Part 15 Slug Dst Mdt Iptt

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    Slug DST WFT MDT - WTA

    Cha ter 15Slug, DST, and MDT Tests

    DST DST (Drillstem Test) has been used as a method of

    formation evaluation for many years.

    Originally used to identify reservoir fluids, DST hasalso become an important method for estimatingreservoir pressure and well potential.

    It can berunboth in o enand cased holeswithasingle packer or a dual (or straddle) packer.

    DST can be viewed as a temporary well completionwith the purpose of obtaining some or all of thefollowing objectives:

    Identification of reservoir fluid An indication of well productivity Pressure transient data to estimate permeability, skin

    factor, and static reservoir pressure.

    DST Tool

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    DST Pressure Response

    A Note on DST Analysis

    DSTs in which fluid is produced to surface (higherproductivity wells) can be analyzed like any othertransient tests semilog plots, pressure andderivative type curves etc.

    DSTs in which fluid is not produced to the surface

    discussed later.

    One important point to note is that DST tests areexamples of variable rate testing problems becausesandface flow rate changes in flow and buildupperiods, and flow rate measurements are often notavailable, and must be inferred from pressure data.

    Flow Rate/Pressure RateBehavior

    Flow periods of DST are

    examples of Slug Tests,

    if the fluid is not produced

    to surface.

    3 cycle DST

    Buildup periods are

    Examples of buildup tests.

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    Flow Rate/Pressure Rate Behavior

    As is seen from the previous slide, flow rateduring the flow periods are variable, in fact

    usually decreases with time. The time rate ofdecrease in flow rate is a strong function ofskin factor and permeability. In cases, if

    ,flow rate is almost constant.

    As mentioned previously, flow rate duringDST tests are not usually measured. In casesit is measured or estimated, then we cananalyze these tests by using variable ratemethods; convolution, deconvolution, etc.

    Flow Periods As noted previously, pressure increases

    during the flow periods of DST. Why does thishappen?

    Flow period is an example of wellbore storagedue to rising of fluid in drill pipe.

    t1

    pwf1

    t2

    pwf2

    pwf2 > pwf1

    =

    615.5

    144 cF

    AC

    2

    pc rA =

    density of the fluidin drill pipe.

    Estimation of Flow Rate

    In cases flow rates are not measured, wecould compute flow rate from the amoun oftotal fluid produced or from measuredpressures, assuming constant wellborestorage coefficient by using the following

    formula:

    Or using a piecewise constant pressureapproximation for the measured pressuredata.

    =

    1

    1)()(2424)(

    jj

    jwfjwf

    F

    t

    wf

    Fjsftt

    tptpC

    dt

    dpCtq

    j

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    Estimation of Flow Rate

    2

    )()( 1+= jwfjwfj

    tptpp

    An Examplew =/144

    = 0.325 psi/ft

    Vu = 0.007 bbl/ft

    CF = Vuw=0.0215 bbl/psi

    qavg = 91.05 bbl/D

    (for one-hour

    flow period)

    Taken from Bourdets book Well Test Analysis: The Use of Advanced Interpretation Models.

    An Example

    ( ) 00

    2424

    4900.73 4724.5124 0.0215 91 /

    1

    pt

    wf pwfFavg F

    p p

    p t pdpCq dt C

    t dt t

    bbl D

    = =

    = =

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    Slug Test Type Curve

    Ramey has developed type curves for analyzing flow periods of DSTs, not requiring

    the knowledge of flow rate data.

    Dimensionless Pressure

    0

    )(

    pp

    tpppp

    i

    wfi

    DRwD

    ==

    0

    0)(11

    pp

    ptppp

    i

    wf

    DRwD

    ==

    Dimensionless Time

    tC

    kh

    C

    t

    FD

    D

    = 000295.0( )

    ( )DDF

    t

    CtCkh

    =

    /

    000295.0

    Rameys Slug Test Type Curve

    Use of Rameys Type Curve Data is matced only sliding in the time axis

    horizontally.

    From time match points determined, we can

    obtain kh/ with the estimated value of CFfrom: From the value of CDe2s curve matched, we

    can estimate skin factor:

    ( )( )

    /

    0.000295

    D DF M

    M

    t Ckh C

    t=

    22

    615.5

    wt

    FD

    hrc

    CC

    =

    ( )21ln

    2

    S

    D M

    D

    C es

    C

    =

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    An Example

    An Example

    k= 41.7 md

    s = 6.5

    Relationship Between Slug andConstant Surface Rate Solutions

    In 1989, Peres et al. (SPE 19843) showedthat slug test data could be converted todata that would be obtined if the well

    produced at a constant surface rate.

    )()(

    000295.0

    0

    s

    iF

    cwD pIkh

    ppCp

    =

    ( )siF

    cwD ptkh

    ppCp

    =

    )(

    000295.0

    0

    ( ) = dptpIt

    ss

    0

    ))((

    )()( tpptp wfis =

    Peres et al. method is valid any model; fractured well, etc.

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    We can use numerical integration to

    perform the conversion:t

    Relationship Between Slug andConstant Surface Rate Solutions

    = ptp ss0

    Trapezoidal rule

    ( ) =

    =

    +

    =

    n

    j

    jj

    jsjsn

    j

    t

    t

    sns tttptp

    dptpI

    j

    j1

    1

    1

    1

    )(2

    )()())((

    1

    Slug ve Sabit Yzey Debili Testlikisi

    Then, we can type curve match I(ps) andtps vs t with the wellbore storage typecurves for constant-rate drawdown tests.

    Relationship Between Slug andConstant Surface Rate Solutions

    ( )( )

    M

    MDDF

    t

    CtCkh /

    000295.0=

    ( )

    =

    D

    M

    s

    D

    C

    eCs

    2

    ln2

    12

    2

    615.5

    wt

    FD

    hrc

    CC

    =

    From Derivative and/or Time Match Points:

    From the curve matched value of CDe(2s):

    ( )( )

    s

    McwDiF

    pt

    pppCkh

    =

    000295.0

    )( 0

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    Example Test 1kh/ = 197 md-ft/cp,s = 0, test during underbalance perforationtest: CF = Vwcwf , cwf = 7.3x10

    -6 1/psi, Vw = 331 bbl,ct = 23x10-6

    1/psi, = 0.41 cp,h = 39.37 ft

    Example Test 2kh/= 575, s = -2.3, = 60 cp, h = 38 ft, = 0.062, ct = 10.2x10-6

    1/psi, CF = 3.65x10-2bbl/psi

    Example Test 3kh/= 21.5, s = -1.5, = 0.43 cp, h = 23 ft, = 0.13, ct = 1.5x10-5

    1/psi, CF = 1.61x10-2bbl/psi

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    Slug Test Semi-log Analysis

    We can perform semilog analysis of slug test datausing convolution or superposition time

    Slope = m

    [ ] +

    +=

    src

    tkhptp wt

    msF

    wf

    s 87.023.3log000295.0

    .

    )(2

    0

    ( )

    =

    =

    0

    1

    1

    1)(

    )()(log

    ptp

    tptpttt

    nwf

    jwfjwfn

    j

    jnms

    ( )[ ]

    +

    = 23.3log

    )/(15.1

    2

    *0*

    wt

    ms

    twfs

    rc

    kt

    m

    pppIs ms

    Slug Test Semi-log Analysis

    Then, make

    ( )ms

    s tvst

    tpI.

    )(

    plot

    ( )[ ]

    +

    = 23.3log)/(

    15.12

    *0*

    wt

    ms

    twfs

    rc

    kt

    m

    pppIs ms

    m

    Ckh

    kh

    Cm FF

    000295.0

    151.1

    000295.0

    151.1==

    Note

    It should be noted that Surge, Perforation inflow,and Impulse Tests are all examples of Slug tests,and can be anayzed by the methods discussed for

    slu tests. Rahman et al. (JCPT, 2008) uses a late-time

    equation given by:

    He also gives early time approximations which canbe used to determine skin.

    ( ) ( ) ( )tkh

    ppCptp iFiwf

    =

    1

    2

    2.141*24)( 0

    His late-time analysis procedure is OK if radial flow exits .

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    Example TestFrom semi-log analysis we found: kh/ = 21.1, s = -1.2From type-curve matching: we found kh / = 21.5, s = -1.5

    t*ms

    DST Buildup Period Buildup pressure data can be analyzed by

    conventional methods based onsuperposition time function if the rates can

    be computed.

    different from the flow period.

    wfwS cVC =

    Volume between shut-in valve

    And production zone, bbl

    compressibility of the fluid,

    1/psi

    Classical Horner Analysis For DSTBuildup

    We can use an average flow rate from theslug period:

    +=

    t

    ttmptp

    p

    iws log)(

    (( )/

    6.162

    kh

    qm

    averagesf= ( )

    =

    p

    pwf

    Faveragesf t

    ptpCq

    0)(24

    +

    = 23.3log151.1

    2

    wt

    porti

    rc

    kt

    m

    pps

    2

    )(0 pwfort

    tppp

    +=

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    Convolution for DST Buildup We will use the flow rate computed priorto shut-in:

    Once flow rates are calculated, we can use them to

    compute Agarwal multi-rate equivalent time:

    Nbj

    =

    +

    =

    j jp

    jp

    eMttt

    tt1 1

    1

    Nsf

    jsfjsf

    jq

    qqb

    ,

    1,, =

    Convolution for DST Buildup

    If we identify radial flow regime from log-logdiagnostic plot of buildup data, then we canperform semilog analysis of buildup data:

    +

    =N

    jpjsfpsf tttqtq 1,)(6.162

    = +j jppsfiws

    ttttqkh 1 )(

    H

    psfpsf

    Hm

    tqkh

    kh

    tqm

    )(6.162)(6.162=

    =

    ( )

    +

    +

    +

    +

    = =

    N

    j wtjp

    jp

    psf

    jsfjsf

    H

    pwfhr

    rc

    k

    tt

    tt

    tq

    qq

    m

    tpp

    s 1 21

    11,,1

    23.3log

    1

    log)(

    )(

    151.1

    DST Buildup ExampleLog-Log plot based on Agarwal Multi-rate

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    DST Kapama Dnemi/rnek

    Klasik Horner grafii

    kh/ = 1309 md-ft/cps = 3.3

    DST Buildup ExampleHorner Plot

    kh/ = 1031 md-ft/cps = 0.8

    Wireline Formation Testers They are used as an alternative to RFT and DST

    tests. They are used to

    Obtain formation fluid samples and pressureprofiling along the wellbore to determine fluidcontacts.

    vertical interference (or in general intervaltransient tests) at distinct points along thewellbore.

    Determine permeability barriers andsuperpermeability streaks along the wellbore

    Determine horizontal and vertical perms (andalso their distributions) along the wellbore.

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    Wireline Formation Testers

    The radius of investigation of these

    tests are normally smaller thanconventional well tests and DSTs, butlarger than cores and logs.

    Their radius of investigation is withintens of feet radially and verticallyalong the wellbore.

    Wireline Formation Testers

    Wireline Formation TestersOverbalance case (pretest)

    Sink

    Total produced fluid is around 5 to 20 cm3 during pretest drawdown.

    formasyon ressure

    2900 psi

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    Wireline Formation Testers

    fz

    p=

    433.0

    Fluid density

    Wireline Formation Testersq = 40 cm3/sec

    Sink

    H

    V1

    Spherical flow

    Wireline Formation Testers

    Sink

    SinkHorizontal

    V probezp

    Spherical flow

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    Wireline Formation Testers

    )(

    4.38

    =

    vp

    h

    pz

    q

    k

    Slope = ms = 1.51 psi-sec1/2

    q (cm3/sec)

    =82.9vh qkk

    2

    )(

    )(3.15

    =

    v

    h

    p

    w

    v

    h

    p

    p

    z

    r

    k

    k

    2

    2

    )(71064.6 wts

    hh rcm

    pk

    =

    hw pr

    Packer-Probe Tests

    Tests performed with such aconfiguration benefit from the largevolume that can be sampled by thepacker, especially when using apumpout assembly for an extendedtest.

    Their radius of investigation is morethan probe tests.

    Both packer and probe responses canprovide estimates of kh, k v, and skinprovided that storativity (ct) is known.