areally infinite reser

    voir,with finite thickness. The applicability

    of

    Eq. 26 is

    not evident because dimensionless pressure is proportional

    to In

    tD

    for large

    tD

    in this case, whereas Eq. 26 is a

    steady-state expression. The method of images leads to

    the calculation

    of

    an infinite sum because infinitely many

    images are necessary to satisfy the no-flow boundary con

    ditions at the upper and lower boundaries, and the infinite

    sum turns out to be divergent. One must then identify this

    mathematical divergence with the physical divergence

    of

    pD, which is caused by In

    t D

    in the limit

    t D -+

    The

    geometrical skin is obtained as the finite

    e x ~ r e s s i o n

    that

    remains when the divergence is subtracted. Ref. 5 dis

    cusses the applicability

    of

    the method of images to the

    problem considered. Re[ 5 shows that the method de

    stroys the condition of strict uniformity of potential at the

    well, but that this condition applies to a good approxima

    tion for the majority

    of

    cases

    of

    interest.

    2d8

    iJ ;

    25)

    1

    D =lf

    In

    t .

    26)

    e

    -1

    Thus t/;w is determined, and so are the k by Eq. 23),

    which means that

    U

    is determined by Eq. 22. One finally

    obtains

    t

    see Appendix

    B :

    1

    = J

    t/;w

    k=O

    R

    k

    t/;w s

    -

    J; -

    ( ~ , a , s ) = w ( s )

    k=O

    Le., an expansion in terms

    of

    angular functions with an

    even second index. The function

    U

    will be determined

    as soon as the coefficients

    {

    k are known.

    Step 3. I t is now possible to solve Eqs.

    17

    and

    18

    to

    find

    t/;w

    and

    U.

    Substitution

    of

    Eqs. 19 and 22 into Eq.

    17

    gives the

    following relation between the coefficients

    { k

    and

    t

    w

    see Appendix

    B :

    Eqs. 24 and 25 constitute the solution

    tothe

    limited-flow

    entry problem. The solution is approximate

    if

    w

    is

    given

    a nonzero value, as noted above. For a line-source well,

    however, the solution is exact but must be obtained by

    letting w-+ 0, taking care of the fact that R i,J;, cosh

    w diverges when w-+0. 9 In practice, this can be done

    by inverting the Laplace transform Eq. 25) for a very

    small value

    of wand

    using an expansion for the func

    tion

    R ~ ~ 1 (i...{;,

    cosh

    w

    valid for small w.

    9

    This has

    not been attempted in the present paper for the reasons

    given in the Introduction. An analytical investigation

    of

    Eqs.

    24

    a nd 25 for small w and small

    s

    however, has

    been carried out in Ref. 5. One product

    of this investiga

    tion is the long-time approximation, obtained by invert

    ing term by term the small-s expansion

    of

    Eq. 25 10 and

    dropping terms that vanish when

    tD

    -+

    One finds that

    N 0 2 k R b ~ k i . j ; ,

    I R ~ i k i J ; , cosh w 23)

    Substitution

    of

    Eqs. 22 and 23 into Eq.

    18

    gives see Ap

    pendix

    B

    and

    Applications.

    Eq. 26 can now be used in conjunction

    with the method

    of

    images to get the steady-state pres-

    220

    Y

    D

    =

    sinh

    p

    sin

    v. .

    28b)

    SPE Reservoir Engineering, May 1987

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    y

    - - - - - : - - - - - - - - - - - - - - - - ~

    X

    Fig.

    3 Vertical

    fracture problem. Fracture Isalong Interval

    -x

    +x,)

    on x

    , axis

    thick line .

    The curves with p constant areellipses, while the curves

    with

    v

    constant are hyperbolas (see Fig. 4). The p= O el

    lipse has degenerated into Segment 1 +1 along the

    xD

    axis and thus represents the fracture. Coordinates

    p

    and v vary in the intervals 0 s p s 00 and 0 S vS

    2 r

    The dimensionless pressure, P

    D ,

    can now be written

    in terms of the unknown dimensionless flux at the frac

    ture,

    qjD

    (see Appendix A):

    r

    D

    r

    21r

    P D = J dt b J

    dv sin

    v qjD v ,tD)

    o

    0

    e [D

    /4 t

    tb ]

    X , (29) .

    tD tb

    where

    kh

    P D

    =

    4 2 ~ q

    P i p (30)

    and

    (31)

    In Eq. 30, h is the reservoir thickness. PjD t

    is the

    uniform dimensionless pressure at the fracture, then by

    setting p= O in Eq. 29, one obtains

    r

    t

    D r

    2

    PjD

    =

    J

    dt b

    J dv sin v qjD v ,tD)

    o 0

    e

    -[ cos p-cos pl 2 /4 t D tb ]

    X

    (32)

    tD tb

    SPE Reservoir Engineering, May 1987

    Fig. 4 Vertlcal fracture problem. Elliptical coordinates.

    With p constant, lines are ellipses labeled by the values

    of

    p

    and

    with

    constant, lines are branches

    of

    hyperbolas

    labeled by the values

    of

    v In degrees .

    Note that there is no difficulty in setting p =0 because

    pressure is known to be finite at a fracture of zero thick

    ness, so there is no limiting procedure involved here, as

    in the case

    of

    the line-source well. Eq. 32 is the first

    of

    two equations that

    qjD

    must satisfy; the second is (see

    Appendix A)

    r

    2

    J

    dv

    sin

    v qjD V ,tD)=1.

    (33)

    o

    Statement of

    the

    Problem; One must solve Eqs. 32 and

    33 for

    qjD

    and

    PjD

    Eq. 29 will then give the dimension

    less pressure. Introducing the notation

    [p D( P,v,tD)]

    =1/t p,v,s), (34)

    [PjD tD)] =

    1/tl

    s

    )

    , (35)

    and

    [qjD V,tD)]

    =

    V v,s), (36)

    one finds that the Laplace transforms

    of

    Eqs. 29, 32, and

    33 are

    r

    2

    t= J dv sin v

    V v

    ,s)K

    o

    .[;V (37)

    o

    r

    2

    1/tf=

    J dv sin

    v

    V v ,s)Ko .[;lcos v-cos v I),

    o

    (38)

    and

    rll dv sin

    v

    V v ,s)=1/s, (39)

    o

    221

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    whereK0 is the modified Bessel function of order

    O

    7

    The problem reduces now to solving Eqs. 38 and 39 for

    and

    V.

    will then be given by Eq. 37.

    Solution. As in the case of the limited-flow-entry well,

    an analytical solution is made possible 2Y the existence

    of an eigenfunction expansion of K0

    s

    D . Such an

    expansion is given in Ref. 8 for the Hankel function

    H0 1) . Using the relation

    7

    one obtains, when D is given by Eq. 31,

    where cem is the angular or periodic Mathieu function

    and Ie

    m

    and Ke

    m

    are radial Mathieu functions.

    7

    There

    is a normalization formula for the ce

    m

    functions analo

    gous to Eq. 20.

    7

    There is also an equation like Eq.

    21

    for the cem; it

    is written below to establish a notation that will be used

    later:

    00

    ce2m(V,q)= q cos 2nv (41)

    n=O

    The Laplace transform

    of

    the dimensionless flux at the

    fracture,

    V

    can beexpanded in a series

    of

    angular eigen

    functions cem An expansion that accounts for its J sym

    metry properties

    V

    is even about v=0,7r/2,7r,37r/2) is

    V(v,s)=

    Akce2k v , - ~ ; (42)

    m=O 4

    Le., an expansion in terms of

    ce

    functions, with an even

    index.

    It is now possible to solve Eqs.

    38

    and 39. The calcu

    lations are exactly analogous to the ones performed in the

    limited-flow-entry case, so only the final results are

    reported.

    The

    Ak S

    of

    Eq. 42 are given by

    2k

    1/Ils) Ao -s/4

    A k (43)

    , 1r

    Ie2k (0,s/4)Ke2k(0,s/4)

    where A has been defined in Eq. 41 and

    1 00 2 [ A ~ m

    -s/4)]

    2

    s

    L; ...... (44)

    I/Ils) ,

    m=O

    Ie2m(0,s/4)Ke2m(0,s/4)

    222

    Finally, the Laplace transform of th e dimensionless

    pressure is

    1 / I p , v ~ s = 1 / I t < s

    2 A ~ m ~

    m=O

    ,4

    Eq. 44 was presented by Kucuk and Brigham

    11

    with

    another notation for the Mathieu functions.

    Applications. The large

    tD

    approximation implied by

    Eq. 45, obtained by inverting its small s expansion term

    by term and dropping terms that vanish when

    t

    D -+ CXJ is

    PD = In

    e -

    2p t

    D

    +2

    In

    2- f

    (46)

    where I is Euler s constant (0.5772), so that2ln 2- 1/2=

    1.09769. Thus for p=O-Le., at the fracture : Kucuk and

    Brigham s 11 result is recovered.

    By assuming that the wellbore is situated at

    x

    D=Y

    D

    =

    and by denoting the well radius as r w, one can extract

    from Eq. 46 the following expression for the skin factor:

    2r

    w

    s ln

    p

    (47)

    XI

    where p can be obtained from Eqs. 28:

    [

    1

    r ~ [ l

    +rh)2

    -4rh

    cos

    2

    8]

    ]lh

    p=arc cosh

    2

    : (48)

    The notation and definition of the inverse hyperbolic func

    tion is that

    of

    Ref. 7, and rD and 8 are the usual polar

    coordinates.

    XD

    =rD

    cos 8 (49a)

    and

    YD=rD

    sin 8 (49b)

    Eq. 46 shows that

    tD/exp 2p ,is

    the proper combina

    tion against which to plot

    PD if

    one wants curves with

    different

    p

    values to collapse as much as possible into a

    unique curve. For larger

    rDi.

    Eq. 48 shows that exp(2p)

    is approximately equal to 4rD Eqs. 44 and 45 have been

    inverted with the Stehfest algorithm.

    12

    Fig. 5 is a plot

    ofpD vs.

    rD

    at a fixed angle 8 and a fixed

    time.tD,

    show

    ing that the condition of uniform pressure at the fracture

    (Le., for

    8=0)

    is satisfied. Table 1 gives PD vs. tD at

    the fracture

    (P=0 )

    for different value

    of

    the Stehfest in

    teger N. Note that

    N=6

    is acceptable for most practical

    purposes. There is some discrepancy between the values

    SPE Reservoir Engineering, May 1987

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    Fig. 5 Vertlcal fracture problem; Po VB. the polar coor

    dinate, r

    for three values

    of

    the polar angle, 8. Note uni

    form pressure at the fracture 8=0).

    omenclature

    a

    =

    half-length of interval open to flow,

    ft

    [m]

    A ;: =

    constant in Eq. 41

    ce

    m

    =

    periodic Mathieu function

    7

    c

    t

    =

    total reservoir compressibility, psi

    [kPa ]

    d r

    ) =

    expansion coefficient in Eq.

    21

    ~ e x p - 2 p

    D =

    constant defined in Eq. 31,

    dimensionless

    h

    =

    reservoir thickness, ft [m]

    = Hankel function

    7

    ~

    Iem =

    Mathieu function

    7

    k =

    permeability, md

    kH:k v =

    horizontal and vertical permeabilities,

    md

    Ke

    m

    =

    Mathieu function

    7

    K

    0 =

    modified Bessel function

    7

    f =

    Laplace transform

    of

    function f

    Fig. 6 Vertlcal fracture problem;

    Po VB. t

    o

    /exp 2p). The

    elliptic angular coordinate v is

    45

    TABLE p0

    VS

    to

    AT THE FRACTURE p =0 FOR

    DIFFERENT VALUES OF THE STEHFEST PARAMETER, N

    Pressure

    Time

    N=6 N=8 N=

    Asymptotic

    *

    .01 0.1698

    0.1697

    0.1699

    -

    0.02 0.2359

    0.2358 0.2357

    -

    0.04

    0.3256 0.3253 0.3253

    -

    0.06 0.3914 0.3911

    0 39fo

    -0.08

    0.4450

    0.4446 0.4446

    -

    0.10 0.4909 0.4904

    0.4904

    -

    0.20 0.6592

    0.6585

    0.6589

    -

    0.40

    0.8693 0.8684

    0.8684

    -

    0.60

    1.0115 1.0105

    1.0105

    0.8423

    0.80

    1.1204 1.1194

    1.1194

    0.9861

    1.00 1.2091

    1.2081 1.2082 1.0977

    2.00

    1.5045

    1.5036 1.5037 1.4443

    4.00

    1.8222

    1.8215 1.8216

    1.7908

    6.00

    2.0148

    2.0142 2.0143

    1.9936

    8.00

    2.1536 2.1529 2.1530

    2.1374

    10.00

    2.2620 2.2614

    2.2615

    2.2490

    20.00

    2.6023 2.6017

    2.6018 2.5956

    40.00

    2.9458 2.9452 2.9452 2.9421

    60.00

    3.1475 3.1469 3.1469 3.1449

    80.00

    3.2908 3.2902

    3.2903

    3.2887

    100.00 3.4021 3.4014 3.4015 3.4003

    200.00

    3.7480

    3.7474 3.7475 3.7468

    400.00

    4.0943

    4.0936 4.0937 4.0934

    600.00

    4.2969

    4.2963

    4.2963

    4.2962

    800.00 4.4407

    4.4401

    4.4401

    4.4400

    1,000.00

    4.5522 4.5516

    4.5517 4.5516

    2,000.00 4.8987 4.8981

    4.8982 4.8981

    4,000.00

    5.2453

    5.2447

    5.2447

    5.2447

    6,000.00

    5.4480 5.4474

    5.4475

    5.4474

    8,000.00

    5.5918 5.5912

    5.5913 5.5913

    Obtained from

    Eq. 48.

    3

    e =

    0

    e

    =

    71 4

    e =

    71 2

    2

    =

    1 0

    1

    5

    1

    onclusions

    New theoretical results concerning infinite-conductivity

    wells have been presented in the form

    of

    Laplace trans

    forms. Some implications

    of

    the result for the limited

    flow-entry problemhave been discussed in general terms.

    Detailed calculations are presented elsewhere.

    5

    ,6 Results

    of

    the inversion

    of

    the Laplace transform have been

    presented for the vertical fracture problem. There are

    some discrepancies with earlier results,4 amounting at

    worst to 4 . These discrepancies are difficult to account

    for because they occur between calculations that are very

    different from each other, but are mild and will not intro

    duce any detectable uncertainty in a type-curve analysis.

    The inversion

    of

    the Laplace transform

    of

    Eq. 45 is fast

    enough to allow the plotting

    of

    type curves directly on

    a screen by an interactive computer-graphics program

    without long waiting periods. Eq. 46 is new and agrees

    with that obtained by Kucuk and Brigham when p

    = O

    1.209

    shown in Table 1 and those

    of

    Gringarten

    et ai

    4

    on

    the

    order of 4 for small times and decreasing to about 0.1

    toward the bottom

    of

    the table. Fig. 6 shows

    P

    D

    vs.

    tD/exp 2p)

    for a range

    of p

    values, the value

    of p

    being

    the same. The curves are drawn by linear interpolation

    between the calculated points, which are equidistant and

    have a density

    of

    6/log cycle. Depending on the work

    load, the calculation of the set

    of

    points needed to draw

    one curve takes from 10 to

    20

    seconds a high-performance

    32-bit minimachine.

    Eq. 46 is represented by the dashed line in Fig. 6. Ta

    ble 1 and.Fig. 6 show that the difference between the log

    approximation Eq. 46 and the exact value is less than

    about 2 when

    tD >4

    SPE Reservoir Engineering,

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    1987

    223

  • 8/10/2019 22. SPE-13846-PA

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    N = positive integer

    Non ; normalIzing constant in Eq. 20

    p = reservoir pressure, psi [kPa]

    pD = dimensionless pressure (see Eq. 30)

    PfD = PD at the fracture

    Pi

    =

    initial pressure

    Pm = Legendre polynomial

    7

    (see Eq. 22)

    q

    =

    real number (see Eq. 41)

    qfD

    =

    dimensionless flux at the fracture (see

    Eqs. 29 and A-12 through A-14)

    qt =

    ,total well volumetric flow rate, RB/D

    [res m

    3

    /d]

    q wD

    = dimensionless flux at the. well (Eqs. 6

    and A-5 through A-7) ,

    q x,y,t = volume of oil withdrawn at point x,y

    and at time

    t

    per unit reservoir

    volume and unit time, RB/D-ft3

    [hours 1 ]

    q x,y,z,t

    =

    volume of oil withdrawn at point x,y,z

    and at time t per unit reservoir

    volume and unit time, RB/D-ft3

    [hours 1]

    r

    D = d i m e ~ s i o n l e s s radial coordinate

    (see Eq. 5)

    r

    w =

    well radius, ft [m]

    R = constant equal to

    rB

    + ZD Zb 2 (see

    Eq. 8), dimensionless

    R

    1

    = radial spheroidal function of the first

    mn

    kind

    7

    ,9

    R = radial spheroidal function of the third

    kind

    7

    ,9

    R

    w

    = R with ~ ~ (see Eq. 10),

    dimensionless

    s

    =

    Laplace parameter, dimensionless

    Smn

    = angular spheroidal function7,9

    t =

    time, hours

    tD = dimensionless time

    U = Laplace transform of

    qw D

    V = Laplace transform of

    qjD

    x,y,z

    =

    Cartesian coordinates, ft [m]

    XD,YD,ZD

    =

    dimensionless Cartesian coordinates

    xi =

    fracture half-length in the x direction,

    ft [m]

    Z = complex variabl,e

    a 3 = angular spheroidal coordinates

    (see Eqs. 4)

    3 k

    =

    coefficient in Eq. 22

    Y = Euler s constant (0.5772)

    oij = Kronecker delta, 1

    if

    i=j 0 otherwise

    8

    =

    angular polar coordinate (see ~ q s 49)

    Ak = constant defined in Eq. 43

    p

    =

    oil viscosity, cp [Pa

    s]

    v

    =

    elliptic angular coordinate (see Eqs. 28)

    = radial spheroidal coordinate (see, Eqs. 4

    =

    at th e well

    p = elliptic radial coordinate (see Eqs. 28),

    dimensionless

    Po = oil mass per unit volume, lbm/ft

    3

    [kg/m

    3

    ] .

    224

    J

    = i.J;

    (see Appendix B) .

    7 =

    real number

    = porosity, fraction

    4> = potential (see Eq. 3), psi [kPa]

    4>

    D

    dimensionless potential (see Eq.

    7)

    eJ>i =

    initial value

    of 4>

    psi [kPa]

    cI

    wD = 4> D at the well (see Eq. 9)

    ;

    =

    Laplace transform

    of

    4>

    D

    in low-flow

    entry problems and

    of

    PD in infinite

    conductivity vertical fracture

    problems

    ;

    f =

    ; at the fracture

    ;w

    =

    ; at = w Laplace transform

    of

    4> wD

    Subscripts

    j k m n = integers

    Superscripts

    , =

    integration variable

    cknowledgments

    I

    gratefully acknowledge the financial support

    of

    Norsk

    Hydro and express my thanks to Leif Larsen for much

    useful advice.

    References

    1 Muskat,M.: Physical Principles

    of

    Oil Production, Inti. Human

    Resources Development Corp., Boston (1981) 209.

    2. Gringarten, A.C. and Ramey, H.J. Jr. : The Use of Source and

    Green s Functions in Solving Unsteady-Flow Problems in

    Reservoirs, SPEJ (Oct. 1973) 285-96; Trans. AIME, 255.

    3. Gringarten, A.C. and Ramey, H.J. Jr.: An Approximate Infinite

    Conductivity Solution for a Partially PenetratingLine-SourceWell,

    SPEJ (April 1975) 140-48; Trans. AIME, 259.

    4. Gringarten, A.C., Ramey, H.J. Jr., and Raghavan, R.: Unsteady

    State PressureDistributions Createdby aWellWith a Single Infinite

    Conductivity Vertical Fracture, SPE/ (Aug. 1974)

    347 60;

    Trans

    AIME,257.

    S Papatzacos, P.: Approximate Partial-Penetration Pseudoskin for

    Infinite-Conductivity

    Wells,

    SPERE (May 1987) 227-34.

    6. Hoyland, L.A.: Critical Rate for Water Coning in Isotropic and

    Anisotropic Formations,

    Cando

    Tekn. thesis, Rogaland Regional

    C., Stavanger, Norway (1984).

    7. Abramowitz , M. and Stegun, I .A.: Handbook of Mathematical

    Functions

    Dover Publishing Inc., New York City (1972).

    8. Morse, P.M. and Feshbach, H.: Methods of

    Theoretical Physics

    McGraw-Hill Book Co. Inc., New York City (1953).

    9. Flammer, C.:

    Spheroidal

    Wave

    Functions

    Stanford U. Press,

    Stanford, CA (1957).

    10. Carslaw, H.S. and Jaeger, J.C.: Conduction of Heat in Solids;

    Oxford Book Co., New York City (1959).

    11. Brigham, W.E. and Kucuk, F .: T r a n s i ~ n t Flow in Elliptical

    Systems,

    SPE/

    (Dec.1979) 401-10;

    Trans.

    AIME, 267.

    12. Stehfest, H.: Numerical Inversion of the Laplace Transforms,

    Cori1nutn ications

    of

    the ACM

    (Jan. 1970) 13,

    No.1,

    Algorithm368.

    13. Williams, W.E.: Partial Differential Equations Clarendon Press,

    Oxford (1980).

    ppendix FlowEquat ons

    Flow Equation and Flux for the Limited-Flow-Entry

    Problem. Equations in this Appendix are written in con

    sistent units, and conversion constants are indicated when

    necessary. The diffusion equation with a source term is

    kH il

    2

    + il

    2

    } + 0

    2

    _

    cPp c

    >

    k

    v

    ox

    2

    oy oz k

    v

    ot

    P

    =--q x,y,z, t ,

    (A-I)

    k

    v

    SPE Reservoir Engineering, May 1987

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    where q(x,y,z,t) is the volumetric rate of oil withdrawn

    at Point (x,y,z,t) per uni t r ese rv oi r volume. I n ot her

    w o r ~ s ,

    lq(x,y,z,t)dxdydz=

    -q ,

    A-2)

    where

    q t

    is the total volumetric flow rate of the well. In

    tegration in Eq. A-2 can be extendedto the whole of space

    because

    q

    wil l be different from zero only at the well.

    By introduction

    of

    dimensionless coordinates Eq. 1),

    dimensionless time Eq. 2), and dimensionless potential

    Eq. 7), Eqs.

    A-I

    a nd A -2 b ec om e

    a

    2

    cpD a

    2

    cpD a

    2

    cpD _ acpD =27ra

    kH

    i

    aXE

    aYE aZE

    atD k

    v

    t

    A-3),

    and

    r

    k

    v

    qt

    j q ~ x D Y D , Z D , t D d x D d Y D d z D= - 3 A-4)

    ,

    kHa

    To find a general expression for the function q describ

    ing a line-source well as shown in F ig.

    1

    it is convenient

    to use the so-called Dirac delta function,

    O x .13

    Here,

    beca use the well i s along t he z axis, on e may wr ite

    k

    v

    qt

    q(XD,YD,ZD,tD)=

    -3 0(XD)O(YD)qwD(ZD,tD),

    kHa

    . . . . . . . . . . . . . . . . . . . . . . . . . A-5)

    where, on the rjght side, the constants are included for

    convenience, and where the unknown function, qwD is

    the dimensionless flux along the well. When qt and

    a

    are

    expressed in customary units, the factor 1.539 X 10

    4

    must

    be included on the r ight side. T he units f or q are then

    RB/D-ft

    3

    .

    Function

    q

    wD i s such that

    qwD(ZD,tD)=O,

    IZDI >

    1 A-6)

    and

    +1

    J

    qwD(ZV,tD)dzv=1.

    A-7)

    1

    E q. A -7 r es ul ts f rom t he co mbi na ti on of Eqs. A-4 and

    A-5. By using Eqs. A-3 and A-5, one obtains

    a

    2

    D

    a

    2

    CPD a

    2

    CPD OCPD

    aXE aYE aZE

    OtD

    Eq. A 8 can

    now be solved with the help of the known

    Green function

    3,8

    to give the dimensionless potential D :

    CPD(XD,yD,ZD,tD)= dtb J

    1

    dzbqwD(Zb,tb)

    o -1

    1 [ -XE -yE -(ZD -ZV)2]

    x = exp

    .

    4J;(tD -tv) 4(tD tv

    A-9)

    SPE Reservoir Engineering, May 1987

    To

    recoverEq.

    6, it suffices to introduce the prolate

    spheroidal coordinates given by Eq.

    4

    and to use zb

    =cos

    a

    E q. A -9 t he n gi ve s E qs .

    6,

    a nd E q. A-7 gives E q.

    9.

    Flow Equation. and Flux for the Vertical-Fracture

    Problem. The equations analogous to Eqs. A-3 and A-4

    a re e asi ly found t o be

    and

    The flux

    q

    at the fracture can be expressed in terms of

    a delta function expressing

    the

    fact that the fracture is an

    infinitely thin sheet and an unknown dimensionless flux

    at the fracture, qfD:

    When

    qt

    h, and

    x

    are expressed in field units, then

    the factor 1.539

    X

    10

    4

    must be included on the right side.

    T he uni ts f or q are then RB/D-ft

    3

    . Function qjD must

    satisfy the following conditions:

    qjD(XD,tD)=O when

    IXDI >

    1 .

    ,

    A-13)

    and

    +1

    J

    qfD(xb,tD)dx

    v

    =

    1

    A-14)

    1

    T he dif fer enti al e qua ti on f or PD E q. A-IO) then

    becomes

    A-15)

    and has the solution

    Using Eqs. 28 together with

    xb =cos u

    in Eqs. A-14

    and

    A-I6

    yields Eqs. 29 and 33.

    225

  • 8/10/2019 22. SPE-13846-PA

    10/10

    ppendix

    B Proof

    of Equations

    Fo r simplicity, the notation u=i.Jiwill be used through

    out this Appendix.

    Proof of Eq . 23.Substitution

    of

    Eqs. 19 and 22 into Eq.

    16 gives

    x [ ~

    _1_

    S k

    u, cos a )Sok U, cos a ) R ~ u , l )

    k k

    X R ~ J u , cosh

    where the terms involved by the a/integration have been

    underlined. This integration can be performed with the

    help

    of

    Eq. 20, giving

    X r l ~ u,

    I R ~ 1

    u, cosh . B-1)

    One first sets

    w

    the left side thus becoming the

    a-independent function w see Eq. 17). Both sides of

    the equation are then multiplied by sin a S02j U, cos a da

    and integrated from 0 to 7 by use of Eq.

    20 .

    Eq. 23

    emerges if, in addition, one uses

    J I da

    sin a

    S02k U,

    cos

    a =2d

    o

    k

    u , B-2)

    o

    which follows easily from Eq.

    21

    and from known prop

    erties

    of

    the Legendre polynomials.

    8

    Proof ofEq. 24, When one makes use of Eq. B-2, sub-

    stitution

    of

    the right side

    of

    Eq. 22 into Eq. 18 yields

    When the right side of

    Eq.

    23 is substituted for the

    k,

    one obtains Eq. 24.

    Proof of

    Eq . 25. Eq.

    25

    is obtained immediately when

    one uses Eq.

    23

    o r t ~

    k

    in Eq. B-1.

    Metric onversion Factor

    degrees X 1.745 329

    E -0 2

    rad

    SPERE

    Original manuscript

    SPE

    13846 received

    in

    the Societyof Petroleum Engineers office

    Dec. 3,

    1984. aper accepted for publication Feb.

    6,

    1986. Revised manuscript

    re-

    ceived Jan. 24,

    1986.