enhanced oil recovery-slides-12
DESCRIPTION
Enhanced Oil RecoveryTRANSCRIPT
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-121
EOR IN NATURALLY FRACTURED RESERVOIRS
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-122
WHAT ARE THE DIFFERENCES BETWEEN “HOMOGENEOUS and FRACTURED RESERVOIRS?
•Fracture network controls the flow due to high k.•Matrix stores most of the oil due to high •Frontal advance theory may not be applicable.•Matrix-fracture interaction is the main cause of HC production
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ELEMENTS OF NATURALLY FRACTUREDRESERVOIR MANAGEMENT
Characterization Reservoir dynamics EOR
Matrix FractureMost proper
methodMatrix effect
CoreWell testWell logsOutcrop
Experiment(Scaling)
Fracture effect
“Monitoring”performance
Numerical simulation
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-124
“HOMOGENEOUS” SYSTEMS
I I
I I
P
WATER BREAKTHROUGH
WATERPRODUCTION
I : INJECTION WELLP : PRODUCTION WELL
Swept ZoneUnswept Zone
Unrecovered oil can be in pores, never swept (not residual oil!!!!) OR it can be in pores swept (residual oil!!!!)
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-125
• UNSWEPT AREA: Channeling
FRACTURED SYSTEMS
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-126
EOR MECHANISMS in NFRs
• Fracture Recovery – Viscous Flow
• Matrix Recovery – Capillarity and Mass Transfer– Gravity Drainage
– Capillary Imbibition
– Convection
– Diffusion
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OIL
WATER
X
x
a
aPgakq cow
o
oi
)(
Magnitude of gravity Magnitude of capillarity
OIL AND WATER
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CONVECTION AND DIFFUSION
CONVECTION
•Result of contrasting oils within the fracture network•Large times are needed to see the effect of convection•High vertical permeability (fractures) accelerates•Oil at the crest is heavier than the base.•Vertical fractures provide communication for convection
DIFFUSION
•Contrast in HC properties between fracture and matrix
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OIL
WATER
H
x
H-Z
])1([
)(
ZMMHkk
ZHgPu
rw
w
c
Z
High H and small Z Gravity dominates
Water wettability is small Gravity dominates
OIL-WATER : FULLY IMMERSED IN WATER
Z Height of the water front in the block above the bottom
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-1210
6 min. 9 min. 12 min. 15 min.
0 20 40 60 80 100
Sw, Average
6 min.
30 min.
x, C
ore
Leng
th (v
ertic
al)
1
WAT
ER
WAT
ER
WAT
ER
WAT
ER
6 min. 9 min. 12 min. 15 min.
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-1211
3 min. 18 min. 30 min. 1 day
0 20 40 60 80 100
Sw, Averagex, C
ore
Leng
th (v
ertic
al)
3 min
80 min.
0
1
OIL OIL OIL OIL
WAT
ER
WAT
ER
WAT
ER
WAT
ER
3 min. 18 min. 30 min. 1 day
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Berea SandstoneHeavy Crude Oil-Brine
Indiana LimestoneLight Crude Oil -Brine
OIL RECOVERY IN NATURALLY FRACTURED RESERVOIRS
Capillary Imbibition Transfer at Static Conditions, i.e. No Flow of Water in Fracture
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Matrix recovery by capillary imbibition is not EFFECTIVE if
• IFT is high• Unfavorable matrix boundary conditions restricting the contact of matrix and water in
fracture exist• Matrix is oil-wet
and• OIL VISCOSITY IS HIGH
PROBLEM
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SURFACTANT, POLYMER, HOT WATER INJECTION
to reduce IFT and oil viscosityor to increase water viscosity
or to overcome unfavorable matrix boundary conditions and oil wettability
or to have additional recovery mechanisms
SOLUTION(Babadagli, Coll. And Surface A: Phys. And Eng. Asp., 2003 – SPE 69564)
?
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EXPERIMENTATION AT STATIC CONDITIONS• Most proper EOR method (injection fluid)• Scaling to reservoir scale
OBJECTIVE
?
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Which method (EOR fluid) yields the most effective recovery methods
different boundary conditions, oil type, IFT, oil viscosity, wettability.
PART I-ASELECTION OF EOR METHODS
for
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0.1 1.0 10.0 100.0Time, minutes
10
30
50
0
20
40
60R
ecov
ery,
% O
OIP
T=26.5 °C
T=50 °C
T=80 °C
ENGINE-OIL (175 cP)
Unfired Berea
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0.1 1.0 10.0 100.0 1000.0Time, minutes
10
30
50
70
0
20
40
60
80R
ecov
ery,
% O
OIP
% 1 SURFACTANT (IFT=6 dyn/cm)
% 2 SURFACTANT (IFT=5 dyn/cm)
BRINE (IFT=41 dyn/cm)
MINERAL OIL (235 cP)
Unfired Berea
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ROCK & FLUID PROPERTIES
OILKerosene
Crude Oil (light)Engine oilMineral Oil
SURFACTANT1 vol %
POLYMER0.1 and 0.2 wt %
Rock type : Unfired BereaLength : 10 cm.Diameter : 3.8 and 2.5 cm.Permeability : 500 md.Porosity : 0.2Brine : 3 wt % NaCl
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FLUID PROPERTIESFLUID TYPES
Densityg/cc
ViscositycP
IFT with
kerosene dyne/cm
IFT with
crude oil dyne/cm
IFT with
engine oildyne/cm
Brine (3% NaCl)
1 1.1 40 25 71
Surfactant Solution (1%)
1 1.1 11 11 15
Surfactant Solution (2%)
1 1.1 - - 14
Polymer I (0.1 wt %)
1 18 - 17 23
Polymer II (0.2 wt %)
1 87 - 22 24
Kerosene 0.79 1.7
Crude Oil 0.81 5.6 Engine Oil 0.89 633
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COUNTER-CURRENT IMBIBITION (CCI)
Open Matrix SurfaceCoated Matrix Surface
(CCI)(CCI) (CCI)
(Babadagli, Coll. And Surface A: Phys. And Eng. Asp., 2003 – SPE 69564)
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CO-CURRENT IMBIBITION (CCI)
Open Matrix SurfaceCoated Matrix Surface
(CCI)
(CCI)
(CCI)
(Babadagli, Coll. And Surface A: Phys. And Eng. Asp., 2003 – SPE 69564)
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OIL
Coating
WATERMovement of waterMovement of oil
Oil saturated rock (Berea SS)
Capillary imbibition(water in oil out)
Gravity (oil up water down)
Capillary re-imbibition(oil down water up)
DIFFERENT OIL WATER BOUNDARY CONDITIONS by COATING (CO-CURRENT FLOW)
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INVERSE BOND NUMBER
N = cg H
kB
-1
Capillarity
Gravity
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NB-1 > 5 NB
-1 < 0.25 > NB-1 > 0.2
R RR
log(t) log(t) log(t)
REPRESENTATIVE RECOVERY CURVESSchechter et al. 1994
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KEROSENE - COUNTER-CURRENT IMBIBITION
0102030405060
0.01 0.1 1 10 100 1000 10000Time, minutes
Oil
Rec
over
y, %
OO
IP
Kerosene-Brine Kerosene-Surfactant
BOUNDARY CONDITIONS
(Babadagli, Coll. And Surface A: Phys. And Eng. Asp., 2003 – SPE 69564)
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-12
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0
10
20
30
40
50
60
0.01 0.1 1 10 100 1000Time, minutes
BrineSurfactant (1 vol %)O
il R
ecov
ery,
% O
OIP
BC: COU-C1 Oil Type : Crude Oil Core Diameter = 1.5 in.
(Babadagli, Coll. And Surface A: Phys. And Eng. Asp., 2003 – SPE 69564)
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-12
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0
10
20
30
40
50
60
1 10 100 1000 10000 100000
Time, minutes
Brine
Surfactant (1 vol %)Oil
Rec
over
y, %
OO
IPOil Type : Crude Oil Core Diameter = 1.5 in.
(Babadagli, Coll. And Surface A: Phys. And Eng. Asp., 2003 – SPE 69564)
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STATIC CONDITIONSCapillary Imbibition Transfer at Static Conditions,
i.e. No Flow of Water in Fracture
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-12
30
0
10
20
30
40
50
60
0.01 0.1 1 10 100 1000 10000 100000Time, minutes
BrineHeat (40 C)Heat (80 C)O
il R
ecov
ery,
% O
OIP
Oil Type : Crude Oil Core Diameter = 1.5 in.
(Babadagli, Coll. And Surface A: Phys. And Eng. Asp., 2003 – SPE 69564)
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-12
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0
10
20
30
40
50
60
0.01 0.1 1 10 100 1000 10000 100000 1000000Time, minutes
BrinePolymer (0.1 wt %)Polymer (0.2 wt %)O
il R
ecov
ery,
% O
OIP
Oil Type : Crude Oil Core Diameter = 1.5 in.
(Babadagli, Coll. And Surface A: Phys. And Eng. Asp., 2003 – SPE 69564)
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-12
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0
5
10
15
20
25
30
100 1000 10000 100000 1000000Time, minutes
BrineTemp. increased to 80 CSurfactant ( 1 vol %)Surfactant (2.5 vol %)O
il R
ecov
ery,
% O
OIP
Oil Type : Engine Oil Core Diameter = 1 in.
(Babadagli, Coll. And Surface A: Phys. And Eng. Asp., 2003 – SPE 69564)
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0
5
10
15
20
25
30
1 10 100 1000 10000 100000 1000000Time, minutes
BrineTemp. increased to 80 CBrine (40 C)Temp. increased to 80 CBrine (80 C)
Oil
Rec
over
y, %
OO
IPOil Type : Engine Oil Core Diameter = 1 in.
(Babadagli, Coll. And Surface A: Phys. And Eng. Asp., 2003 – SPE 69564)
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-12
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Berea Sandstone, Oil Type : Heavy Crude Oil (2200 cP) Core Diam. = 1 in.
0
10
20
30
40
50
60
70
1 10 100 1000 10000 100000 1000000
Time, min.
Brine-Heavy Crude Oil
Polymer-Heavy Crude OilSurfactant-Heavy Crude Oil
Hot Water-Heavy Crude Oil
Oil
Rec
over
y, %
OO
IP
(Babadagli, CIPC, 2001-130, 2001
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Berea Sandstone, Oil Type: Heavy Crude Oil (2200 cP)Core Diam.= 1.5 in.
0
5
10
15
20
25
30
35
40
45
50
1 10 100 1000 10000 100000 1000000
Time, min.
Brine-Heavy Crude Oil
Hot Water-Heavy Crude Oil
Oil
Rec
over
y, %
OO
IP
(Babadagli, CIPC, 2001-130, 2001
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-12
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Indiana Limestone, Oil Type : Heavy Crude Oil (2200 cP) Core Diam. = 1 in.
0
1
2
3
4
5
6
7
8
9
1 10 100 1000 10000 100000 1000000
Time, min.
Brine-Heavy Crude OilPolymer-Heavy Crude OilSurfactant-Heavy Crude OilHot Water-Heavy Crude Oil
Oil
Rec
over
y, %
OO
IP
(Babadagli, CIPC, 2001-130, 2001
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Tayfun Babadagli, PhD, PEng Short Course - EOR File-12
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0
2
4
6
8
10
12
14
16
1000 10000 100000 1000000Time, minutes
Brine, k=276 mD Polymer (0.1 wt %), k=128 mDPolymer (0.2 wt%), k=155 mD Surfactant (1 vol %), k=19 mDSurfactant (2.5 vol %), k=24 mD Heat (40 C), k=1 mDHeat (80 C), k=4 mD Temp. increased from 40 to 80 C
Oil
Rec
over
y, %
OO
IP
DOLOMITIC LIMESTONE
(Babadagli, Coll. And Surface A: Phys. And Eng. Asp., 2003 – SPE 69564)
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- Light oils: no surfactant. Especially for unfavorable BC.- Heavy oils: surfactant is desirable. Especially for
unfavorable BC.- Light oils: polymer is not desirable. For all BCs.- Heavy oils: polymer is desirable. Especially for
unfavorable BC.- Thermal is effective to fasten light oil recovery but not
for ultimate recovery.- Thermal is effective to fasten heavy oil recovery and for
ultimate recovery.
SELECTION CRITERIASANDSTONES
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- They all good!- Thermal > surfactant > polymer > brine.
SELECTION CRITERIACARBONATES