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CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Status and advances within EOR modeling
Arne Skauge
CIPR, Uni Research
EOR Process modeling
26.05.14 Måltidets Hus
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Conclusion - EOR simulation
Detailed mechanistic EOR models can be performed on cross-section models or idealized sector models BUT CARE SHOULD BE USED WITH FULL FIELD MODELS (Grid block size, well controls, etc)
Surfactant Polymer Water Oil
• Surfactant
• Polymer
• Alkaline
• Foam
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Simulator
type
Processes
modelled
Degree
of
difficulty
Relative
computing
costs
Amount of
Industrial
Experience
Example
references2
Black Oil
Model
- Primary
depletion
-Waterflooding
-Immiscible gas
injection
- Imbibition
Routine Cheap = 1 - huge
- but there are
still challenges
with upscaling
of large models
- >90% of cases
Any of the books on
reservoir simulation
listed in Section 1.7
Composit-
ional Model
- Gas injection
- gas recycling
-CO2 injection
- WAG
Difficult
Specialised
Expensive
(x3 - x20)
- moderate
- high in certain
companies
Coats, (1980a), Acs et
al (1985), Nolen
(1973), Watts (1986),
Young and Stephenson
(1983).
Composit-
ional Model
- Near Crit.
- gas injection
near crit.
- condensate
development
- MWAG
Difficult Very
expensive
(x5 - x30)
- low to
moderate
as above
Comparison of field experience with various types of simulation model
(after Mattax and Dalton, 1990)
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Simulator
type
Processes
modelled
Degree
of
difficulty
Relative
computing
costs
Amount of
Industrial
Experience
Example
references2
Continued
Chemical
Model -
Polymer
- polymer
flooding
- near-well
water shut-off
Not too
difficult
Moderate
(x2 - x5)
- moderate to
large
Bondor et al (1972),
Vela et al (1976),
Sorbie (1991)
Chemical
Model -
Surfactant
- micellar
flooding
-low tension
polymer
flooding
Difficult
Specialisd
Expensive
(x5 - x20)
- low
- mainly
"research type"
pilot floods
Todd and Chase
(1979), Todd et al
(1978), Van Quy and
Labrid (1983); Pope
and Nelson (1978)
Thermal
Model -
Steam
-steam soak
(Huff n' Puff)
- steam
flooding
Not too
difficult
Expensive
(x3 - x10)
- moderate
- high in limited
geographical
areas
Coats (1978),
Prats (1982),
Mathews (1983)
Thermal
Model -
In Situ
Combustion
- in situ
combustion
processes
Very
difficult
Very
specialised
Expensive
(x10 - x40)
- very low Crookston et al (1979),
Youngren (1980),
Coats (1980b)
after Mattax and Dalton, 1990
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
2006
New processes
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Eclipse Low Salinity Model
• Two sets of relative permeability curves.
Hri
Lriri kFkFk 11 1
Hml
Lmlml SFSFS ,1,1, 1
cowH
cowL
cow PFPFP )1( 22
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Oil Recovery Berea Core 8 - syntetic brine waterflood
0
10
20
30
40
50
60
0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 5 5.5
Volume Injected [PV]
Oil
Re
cov
ery
[%
]
Experimental result
UTCHEM Match
Oil Recovery Berea Core 2 Low Salinity Injection
0
10
20
30
40
50
60
70
0 1 2 3 4 5
PV injected
Oil
Re
cov
ery
[%
]
Experimental result
UTCHEM
Relative permeability curves
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 0.7 0.8
Water saturation
Relat
ive pe
rmea
bility
Initial
Wettability altered
OILWATER
HS LS
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Sensitivity tests on the rel perm
F1 - factor
Salt concentration (g/cc)
Hri
Lriri kFkFk 11 1
Dependency on local salt concentration
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Well
block
Near
well
Center
part
Near
well
Well
block
Standard 1 10 98 10 1
Coarse grid 1 5 14 5 1
0
0.002
0.004
0.006
0.008
0.01
0.012
0 2 4 6 8 10 12 14 16 18 20
PV injected
Na
+ (
gr/c
c)
Experimental data
Model results (ECL)
Physical dispersion – numerical dispersion
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Dispersitivity
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Nano particle EOR
Example another new process
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Estimation LPS flow functions from by history matching core floods
• Matching waterflood response (Sendra) • LPS match by ECL-200
0
5
10
15
20
25
30
35
40
0 1000 2000 3000 4000 5000 6000 7000 8000
Time
Delt
a P
0
0.05
0.1
0.15
0.2
0.25
0.3
0.35
0.4
0.45
0.5
Oil P
rod
ucti
on
Core OP Matched DP Core DP Matched OP
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Estimation LPS flow functions from by history matching core floods
• Estimated rel perms before and after LPS
Increased oil perm
Reduced water perm
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Network Model Challenges
• In traditional Network Model, residual oil at the end of imbibition can not be mobilized
• Modeling EOR processes requires movement of trapped oil
• Quasi static networks are stable but are not designed to consider viscous forces
• Dynamic networks are potentially a good alternative for EOR processes but their estimation of fluid flow is not reliable enough
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Our Approach
• Our approach includes Double displacement of fluids to mobilize trapped oil
• It also includes the combination of invasion percolation model with one-phase dynamic network model.
• The dynamic network is necessary because efficiency of many EOR processes like polymer injection, surfactant and etc depend strongly on concentration. The concentration should be evaluated in dynamic basis.
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Relperm derived from core flow data and network models
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Some Results of LPS injection in a network model
0.25
0.3
0.35
0.4
0.45
0 5 10 15 20
LPS Slug Number [-]
So
r [-
]
Sor
Parameter Value Unit
Network Size 15x15x15 Node
Pore Size 2.4 - 20 μm
Coordination Number 4.02 -
Pore-throat Length 0.8 - 1.12 mm
Porosity 31.02 %
Absolute Permeability 924 mD
Interfacial Tension 41 mN/m
Initial Contact Angle 0.8 - 1.0 Cos( θ )
Wettability Class (After Ageing) Mixed Wet
Large -
Oil Wet Contact Angle (After
Ageing) (-0.2) - (-0.8) Cos(θ)
Water Wet Contact Angle (After
Ageing) 0.1 - 0.3 Cos(θ)
Largest Water Radius/Smallest
Oil Radius (Rwet) 15 μm
MWL
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Possibility for visualisation of blocking and oil mobilisation
• Strongly water-wet pores – Driving force for spontaneous imbibition in the smallest pores
• Weakly oil-wet pores give low entry pressure for displacement of oil by water
0
100
200
300
400
500
600
700
3.3
4.2
5.1
5.9
6.8
7.7
8.6
9.5
10.3
11.2
12.1
13.0
13.8
14.7
15.6
16.5
17.4
18.2
19.1
20.0
radius [μm]
bo
nd
s [
-]
PSD
Blocked
Water- wet Oil- wet
0
100
200
300
400
500
600
700
3.3
4.2
5.1
5.9
6.8
7.7
8.6
9.5
10.3
11.2
12.1
13.0
13.8
14.7
15.6
16.5
17.4
18.2
19.1
20.0
radius [μm]
bo
nd
s [
-]
PSD
LPS start
LPS endWater- wet Oil- wet
MWL
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
other issues
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
The type of reservoir simulation that becomes more possible with parallel processing. Ex. fine grid and megacell simulation which identifies the scale of remaining oil in a reservoir displacement process; (Dogru, SPE57907, 2000).
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
+ polymer injectivity
Polymer flooding
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Five-Spot Areal Sweep...
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Viscous Fingering in a Quarter Five-spot Model, Mo = 17
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Theory and Background Mobility Ratio
(Habermann 1960)
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Waterflood at adverse mobility ratio (heavy oil)
Skauge et al., SPE 154292
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Development of viscous fingers
• Heterogeneity
• Oil Viscosity
• Capillary Pressure
• Relative Permeability
• Rate
• Finer Grid
• Higher Order Flux
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
CO2 sequestration
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Dissolution
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
SCALES
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
FOAM Simulations
The sensitivity of the simulated foam response
to variations in the foam parameters was studied:
· Surfactant adsorption on the rock (+ reversability)
· Critical surfactant conc. to generate reference foam strength
· Foam drying effect
· Foam strength - MRF
MRF as distance from injector Gas mobility reduction by foam in the top S1 layer
Modelling of FAWAG on Snorre
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Best history match
The best match of the first surfactant slug was achieved with 50 MRF
foam and 100 MRF foam for the second surfactant slug, when foam
drying effect was switched off
Skauge et al., SPE 75157
No foam
MRF=100
WAG Foam
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
0
10
20
30
40
50
60
70
80
90
100
0 1 2 3 4 5 6 7 8 9 10 11 12 13PV injected
Oil
Reco
very
[%]
Experimental Data Best Fit LS-S flood on Core B2
Experimental results: Alagic and Skauge, 2009 Simulation results: Skauge, Ghorbani, Delshad, 2011
Low salinity + surfactant Hybrid processes
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
S6-S7:4-weeks aged Berea cores
0
10
20
30
40
50
60
70
80
90
100
0 5 10 15 20 25
Volume Injected (PV)
Oil
pro
du
ctio
n (
% O
OIP
)
Low Sal 300 ppm polymer
0
10
20
30
40
50
60
70
80
90
100
0 1 2 3 4 5 6 7 8 9 10 11 12 13PV injected
Oil
Re
cov
ery
[%
]
Experimental Data Best Fit LS-S flood on Core B2
Experimental results: Alagic and Skauge, 2009 Simulation results: Skauge, Ghorbani, Delshad, 2011
Low salinity in combination with other EOR processes
Shiran and Skauge, 2012
Low salinity + surfactant Low salinity + polymer
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Final comments
We have a lot of mechanistic tools to model EOR processes Example: MEOR – key mechanisms uncertain, but lower IFT, build up of viscous phases etc., are available FOAM – lot of mechanisms available for history matching, but frontal advance uncertain Surfactant, ASP, detailed mechanisms available, but upscaling is often difficult Low salinity – mechanisms uncertain, but modeling tools seems adequate for history matching upscaling may be influenced by grid resolution (numerical dispersion) Polymer – mature EOR process, but still some issues to be further developed influence of viscoelasticity, injectivity, etc. (unstable waterflood has to be modelled correctly prior to polymer injection Miscible gas – errors often done on extrapolations towards miscibility WAG – combined compositional effect and hysteresis yet to be jointly included in commercial codes
CIPR – Center for Integrated Petroleum Research, Bergen, Norway
Further comments Too simplified models may not show the potential of the EOR process Known and important physical mechanisms should be respected in the simulation Simulations should be made on controllable models and avoid large grid blocks Cross-sections and/or sector models including key-process EOR mechanisms is the best way of quantifying the potential
CIPR – Center for Integrated Petroleum Research, Bergen, Norway