strategies for maximizing secure storage of co2 in deep aquifers
TRANSCRIPT
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CPGE
Strategies for Maximizing Secure Storage of CO2 in Deep Aquifers
Steven BryantDirector, Geological CO2 Storage JIP
Center for Petroleum and Geosystems Engineering
The University of Texas at Austin
Princeton Workshop on Leakage Modeling, 1-2 Nov 2005
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CPGE
Original Motivation of JIP
• Identify key phenomena influencing aquifer storage
• Understand governing mechanisms• Demonstrate feasibility of permanent
storage in aquifers• Founding membership
- ChevronTexaco- ExxonMobil- ENI- CMG
CO2
Deep Saline Aquifer
Aquifer/DepletedOil or Gas Reservoir
Oil/Gas Producing Reservoir
Unmineable Coal
CO2
Deep Saline Aquifer
Aquifer/DepletedOil or Gas Reservoir
Oil/Gas Producing Reservoir
Unmineable Coal
CO2
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CPGE
People
• Research Scientists- Srivatsan Lakshminarasimhan- Mojdeh Delshad- Aura Araque- Heather Pedraza
• Grad Students- Vikas (MS 03)- Ajitabh Kumar (MS 04) - Myeong Noh (PhD 04)- Robin Ozah (MS 05)- Elizabeth Zuluaga
(PhD 05)- Yousef Ghomian- Justin Ferrell- Derek Wood- Sang-Yeop Park- Kyung-won Chang
• Undergraduates - Sarah Dobbs- Nurhidayah Hutamin- Chris Irle- Archna Agrawal- Michael Boyle
• Faculty- Bryant- Pope- Lake
- Sepehrnoori- Nguyen- Jablonowski- Minkoff (UMBC)
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CPGE
Key points
• Reservoir simulation is important tool for understanding mechanisms in aquifer storage
• Augmented reservoir simulators essential for designand risk assessment of aquifer storage
• Permanent storage of CO2 feasible- Implications for probability of leakage
• Simulation-based optimization as guide to future needs- Petrophysical characterization- Laboratory experiments- History matching- New field measurement techniques/tools- Site selection & Risk assessment
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CPGE
Outline
• What we’re trying to do- Geological CO2 Storage Joint Industry Project- www.cpge.utexas.edu/gcs
• How we’re trying to do it- which simulators- what kind of simulations
• What we’ve learned• What’s next
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CPGE
AA'Approach
• Simulate prototypical storage scheme - Inject 1 million tons/yr for 50 yrs- Shut in injection well- Simulate 10 3-104 years of gravity-
driven flow• Examine sensitivity of behavior
- Aquifer characteristics- Injection strategy
• Track CO2 fate- CO2-rich phase
• Mobile saturation• Residual saturation
- Brine phase- Carbonate minerals
SgInjection well
A'
A
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CPGE
Phase Densities: CO2-Saturated Brine
60
62
64
66
68
70
72
74
76
78
0 50000 100000 150000 200000 250000 300000 350000
Salinity, ppm NaCl
Brin
e D
ensi
ty, l
b / c
u ft
CO2 Saturated Brine
Brine (Without CO2)
T = 140°F; P = 3000 psi
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CPGE
Key Petrophysical Properties
• Porosity• Permeability
- Magnitude- Anisotropy
• Residual gas saturation• Property correlation (Holtz,
2002)• Capillary pressure• Relative permeability• Hysteresis
- Land model
0.0
0.2
0.4
0.6
0.8
1.0
0.16 0.19 0.22 0.25 0.28 0.31 0.34Porosity, fraction
Frac
tion
0.001
0.01
0.1
1
10
100
1000
10000
Per
mea
bilit
y, m
d
Irreducible water
saturationPermeability
Maximum residual
gas saturation
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0 0.1 0.2 0.3
Porosity (fraction)
Res
idua
l gas
sat
urat
ion
(fra
ctio
n)
0.4
Courtesy Mark Holtz, BEG
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
00
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0 0.1 0.2 0.3
Porosity (fraction)
Res
idua
l gas
sat
urat
ion
(fra
ctio
n)
0.4
Courtesy Mark Holtz, BEG
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CPGE
0.0
0.2
0.4
0.6
0.8
1.0
0.0 0.2 0.4 0.6 0.8 1.0Water Saturation, fraction
Rel
ativ
e P
erm
eabi
lity,
frac
tion
krg, Drainage
krg, Imbibition(Sgh=0.35, Sgrh=0.18)
krw
krg, Imbibition(Sgh=0.5, Sgrh=0.22) krg, Imbibition
(Sgh=0.855, Sgrh=0.27)
krg, Imbibition(Sgh=0.7, Sgrh=0.25)
Hysteresis in Relative Permeability
Injection stage: CO2 displacing water
Post-injection: water displacing CO2
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CPGE
Permanent Storage of CO2 in Aquifers
• CO2 is stored permanently when it will not escape f rom the aquifer any faster than the chemical species native to that aquifer
CO2
Deep Saline Aquifer
Aquifer/DepletedOil or Gas Reservoir
Oil/Gas Producing Reservoir
Unmineable Coal
CO2
Deep Saline Aquifer
Aquifer/DepletedOil or Gas Reservoir
Oil/Gas Producing Reservoir
Unmineable Coal
CO2
escapet
residencet
residenceescape tt ≥
Time for CO2 to travel from aquifer to
surface
Time for {water, aqueous species} to travel from
aquifer to surface
Condition for “permanence”
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CPGE
Simulators we have used
• Fully compositional (Peng-Robinson Equation of Stat e)- UTCOMP
• Research code• 20+ years development
- GEM• Commercial reservoir simulator (CMG)
• Augmented reservoir simulator- GEM-GHG- Compositional + geochemistry
• Intra-aqueous reactions• Mineral dissolution/precipitation
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CPGE
Example Simulation Results
• Injection along entire interval• Injection in bottom half of aquifer• Influence of buoyant fingers• Frio pilot behavior• Gravity-stable EOR/storage
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CPGE
Results – Influence of Well Completion (1)
• Injection across entire interval leads to extensivecontact with seal
T = 10,000 y
Plan ViewVertical Cross section
well
Saturation Profiles of CO2-rich Phase (vertical slice through the injection well in X-Z direction)
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CPGE
Results – Influence of Well Completion (2)
• Injection across lower part of interval eliminates contact with seal
Injection only into lower interval
50 Years 1000 Years
Saturation Profiles of CO2-rich Phase (vertical slice through the injection well in X-Z direction)
25.0, =residualgS
buoyant flow
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CPGE
Vertical Well
Perforation - 500 feet48 million tons injected
Horizontal wells increase aquifer utilization
• Well spacing and type
• Optimal volume as function of aquifer thickness, well type
Horizontal Well
Perforation - 5300 ft338 million tons injected
Vertical Well
Perforation - 500 feet338 million tons injected
Gas saturation at 1000 y
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CPGE
Mechanisms for permanence: residual phase
• CO2 phase is nonwetting relative to brine
• Size of pores in sedimentary rocks ~ 1-10 microns- Capillary forces dominant
• Origin of residual phase saturation(volume fraction of pore space)- Nonwetting phase
spontaneously disconnectedduring flow
- Disconnected blobs held by capillary forces
100 micron
CO2
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CPGE
Residual saturation varies with rock type
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0 0.1 0.2 0.3
0.4 0.5 0.6
Porosity (fraction)
Katz, 1966 SgrChierici, et al, 1963Fishlock, et al., 1886Firoozabadi, et.al, 1987
Keelan, 1976 Sgr (fraction)Mulyadi H. et. al, 2000 (SS*) SgrMulyadi H. et. al, 2000 (CoC*) SgrMulyadi H. et. al, 2000 (CC*) SgrGeffen T. M. et. al 1952 SgrCrowell SgrMAissaoui, 1983 SgrJerauld 1996 SgrHamon et. al, 2001 SgrKantzas et. al, 2000 SgrMMoomba SgrM
Res
idua
l gas
sat
urat
ion
(fra
ctio
n)
0.4 0.5Courtesy Mark Holtz, BEG
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CPGE
Results – Controlled buoyant flow enhances permanent storage
Mole fraction CO2 in brine
Saturation of mobileCO2 phase
Saturation of residualCO2 phase
50 years
Saturation of CO2 phase
1000 years
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CPGE
CO2
Contrast: gas cap storage minimizes permanence
aquifer
• CO2 cannot move• Brine cannot displace CO2• Will not form residual
saturation • Mass transfer only at
CO2/brine interface
shale
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CPGE
0
10
20
30
40
50
60
70
80
90
100
10 100 1,000 10,000
Time, years
CO
2 S
tore
d in
Var
ious
form
s,%
0
10
20
30
40
50
Tot
al C
O2
Sto
red,
mill
ion
met
ric to
ns
Percentage CO2 in Aqueous Phase
Percentage CO2 as Free Gas
Percentage CO2 as Residual Gas
Total CO2 Sequestered, Million Tons
Results – Controlled buoyant flow enhances permanent storage
residual
aqueous
mobile
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CPGE
Results – Mineralization contributes long term
• Key reaction: dissolution of aquifer mineral containing divalent cation
• Causes carbonate mineral precipitation
Anorthite + 2H+ + H2O �
Ca2++Al2Si2O5(OH)4
residual
aqueous
mobilemineral
Distribution of CO2 in Various Forms
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CPGE
Sample results for Frio Brine Pilot
Permeability Distribution
• Collaboration with Bureau of Economic Geology at UT-Austin
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CPGE
Upper Frio Formation Cross Section
Upp
erF
rioF
orm
atio
n
CO2 Injection Interval
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CP
GE
Frio P
ilot CO
2 Breakthrough T
ime
CO2 Mass fraction Rate in Brine (lb/day)
Observed arrival at monitoring well
simulation
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CPGE
Comparison of Predicted Gas Saturation for Alternative Frio Injection Strategies
Injection at the BottomInjection at the top
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CPGE
Predicted CO2 Distribution in Frio Pilot
Injection at the BottomInjection at the top
0
10
20
30
40
50
60
70
0 500 1000 1500 2000 2500 3000
Time, Days
CO
2 S
tore
d in
Var
ious
For
ms,
%
Mobile CO2
CO2 in the Brine
Residual Gas
0
10
20
30
40
50
60
70
0 500 1000 1500 2000 2500 3000
Time, Days
CO
2 S
tore
d in
Var
ious
For
ms,
%
Mobile CO2
CO2 in the Brine
Residual CO2
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CPGE
Gravity Stable EOR/Storage
� Candidate Reservoirs Specification� Steeply Dipping Reservoirs in Gulf Coast� Mature Oil Fields with High Remaining Oil Saturatio n� Highly Faulted Around Salt Domes�Heterogeneous
Permeability Distribution
md
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CPGE
Permeability Distribution
Oil Saturation
Frac.
md
Frio Type Reservoir; Horizontal Producer, Vertical Injectors
Top Layer
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CPGE
Permeability Distribution
md
Frac.
Frio Type Reservoir; Horizontal Producer, Vertical Injectors
Oil Saturation
Oil Recovery as % of OOIP= 31.8Sequestered portion of injected CO2= 43.6 %Cumulative gas injected= 81,000 MM SCFTotal CO2 Sequestered=35,500 MM SCF
CO2 stored=4.8 MSCF/STBOO2 injected=10.9 MSCF/STBO
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CPGE
Preliminary Simulations of Frio 2 CO2 Injection
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CPGE
Objectives of Study
• Very rapid “look-see”• Illustrate “inject at the bottom” principle
- maximize residual phase trapping• Estimate whether CO2 reaches top of formation
- Injected volumes between 1500 and 6000 ton- 3000 ton injected in Frio 1
• Examine two target sands:- “5400” sand- Lower ~100 ft of the “C” sand
• Top part of “C” used in Frio 1
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CPGE
Simulation Approach
• GEM-GHG from CMG• CO2/brine phase behavior from previous CPGE
work• Grid, wells, properties from Frio 1
- Geological model from BEG- Model limited to top 60’ of “C” sand
• Assumptions for this study (quick look)- 5400 sand
• Geometry (thickness, dip, etc) same as the top 60’ of “C” sand
• All permeabilities adjusted based on logs in C and in 5400 (range 0.8 to 4 D)
- Lower “C” sand• Rectangular box (layered) with same
dip, 150’ thick• Porosity/permeability of top 60’ same
as Frio 1• Porosity/permeability of bottom 90’
estimated from log (shaly sand)
“C” sand
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CPGE
Cases Tested
• Compare injection at top vs injection at bottom in F rio 1 (retrospective)
• Inject in bottom 35’ of 5400 sand- Different volumes of injection in 12 days
• Rates of 125 tpd, 250 tpd, 500 tpd- Different values of residual saturation
• Value for Frio 1 (Sgrmax = 0.276)• Sgrmax = 0.276/2 = 0.138
• Inject in bottom 30’ of extended C sand- Initial condition
• Simulate Frio 1 to date, then continue simulation f or 6 months
- Inject 3000 tons, starting one year after Frio 1• Reduce injection rate to 50 tpd for 60 days
- Keeps BHP < 2500 psi- ~50 mD formation in bottom of “C” sand
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CPGE
Summary of input data for Frio 1 simulations.
Length,ft 3520 Width,ft 2300 Dip, Degree 5-35 Thickness,ft 100-200 Number of blocks 43*28*26 Depth at top of formation at injection well,ft 5050 Vertical to horizontal Perm. Ratio 0.1 Average horizontal permeability,md 374 Average vertical permeability,md 37.4 Average porosity 0.214 Initial Pressure, psia 2196 Residual Water Saturation 0 .25 Residual Gas Saturation 0.25 Maximum Injection Pressure(psia) 3600 Temperature,°F 134.5 Salinity, ppm 100000
Summary of input data for base case Frio 2 simulations
5400 sand
Lower C sand
Length,ft 3520 3870 Width,ft 2300 2520 Dip, Degree 5-35 15 Thickness,ft 60 150 Number of blocks 43*28*26 43*28*15 Depth at top of formation at injection well,ft 5350 5050 Vertical to horizontal Perm. Ratio 0.1 0.1 Average horizontal permeability,md ~2000 ~100 Average vertical permeability,md ~200 ~10 Average porosity ~0.30 ~0.30 Initial Pressure, psia 2196 2196 Residual Water Saturation 0.25 0.25 Residual Gas Saturation 0.25 0.25 Maximum Injection Pressure(psia) 3600 3600 Temperature,°F 134.5 134.5 Salinity, ppm 100000 100000
All cases held at constant pressure far field boundaries
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CPGE
5400 Sandstone Simulations: Effect of volume of dis charge
Gas saturation along injection plane at t = 1 week
2.365 x 10^6 cu. ft./ day 4.73 x 10^6 cu. ft. / dayInjection rate
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CPGE
5400 Sandstone Simulations: Effect of volume of dis charge
Gas saturation along injection plane at t = 1 week
4.73 x 10^6 cu. ft./ day 9.46 x 10^6 cu. ft. / dayInjection rate
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CPGE
5400 Sandstone Simulations: Effect of volume of dis charge
Gas saturation along injection plane at t = 2 weeks
2.365 x 10^6 cu. ft./ day 4.73 x 10^6 cu. ft. / dayInjection rate
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CPGE
5400 Sandstone Simulations: Effect of volume of dis charge
Gas saturation along injection plane at t = 2 weeks
4.73 x 10^6 cu. ft./ day 9.46 x 10^6 cu. ft. / dayInjection rate
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CPGE
5400 Sandstone Simulations: Effect of volume of dis charge
Gas saturation along injection plane at t = 1 month
2.365 x 10^6 cu. ft./ day 4.73 x 10^6 cu. ft. / dayInjection rate
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CPGE
0.0001
0.001
0.01
0.1
0 100,000 200,000 300,000
Pure Phase Properties Used to Model Mixed Gas/Brine System
Shown: CO 2 Solubility in Aqueous Phase at 140 °FOverall Mole Fractions are 0.15 H 2S, 0.35 CO2 and 0.50 H2O
CO
2C
once
ntra
tion
in A
queo
us P
hase
, m
ole
frac
tion
Salinity, ppm NaCl
100 psi
1,000 psi 2,000 psi 3,000 psi
5,000 psi 10,000 psi
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CPGE
High resolution simulations indicate that buoyancy-driven instabilities do not dominate
Pure CO2 Injected for 50 Years in Bottom Half of AquiferThen 10000 y Gravity-Driven Flow
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CPGE
Gas Saturation Profile at 10,000 Years for Coarse Grid Case (Base Case)
Pure CO2 Injected for 50 Years in Bottom Half of Aquifer
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CPGE
Conclusions
• Collaboration with CMG has been fruitful- Augmented reservoir simulation capability in place
(GEM-GHG)- Tuned equation of state, transport properties,
geochemistry- Full multiphase petrophysical properties necessary
for aquifer storage simulations- Basis for coupling reservoir to compartment
models of leakage• Important tool for research, design
- Permanent storage of CO2 in aquifers is feasible- Exploits buoyancy-driven flow
• Residual saturation• Dissolution in brine
- Evaluate tradeoffs for site selection, leakage riskassessment
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CPGE
Future Work (2)
• Structural traps within range of plume travel- Sealing faults- Anticlines- Criteria for avoiding gas
cap accumulation• Incorporate fine-scale
behavior as needed• Effect of background brine
flow
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CPGE
Future Work (3)
• Optimize combined EOR/storage
Single stage injection/production
well pair
Three stage injection/production
well pair