2_oil prop

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  • 8/19/2019 2_OIL PROP

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    BLACK OIL

    PROPERTIES

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    Black Oil Properties

    Important in Reservoir Engineering andProduction Engineering Calculations

    Formation Volume Factor of Oil, B oSolution Gas-Oil Ratio, R sTotal Formation Volume Factor, B t Coe icient of Isot!ermal compressi"ilit#, c oOil Viscosit#, µ oInterfacial Tension, σ o

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    Solution Gas-Oil Ratio

    T!e $uantit# of %gas& dissolved in %oil& atreservoir conditions

    Treat as a t'o-component s#stem (ctuall# %gas& and %oil& consist of man#components, and composition of eac! p!asec!anges as pressure declines)

    * ""l of oil at reservoir conditionsSplits into stoc+ tan+ oil and gas at standard

    conditions

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    Solution Gas-Oil Ratio

    e nition

    .nits / scf0ST1

    stock tank atsurfaceat producedoilof volumeconditionsstandardatsurfaceat producedgasof volume

    = s R

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    Behavior of B o ith Pressure

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    Li!ui" Speci#c Gravit$% o

    T!e ratio of t!e densit# of a li$uid to t!edensit# of 'ater at t!e same 2P,T3)

    (PI gravit#

    5.1315.141

    −γ = o API

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    E&a'ple

    T!e densit# of a stoc+-tan+ oil at 45 o F is6*)76 l"m0cu)ft) Calculate t!e speci cgravit# and (PI gravit#)

    Speci c Gravit#

    8217.037.62

    25.51==

    ρρ

    =γ wo

    o

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    E&a'ple

    (PI gravit#

    AP7.405.131

    8217.0

    5.141

    5.1315.141

    o

    o API

    =−=

    −γ

    =

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    Oil (or'ation )olu'e (actor

    T!e volume of reservoir li$uid 2atreservoir 2P,T33 re$uired to produce one"arrel of stoc+-tan+ oil

    .nits / res) ""l0ST1

    Volume of reservoir oil is al'a#s "iggert!an stoc+-tan+ #ield

    Reservoir li$uid contains dissolved gas)

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    Oil (or'ation )olu'e (actor

    Value of B o a ected "#Evolution of dissolved gas 'it! reducedpressureE8pansion of li$uid 'it! reduced pressureS!rin+age of li$uid as temperature falls

    T!e last t'o e ects are small, and tend too set eac! ot!er)

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    Behavior of B o ith Pressure

    ("ove t!e "u""le point pressure, B o increases slig!tl# as pressure is reduced

    E8pansion of li$uid 2no gas evolved31elo' t!e "u""le point pressure, B odecreases

    S!rin+age of oil as dissolved gas evolves (t atmosp!eric pressure, B o ≈ *)

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    Total (or'ation )olu'e (actor

    9ot 'idel# used no'ada#sFound in some older ReservoirEngineering applications

    ( ) s sb g ot R R B B B −+=

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    Coe*icient of Isother'alCo'pressi+ilit$ of Oil

    C!ange in volume per unit volume per psi

    For li$uids, oil compressi"ilit# is almostconstant

    T o P

    V V

    c

    ∂∂−= 1

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    Coe*icient of Isother'alCo'pressi+ilit$ of Oil

    Oil a"ove t!e "u""le point pressure, c o issmall and almost constant

    Slig!tl# compressi"le li$uid

    Separate varia"les and integrate

    ∫ ∫ −=

    ∂∂

    −=2

    1

    2

    1

    1

    V

    V

    p

    p

    o

    T o

    V

    dV dP c

    P V

    V c

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    Coe*icient of Isother'alCo'pressi+ilit$ of Oil

    For c o small

    ( )

    ( )( )12121

    212

    e!p

    ln

    p pcV V

    V V p pc

    o

    o

    −−=−=−

    ( )( ) ( )

    12

    12

    1

    1212

    11e!p

    p pV V

    V c

    p pc p pc

    o

    oo

    −−−≈

    −−≈−−

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    Belo the Bu++le Point

    :it! decreasing pressure, gas evolves andt!e li$uid s!rin+s

    ∂∂−

    ∂∂−=

    T

    s g

    T

    o

    oo P

    R B

    P B

    Bc

    1

    h f

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    Behavior of c o at ConstantTe'perature

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    Coe*icient of )iscosit$ of Oil

    Increase in temperature causes decreasein viscosit#

    ecrease in pressure ("ove "u""le point< decrease in viscosit#1elo' "u""le point< increase in viscosit#

    $

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    Oil )iscosit$ at ConstantTe'perature

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    Initial Reservoir Pressure

    (t initial pressure reservoir isSaturated< P r ≤ P ".ndersaturated< P r = P "

    Saturated< free gas present in a gas cap)Initial Pressure > Saturation Pressure.ndersaturated / no free gas)

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    ,n"ersaturate" Reservoir

    Production trends, P r = P "Initiall# all gas dissolved in oilSingle p!ase li$uid containing all availa"le gasenters 'ell"ore

    (s oil travels to surface gas evolvesProduced GOR > initial dissolved GOR >constantPressure declines rapidl# 2e8pansion of li$uid3

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    ,n"ersaturate" Reservoir

    Production trends, P r ≤ P " (t t!e "u""le point, rst "u""le of gas evolvesInitiall#, gas does not ;o' / small "u""les%stic+& to sides of t!e poresOil entering 'ell"ore contains less dissolvedgas t!an initialProducing GOR falls slig!tl#)

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    ,n"ersaturate" Reservoir

    Production trends, P r ≤ P " (s pressure continues to decline, gas "u""lescoagulate to form large "u""les, and gas;o's)

    Gas ;o's more easil# t!an oil / GORincreases)Reservoir pressure declines slo'l#< gas inreservoir e8pands and maintains pressure)

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    Black Oil Pro"uction

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    Black Oil Pressure ecline

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    .ote

    ?ig! gas compressi"ilit# is a great sourceof energ# storage in t!e reservoir:it! oil removal, gas e8pands to ll up

    void left 'it! onl# a small pressuredecline)It is "etter to +eep t!e gas in t!e reservoirt!an to remove it)

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    Esti'ation of (lui" Properties

    Production a"ove "u""le pointProducing GOR ≈ constant > R s"Pressure declines rapidl#

    1elo' "u""le pointProducing GOR increases rapidl#Pressure declines slo'l#

    Can estimate R s" and "u""le pointpressure

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    Bubble Point Pressure

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    )olatile Oils

    Same trends as for 1lac+ Oil ("ove "u""le point, pressure does notdecrease as rapidl#

    C!ange of slope in pressure decline at"u""le point di icult to detect)1u""le point pressure !ard to identif#

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    Retro/ra"e Gas

    ("ove de' pointProducing GOR constant

    1elo' de' pointProducing GOR increases "ecause li$uids are left in t!e

    reservoir)e' point pressure cannot "e determined from

    pressure decline data9o apprecia"le c!ange in slope at de' point)

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    Reservoir (lui" Stu"ies

    etermine1u""le-point pressureFormation volume factor of oil

    Solution gas-oil ratioTotal formation volume factorCoe icient of isot!ermal compressi"ilit# of oilOil viscosit#

    @-factorFormation volume factor of gasGas viscosit#

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    Reservoir (lui" Stu"ies

    Variation of separator conditions todetermine

    Separator gasStoc+ tan+ gasStoc+ tan+ oil

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    Proce"ures

    Composition measurementFlas! vaporiAation

    i erential vaporiAation

    Separator tests Viscosit# measurement

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    Sa'plin/

    O"taining a representative reservoirli$uid sample is di icult '!en t!ereservoir is saturated

    1ottom-!ole sampleSample o"tained at "ottom-!ole 2P,T3

    Separator samplesSeparator oil and gas samples are recom"ined in t!e%correct& ratio

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    Co'position

    i icult to determine e8act compositionof !undreds of di erent c!emical speciesin crude oilCompositions of C* / C4 usuall#determined?eavier components lumped in a CBpseudo-component)

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    (lash )apori0ation