2_oil prop
TRANSCRIPT
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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