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  • 7/21/2019 Pore Carbonate Properties

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    SPWLA 52nd

    Annual Logging Symposium, May 14-19, 2011

    BASIC LOGS UNLOCK COMPLEX CARBONATE PORE PROPERTIES

    Stefan Calvert,BG Group PLCand Gene Ballay,Independent Consultant

    Copyright 2011, held jointly by the Society of Petrophysicists and Well Log

    Analysts (SPWLA) and the submitting authors.

    This paper was prepared for presentation at the SPWLA 52 ndAnnual LoggingSymposium held in Colorado Springs, Colorado, United States, May 14-19,

    2011.

    ABSTRACT

    Many carbonate fields exhibit a high degree of

    heterogeneity and structural complexity leading to

    challenges in understanding the production performance.

    In many cases only triple combo data is available due to

    cost and/or operational considerations.

    It is generally recognised that an understanding of the

    complex micritic pore structure properties of carbonates

    is essential to the development of an understanding of

    formation properties that impact on production; such as

    the effective (flowing) porosity, water saturation either

    from resistivity logs and/or saturation height functions,

    permeability, relative permeability, wettability and

    recovery factors.

    Carbonate rock typing from logging data is generally

    considered to lie within the realms of NMR and image

    log analysis that is calibrated to core data. The

    characterisation of the different porosity types present in

    carbonates are driven by pore size variation (micro,

    meso and macro) which have wide variations in poro-

    perm characteristics for samples with the same total

    porosity. Similarly, the complex and heterogeneous pore

    structures can result in associated problems quantifying

    hydrocarbon saturations due to non-Archie resistivity

    water saturation relationships.

    The application of the Thomeer technique has provided

    insights and better production estimates. Integration of

    core derived Thomeer parameters with basic logs has

    delivered a robust and readily implementable reservoir

    property framework. The density-neutron logs canprovide a direct measure of threshold entry pressure thus

    allowing simple and reliable rock typing using the basic

    logging suite. The resultant rock typing significantly

    improved the formation evaluation description for the

    full field reservoir modelling.

    INTRODUCTION

    In many cases the data available to examine field

    heterogeneity is limited to only triple combo data due to

    cost and/or operational considerations. Core data

    therefore is especially valuable to investigate the

    possible explanations.

    An understanding of the complex micritic pore structureproperties of carbonates was found to be key to the

    describing the formation properties that impacted on

    production. The study field undertook a petrophysical

    re-evaluation based on several factors:

    Discrepancies between the fluid distributions based

    on the reservoir model predictions and production

    volumes implying that the in place volumes and

    production characteristics were not understood.

    Realisation that textural variations and fractures

    within the carbonate formations were prolific and

    should be captured in the petrophysical model.

    Poor agreement between log and core data.

    Geology

    The study field consist of three main units: Alternates,

    that rapidly alternate from limestone to shale. The A

    zone, a tight limestone and shale unit forms ephemeral

    local seals for the B zone. The B zone is 50m thick with

    excellent continuity and quality. The top 10-15m of B

    unit contains the best reservoir rock. The A zone is

    ~50m thick and comprises 10m zone of tight limestone

    with thin marl/shale beds, overlain by moderate quality

    limestone reservoir. The tight zone acts as a local

    baffle between the gas cap primarily in A zone, and the

    oil column which largely resides in the B zone.

    The oil column is approximately 20m thick (xx37-

    xx57m TVDSS) with a gas cap and a 40-60m water leg.

    The gas column is typically 50m thick, but locally

    exceeds 130m. The free water level is at xx62m

    TVDSS.

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    THOMEER MODEL

    Thomeer (1960) introduced a pore geometrical factor to

    assist the description of saturation-height as defined by

    capillary pressure curves. The premise being that

    reservoir quality is driven by rock fabric and thereforesaturation-height function must reflect the rock fabric.

    Thomeers method (1960) is based on fitting hyperbola

    to the logarithm of capillary pressure (Pc) and bulk

    volume occupied (BV = !T* Sw, !T= total porosity andSw= water saturation):

    [log(BV/BV")] * [log(Pc/Pd)] = log(e-G)

    (BV/BV") = e-G*[log(Pc/Pd)]

    where Pd is the threshold capillary pressure, BV" is the

    bulk volume at infinite pressure (close to !T) and G is

    the Thomeer pore geometrical factor.

    The advantages of Thomeers formulation are:

    Independent from permeability, K

    Can be superimposed for multiple pore volumes

    Texturally representative

    Facies are separable

    Permeability, K and irreducible water saturation,

    Swircan be predicted as follows

    Swir= [eG*log(Pd_macro)

    ] / !T

    where Pd_macro is the threshold capillary pressure of themacro pores. Permeability, K can be calculated using the

    Thomeer (1983) or Clerke (2008) methods respectively:

    KThomeer= 3.8068 * (BV"_macro/Pd_macro)2* G-1.3334

    KEd_Clerke= 10(a + b * log(214/P

    d_macro) + c *

    !

    T)

    where a, b and c are the appropriate fitting constants.

    Micritic Carbonates

    Micritic carbonates typically consist of two or three

    separable pore volumes related to the pore size; micro

    (5!m). The

    Thomeer model is most effective when hyperbolae are

    superimposed therefore each pore size can be fitted and

    summed to describe the whole pore system:

    BVT= BVmacro+ BVmeso+ BVmicroBVi= 10^{-Gi*(log(BV"_i)+[log(Pc)-log(Pd_i)]}

    where i is micro, meso and macro respectively.

    POROSITY AND SHALE VOLUME

    The density-neutron crossplot was used to compute

    shale volume, Vsh, assuming linear response equations:

    ( )( )

    ( )( )

    ( )( )

    ( )( )!

    !"

    #

    $$%

    &

    '

    ''

    '

    '

    !!"

    #

    $$%

    &'

    '''

    '

    =

    LimeWater

    LimeKao

    LimeNWaterN

    LimeNKaoN

    LimeWater

    Lime

    LimeNWaterN

    LimeNN

    shV

    ((

    ((

    ))

    ))

    ((

    ((

    ))

    ))

    __

    __

    __

    _

    where !N= neutron porosity, !N_Lime= limestone neutron

    porosity, !N_Water = water neutron porosity, !N_Kao =

    kaolinite neutron porosity, " = bulk density, "Lime =

    limestone bulk density, "Water= water bulk density, "kao

    = kaolinite bulk density. Note that XRD data shows the

    shale is almost entirely kaolintie in the form of dickite.The fluid parameters were fixed to that of the formation

    water ("water=!N_water=1) that provided an excellent match

    with XRD data even within the hydrocarbon intervals

    and provided a stable solution within the inversion.

    The volumes of limestone, Vlime, dolomite, Vdolo, and,

    effective porosity, !e were calculated using a material

    balance matrix inversion method:

    !!!

    "

    #

    $$$

    %

    &

    '

    ('

    ('

    =

    !!!

    "

    #

    $$$

    %

    &

    (((

    (((

    sh

    kaoNshN

    kaosh

    doloee

    doloNdoloeNeflNe

    dolodoloeefle

    V

    V

    V

    VV

    VV

    VV

    1

    _

    lim

    _lim_lim_

    limlim

    ))

    **

    )

    ))))

    ***)

    ( )( )

    ( )( ) !

    !"

    #

    $$%

    &

    '

    '+

    '

    '(=

    waterNkaoN

    claydryNkaoN

    waterkao

    claydrykao

    Sh

    __

    ____2

    3

    1

    ))

    ))

    **

    **)

    ShSheT V !!! "+=

    where limestone, dolomite, kaolinite and dry clay

    density are "lime, "dolo, "kao and "dry_clay respectively

    likewise limestone, dolomite, clay and dry clay neutron

    porosity are !N_lime, !N_dolo, !N_kao and !N_dry_clay

    respectively. Hydrocarbon density, "hc was chosen

    appropriately for the oil and gas legs then solved

    iteratively for the unknowns. Grain density, "matrix was

    calculated by:

    ( ) ( ) ( )( )

    She

    hcxoWaterxoekaoSh

    Matrix

    V

    SSV

    !!

    "!+""!"!

    =

    #

    $$#$$$

    1

    1

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    where Sxo is calculated using the Archie equation

    assuming Rmf=Rw,

    n

    mTxo

    mf

    xo

    R

    aRS

    1

    !

    !

    "

    #

    $

    $

    %

    &=

    '

    where a = 1, m = 2, n = 2. The effective porosity, !e

    calculated here is not used in anyway apart from to

    calculate total porosity, !T. Effective porosity was

    calculated from the rock typing and capillary pressure

    model detailed below.

    WATER SATURATION

    Formation and flushed zone water saturations were

    calculated using the dual porosity method, Petricola andWatfa (1995). Rw, m and n values were based on Rw

    analysis and SCAL results from two wells.

    Effective and total formation and invaded water

    saturations were calculated using equation 3, Petricola

    and Watfa (1995):

    ( )

    ( ) ( )

    ( )micro

    micro

    micro

    macro

    micro

    marcom

    macro

    mircom

    micro

    T

    w

    n

    w

    R

    R

    S

    !

    !!

    !

    !

    !

    +

    +

    +

    +

    "##$

    %&&'

    (

    =

    1

    )(

    1

    )(1

    1

    1

    )T

    microwe

    wT

    SS

    !

    !! +"=

    where m(micro) and m(macro) were taken to be the

    minimum and maximum measured Archie m values

    respectively.

    IRREDUCIBLE WATER SATURATION AND

    RESIDUAL OIL SATURATION

    Irreducible water saturation, Swir, and residual oilsaturation, Sor, were fitted to total porosity derived from

    SCAL data.

    Swir=1*e-a

    !

    T

    Sor=1*e-b

    !

    T

    Maximum recoverable oil = (1- Swir- Sor)

    where a and b are the appropriate fitting constants.

    CAPILLARY PRESSURE AND ROCK TYPING

    The hyperbolae for each plug of nearly 90 plugs were

    plotted on the bulk volume occupied against capillary

    pressure plot (Figure 1). A histogram of the threshold

    entry pressures for the macro pores, Pd_macro, (Figure 2)provided the classification of the rock types (Table 1).

    It is interesting to know that at the basic level, the Lucia

    (1995) classes are also based upon variations in

    displacement pressure, which Lucia then relates to

    crystal size (and poro-perm crossplot position). Thomeer

    (1983), however, has the enhanced capability of being

    able to simultaneously address multiple pore systems.

    Gaussian fits to each of the rock types enabled P10, P50

    and P90 estimates to be developed (Figure 1). The

    average and standard deviation of Pd, BV", G parameters

    for each pore space were analysed to produce the BVP10, P50, P90 data fits.

    Rock TypeCapillary Pressure

    Range (psia)

    0 275

    Table 1.Rock typing pressure classes

    An observation was made that the P10-90 range of eachPd, BV", G parameter was ~0.5 times the parameter

    average. This was utilised to generate the P10 and P90

    from the P50 parameters.

    The Pd, BV", G fitting parameters were analysed to

    develop relationships that allowed the prediction of the

    parameters from known/measured inputs !Tand Pd_macro

    were taken forward (Figure 3).

    (macro and micro) Pd= a * !T-b

    (meso) Pd= a * Pd_macro-b

    (macro) BV#= c * Pd_macrod(meso and micro) BV#_i= c * !T

    d

    G_i= e

    where i is micro, meso and macro respectively and a to e

    are the appropriate fitting constants.

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    P10 parameters were calculated as = 1.5 * parameter and

    P90 parameters were calculated as = 0.5 * parameter.

    Effective porosity, !e is defined as the macro pore space

    as this is the only pore space considered to contribute to

    flow in this reservoir.

    !e= (BV#_macro/BVT) * !T

    SATURATION HEIGHT IMPLEMENTATION

    Implementation of the saturation height model required

    linking Pd_macroto log data allowing log based rock types

    calibrated to the capillary pressure data thus allowing

    delivering textural representative K, !eand Swestimates.

    Most log datasets contained only LWD gamma ray,

    resistivity, density and neutron logs. Advanced logswere restricted to a small number of vertical wells.

    Density-neutron log separation was been observed to

    indicate rock quality irrespective of pore fluid thus

    establishing a relationship between density-neutron

    porosity separation and Pd_macro(Figure 4):

    !density= (2.71 - "b) / 1.71

    !dif= !density- !neutron

    Pd_macro= a*10-b.

    !dif

    where a and b are the appropriate fitting constants. Thevariations in mineralogy (calcite dolomite, kaolinite)

    were linked to the rock quality variations. High kaolinite

    and/or dolomite found in the poorer facies but due to the

    close values of the photoelectric factor for example both

    ~3B/e, a photoelectric factor method was unsuitable for

    implementation.

    In combination with !T from density-neutron logs and

    height above free water level the capillary pressure, Sw

    (BV/!T), !e, Swirand K could be calculated.

    Wireline implementation and comparison with SCAL

    data was performed on a number of wells with therelevant core data sets (Figure 5). Note the log based

    rock typing (curves) are most well fitted to SCAL data

    (stars) and that the log based rock typing is never more

    that one rock type incorrect.

    Permeability

    The relationship between !T and K is compared with

    Pd_macro and permeability, K. Note that the stronger

    correlation is between Pd_macro and K (Figure 6). An

    improved relationship is established by combining !Tand Pd_macro(green) compared with Pd_macroalone (black)

    to predict K (Figure 7). P10 and P90 estimates were also

    given (Table 2).

    KClerke= 10[d + e * log(Pd_macro) + f * log(

    !T)]

    Parameter P10 P50 P90

    d 0 -0.6 -1.2

    e -0.59 -0.59 -0.59

    f 7.3 7.3 7.3

    Table 2.Permeability fitting parameters

    Lucia (1995) also notes the strong correlation between

    Pd_macro and K specifically that pore throat size, the

    largest of which is reflected in the displacement

    pressure, is more important than is the porosity. The

    Thomeer analyses approach presented here is an

    improvement on the usual Lucia model in that it

    recognizes simultaneous multiple pore size modes.

    Absolute fluid permeabilities were measured as part of

    the relative permeability tests at residual oil saturation

    and irreducible water saturation. Crossplotting fluid

    permeabilities with core Klinikenberg permeability

    demonstrated that only simple power trends wererequired (Figure 8). Note that the magnitude of the

    Klinkenberg correction is smaller, as permeability

    becomes larger.

    Relative Permeability

    The objective of relative permeability analysis is to

    describe the fractional flow of the fluids produced at any

    given water saturation observed. In combination with

    the rock typing it was possible to estimate fluid fractions

    based on fitted parameters by extending Clerkes (2007)

    fitting method for oil curves in a water/oil system to all

    fluids in the three phase system present in this case.

    In addition the concave relative permeability

    behaviour observed could be fitted and is due to the

    micritic nature of the rock. Fitting concave curves was

    possible using exponents

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    By normalising water/oil saturation between the residual

    oil/trapped gas to irreducible water/residual oil, fitting

    parameters were obtain for each of the sample-fluid pair

    curves and fractional flow curves (Figure 9). These

    fitting parameters were analysed to obtain predictive

    trends with absolute permeability (Figure 10).

    Permeability thickness and fractional flow could be

    derived to assist with production volume and rates

    estimates.

    Oil/Gas

    ( )( )( )

    ( ) ( )[ ]

    ( ) ( )[ ]gasoilgasoilgasoil

    gasoil

    Sdoilgas

    b

    gggasoil

    orgt

    orwgg

    KrKrFF

    cecKr

    SaKr

    SS

    SSS

    gg

    !!+=

    "!+=

    !=

    ""

    ""

    =

    !

    __

    _

    _

    _

    1

    1

    1

    1

    1

    Water/Oil

    ( )( )

    ( ) ( )[ ]

    ( ) ( )[ ]oilwateroilwateroilwater

    oilwater

    Shwateroil

    f

    soilwater

    orwir

    wirws

    KrKrFF

    gegKr

    SeKr

    SS

    SSS

    s

    !!+=

    "!+=

    !=

    ""

    "

    =

    !

    __

    _

    _

    _

    1

    1

    1

    1

    where SSand Sggare the normalised saturation, Sgtis the

    trapped gas saturation, Kris the relative permeability to

    the respective fluids, FF is the fractional flow to the

    respective fluids and ! are the respective fluid

    viscosities and, a to h are the appropriate fitting

    functions of the form:

    a=x*Ky

    a = x*log(K)+y

    CONCLUSIONS

    The use of an appropriate capillary pressure model

    enabled the petrophysical characterisation of a micritic

    carbonate field. It was observed that the difference in

    density and neutron porosity values was related tothreshold entry pressure of the macro pore system. In

    combination it was possibly to extend the water

    saturation and permeability calculations to all wells with

    triple combo logs in the field.

    The Thomeer analyses approach presented here is an

    improvement on the usual Lucia model in that it

    recognizes simultaneous multiple pore size modes. The

    approach also extends Clerkes methods.

    The revised approach assisted the understanding of the

    hydrocarbon distribution within the field and thus well

    planning and recoverable volumes. As a consequence of

    the improved description of the matrix behaviour, there

    was recognition of the significance of fracture flow to

    production.

    Production and well test permeability values were an

    order of magnitude greater than the maximum

    permeability values calculated from the matrix. Fracture

    mapping and image analysis was therefore required and

    gave rise to the re-processing of the seismic volume for

    fracture attributes and an integrated study of fracture

    from core and image logs.

    ACKNOWLEDGMENTS

    The authors wish to thank BG Group for permission to

    publish this work. Dr. Tim Pritchard, Head of

    Petrophysics (BG Group) is gratefully acknowledged for

    reviewing the text and discussing the results.

    REFERENCES

    Ballay, G., 2008, Monte Carlo modelling with Excel,

    GeoNeurale. ([email protected])

    Bateman, R.M., and Konen, C.E., 1977, "The Log Analystand the Programmable Pocket Calculator, Part II -

    Crossplot Porosity and Water Saturation", The Log

    Analyst, November-December 1977.

    Batzel, M., and Wang, Z., 1992, Seismic properties of pore

    fluids, Geophysics., 57, 1396-1408.

    Clerke, E.A., Mueller III, H.W., Phillips, E.C.,

    Eyvazzadeh, R.Y., Jones, D.H., Ramamoorthy, R., and

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    Srivastava, A., 2008, Application of Thomeer Hyperbolas

    to decode the pore systems, facies and reservoir properties

    of the Upper Jurassic Arab D Limestone, Ghawar field,

    Saudi Arabia: A Rosetta Stone approach, GeoArabia,

    Vol. 13, No. 4, p.113-160

    Clerke, E.A., 2007, Permeability and microscopic

    displacement efficiency of M_1 Bimodal pore systems in

    Arab-D Limestone, SPE 105259

    Crain, E.R., 1986, "The Log Analysis Handbook, Volume

    1: Quantitative Log Analysis Methods", PennWell, ISBN

    0-87814-298-3 (v.1).

    Kewen, L. and Horne, R.N., 2002, Experimental

    verification of methods to calculate relative permeability

    using capillary pressure data, SPE 76757

    Lucia, F.J., 1995, Rock-fabric/petrophysical classification

    of carbonate pore space for reservoir characterization,

    AAPG Buletin no.79 v.9, pp1275-1300.

    Petricola, M.J.C., and, Wafta, M., 1995, Effect of micro

    porosity in carbonates: Introduction of a versatile saturation

    equation, SPE 29841

    Schlumberger Chartbook, 2009, Schlumberger.

    Thomeer, J.H.M., 1983, Air permeability as a function of

    three pore-network parameters, Journal of Petroleum

    Technology, April, p. 809-814.

    Thomeer, J.H.M., 1960, Introduction of a pore

    geometrical factor defined by a capillary pressure curve,

    Petroleum Transactions, AIME, v. 219, T.N. 2057, p. 354-

    358.

    ABOUT THE AUTHORS

    Stefan Calvert is a Principal Petrophysicist currently

    working in Brisbane and for the last seven years withBG Group Plc. Prior to BG he spent four years working

    as a Research Petrophysicist for Reeves Wireline

    Technologies Ltd (now Weatherford). His interests

    include unconventional reservoirs, horizontal well log

    interpretation, induction logging, cased hole nuclear

    logging, carbonates and thin bed evaluation. Stefanholds a BSc in Physics, an MSc in Geophysics and a

    PhD in Petrophysics from UK universities. He has also

    published papers with the SPWLA, SPE and EAGE.

    Stefan is current President of the FESQ and member of

    SPWLA, SPE, IOP and PESGB. Stefan jointly holds a

    patent for cased hole density log hydrocarbonevaluation. Outside of work Stefan enjoys swimming,

    scuba diving, hiking, snowboarding and travelling.

    Gene Ballay served in the U.S. Army as a microwave

    repairman and in the U.S. Navy as an electronics

    technician, and he is a USPA parachutist and a PADI

    dive master. He holds a PhD in theoretical physics with

    double minors in electrical engineering/mathematics,

    has taught physics in two universities and heldpetrophysical engineering assignments in Houston,

    Texas; Anchorage, Alaska; Dallas, Texas; Jakarta,

    Indonesia; Bakersfield, California; and Dhahran, Saudi

    Arabia.

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    Figure 1. Bulk volume occupied against capillary pressure.

    Figure 2. Pore throat radius distribution.

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    Figure 3. The Pd, BV", G fitting parameters relationships with known inputs !Tand Pd_macro.

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    Figure 4. Core threshold entry pressure to wireline density neutron porosity difference calibration crossplot.

    Capillary pressure data was available for four wells each represented in a different colour.

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    Figure 5. Example log with wireline predicted threshold entry pressure (blue curve) and rock type (magenta curve)

    compared to core threshold entry pressure (blue star) and rock type (magenta star).

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    Figure 6. Core total porosity (green) and core threshold entry pressure (blue) crossplot with core permeability.

    Figure 7. Permeability prediction comparing Clerke (2007) {green} and Thomeer (1983) {black} methods.

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    Figure 8.Crossplot of fluid permeabilities with core Klinikenberg permeability.

    Figure 9.Fitting parameters to fractional flow curves, gas-oil example. Note that one sample has a concave shape.

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    Figure 10.Relative permeability fitting parameters predictive trends with absolute permeability.