Multiphase flow modelling of calcite dissolution patterns from core scale to reservoir scale - Jeroen Snippe, Shell, at UKCCSRC specialist meeting Flow and Transport for CO2 Storage, 29-30 October 2015
Multiphase flow modelling of calcite dissolution patterns from core scale to reservoir scale - Jeroen Snippe, Shell, at UKCCSRC specialist meeting Flow and Transport for CO2 Storage, 29-30 October 2015
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Multiphase flow modelling of calcite dissolution patterns from core scale to reservoir scale - Jeroen Snippe, Shell, at UKCCSRC specialist meeting Flow and Transport for CO2 Storage, 29-30 October 2015
1. Copyright of Shell Global Solutions International B.V.
MULTIPHASE FLOW MODELLING OF
CALCITE DISSOLUTION PATTERNS FROM
CORE SCALE TO RESERVOIR SCALE
Jeroen Snippe, Holger Ott
Shell Global Solutions International B.V.
1October 2015
Presentation for UKCCSRC
Specialist Meeting on Flow and
Transport for CO2 Storage
Imperial College London,
30th October 2015
2. Copyright of Shell Global Solutions International B.V.
DEFINITIONS & CAUTIONARY NOTE
Reserves: Our use of the term “reserves” in this presentation means SEC proved oil and gas reserves.
Resources: Our use of the term “resources” in this presentation includes quantities of oil and gas not yet classified as SEC proved oil and gas reserves. Resources are consistent with
the Society of Petroleum Engineers 2P and 2C definitions.
Organic: Our use of the term Organic includes SEC proved oil and gas reserves excluding changes resulting from acquisitions, divestments and year-average pricing impact.
Resources plays: Our use of the term ‘resources plays’ refers to tight, shale and coal bed methane oil and gas acreage.
The companies in which Royal Dutch Shell plc directly and indirectly owns investments are separate entities. In this presentation “Shell”, “Shell group” and “Royal Dutch Shell” are
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subsidiaries in general or to those who work for them. These expressions are also used where no useful purpose is served by identifying the particular company or companies.
‘‘Subsidiaries’’, “Shell subsidiaries” and “Shell companies” as used in this presentation refer to companies in which Royal Dutch Shell either directly or indirectly has control.
Companies over which Shell has joint control are generally referred to as “joint ventures” and companies over which Shell has significant influence but neither control nor joint control
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company, after exclusion of all third-party interest.
This presentation contains forward-looking statements concerning the financial condition, results of operations and businesses of Royal Dutch Shell. All statements other than statements
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‘‘risks’’, ‘‘goals’’, ‘‘should’’ and similar terms and phrases. There are a number of factors that could affect the future operations of Royal Dutch Shell and could cause those results to
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expropriation and renegotiation of the terms of contracts with governmental entities, delays or advancements in the approval of projects and delays in the reimbursement for shared
costs; and (m) changes in trading conditions. All forward-looking statements contained in this presentation are expressly qualified in their entirety by the cautionary statements
contained or referred to in this section. Readers should not place undue reliance on forward-looking statements. Additional factors that may affect future results are contained in Royal
Dutch Shell’s 20-F for the year ended 31 December, 2014 (available at www.shell.com/investor and www.sec.gov ). These factors also should be considered by the reader. Each
forward-looking statement speaks only as of the date of this presentation, 2 October, 2015. Neither Royal Dutch Shell nor any of its subsidiaries undertake any obligation to publicly
update or revise any forward-looking statement as a result of new information, future events or other information. In light of these risks, results could differ materially from those stated,
implied or inferred from the forward-looking statements contained in this presentation. There can be no assurance that dividend payments will match or exceed those set out in this
presentation in the future, or that they will be made at all.
We use certain terms in this presentation, such as discovery potential, that the United States Securities and Exchange Commission (SEC) guidelines strictly prohibit us from including in
filings with the SEC. U.S. Investors are urged to consider closely the disclosure in our Form 20-F, File No 1-32575, available on the SEC website www.sec.gov. You can also obtain
this form from the SEC by calling 1-800-SEC-0330.
October 2015
3. Copyright of Shell Global Solutions International B.V.
INTRO: CALCITE DISSOLUTION DURING CO2 INJECTION
Context: CO2 storage/EOR
CO2 injection → acidification →
carbonate dissolution
3October 2015
Fred and Fogler (1999), SPE 56995
Experiments show ‘wormholing’
for CO2 -saturated brine injection
Similar to patterns in extensive
acid stimulation literature
Very limited experimental work
done with gas/SC CO2 injection
Model investigation
Impact of gas phase
Upscaling to field scale
4. Copyright of Shell Global Solutions International B.V.
MODELLING APPROACH
Using in-house dynamic multiphase reservoir flow simulator (MoReS)
coupled to open-source geochemical package (PHREEQC v3)
4October 2015
Detailed model (core scale)
Explicit representation of WH patterns
Grid resolution << WH diameter
Chemistry including kinetics (phreeqc.dat, Palandri & Kharaka)
2-phase flow description including capillary effects and diffusion
Permeability, capillary pressure, relperms modified during dissolution
Continuum scale (Darcy) model → flow within WH approximate
Effective model (core scale to well/reservoir scale) [2nd part of presentation]
Implicit representation of WH patterns
Generalised to 2-phase case with CO2
Parameters tuned to detailed model and experiments
5. Copyright of Shell Global Solutions International B.V.
DETAILED MODEL
5October 2015
6. Copyright of Shell Global Solutions International B.V.
3D
SOME MODEL RESULTS (SINGLE PHASE)
6October 2015
WH competition 5mm…
Most of fine-scale simulations done in 2D
Compact dissolution Conical dissolution Conical wormhole
Ramified wormholes Homogeneous dissol.Dominant wormhole
2D
WH width 2 mm
7. Copyright of Shell Global Solutions International B.V.
MODEL VALIDATION (SINGLE PHASE)
7October 2015
Ramified wormholes
Uniform dissolution
Dominant wormhole
Conical
wormhole
Compact
dissolution
Dahmkohlernumber(reactionrate/convectionrate)
Peclet number (convection rate/diffusion rate)
MoReS results (colour) plotted on domain boundaries from
Golfier et al., J. Fluid Mech. (2002), vol. 457, pp. 213-254
with experimental patterns from Fred and Fogler (1999), SPE 56995
8. Copyright of Shell Global Solutions International B.V.
TWO-PHASE EXPERIMENT/MODEL RATIONALE
Experiment
Two experiments were done at Shell with CO2 + brine co-injection
This is ~representative for the conditions somewhat behind the CO2
plume front in CCS
Pure CO2 injection WH experiment would be more challenging
longer core to resolve profiles (gas saturation, calcite dissolution)
high CT signal:noise to resolve subtle calcite dissolution patterns
Model:
Model experiment with CO2 + brine co-injection and compare results
Derive upscaled (effective) model description
Apply effective model to pure CO2 injection (larger model dimensions)
8October 2015
9. Copyright of Shell Global Solutions International B.V.
2-PHASE RELPERM AND CAPILLARY PRESSURE
9October 2015
During dissolution
Interpolation between curves (linear in porosity)
Power law scaling of permeability with porosity
0.0
1.5
3.0
0.00
0.25
0.50
0.75
1.00
0.00 0.25 0.50 0.75 1.00
Capillarypressure(Gas-Water)[bar]
Relativepermeability
Gas saturation
krw matrix
krg matrix
krw cavity
krg cavity
Pc matrix
Pc cavity
10. Copyright of Shell Global Solutions International B.V.
TWO-PHASE MODEL RESULTS (CO-INJECTION)
10October 2015
The gas phase slightly suppresses WH velocity
260 PV
single-phase two-phase co-injection (same rate)
720 PV
560 PV
760 PV
760 PV
2000 PV
260 PV
880 PV
760 PV
880 PV
760 PV
2000 PV
11. Copyright of Shell Global Solutions International B.V.
1
10
100
1000
10000
0.001 0.010 0.100 1.000 10.000 100.000
PoreVolumestoBreakthrough
Interstitial Water Velocity (cm/min)
Brine + gas
Observed
TWO-PHASE MODEL RESULTS (CO-INJECTION)
11October 2015
Most suppression around optimal flow rates (~dominant WH regime)
12. Copyright of Shell Global Solutions International B.V.
TWO-PHASE MODEL RESULTS: ANALYSIS/COMPARISON
12October 2015
2-phase, 1+1 ml/min co-inj.1-phase, 1ml/min
Porosity
Experiment
(Shell)
(Porosity)
Ott et al. (2013)
SCA2013-029
Gas
saturation
Water flux
(log scale)
760 PV 880 PV
13. Copyright of Shell Global Solutions International B.V.
Ott, H., and S. Oedai (2015)
Geophys. Res. Lett., 42, 2270–2276
doi:10.1002/2015GL063582
2ND SHELL EXPERIMENT: WH SUPPRESSION
In this experiment gas co-injection seems to trigger transition from
dominant WH into conical WH/compact dissolution
Slumping reproduced in model runs with gravity (only investigated on
small diameter core)
13October 2015
14. Copyright of Shell Global Solutions International B.V.
EFFECTIVE MODEL APPROACH
14October 2015
15. Copyright of Shell Global Solutions International B.V.
LEARNINGS FROM ACID STIMULATION LITERATURE
15August 2015
Acid stimulation literature
(single phase): Universally
shaped curve #PVBT vs vi (or
vWH vs vi)
Location of curve depends on
phi, perm, aspect ratio, HCl
strength, …
‘Global Wormholing Model’
(GWM), Talbot&Gdanski
(2008), SPE 113042, offers
~universal parameterisation
~predictive vWH vs vi for given
phi, perm, HCl strength, etc.
Buijse & Glasbergen
(2005), SPE 96892
16. Copyright of Shell Global Solutions International B.V.
GWM CHARACTERISTICS
16October 2015
Talbot&Gdanski (2008),
SPE 113042
17. Copyright of Shell Global Solutions International B.V.
1
10
100
1000
10000
0.001 0.010 0.100 1.000 10.000 100.000 1000.000
PoreVolumestoBreakthrough
Interstitial Water Velocity (cm/min)
Brine + gas Observed
compact dissolution limit Model (fit)
Model (solubility-equivalent HCl) Model (pH-equivalent HCl)
GWM APPLICATION TO CO2-BRINE
17August 2015
Deviation in single
WH regime because
Poiseuille flow profile
in model poorly
resolved or grid
resolution too coarse
Model was run in 2D,
for which GWM
model is overshooting
in face dissolution
regime
GWM model fitted by tuning HCl strength
Resulting GWM model also fits available experimental data well (next slides)
GWM model applied to dynamic flow simulations by locally accounting for
calcite saturation index through HCl strength parameter
For 2-phase use same GWM parameters – use the water vi as input velocity
18. Copyright of Shell Global Solutions International B.V.
1
10
100
1000
10000
0.001 0.01 0.1 1 10 100 1000
PoreVolumestoBreakthrough
Interstitial Fluid Velocity (cm/min)
Model Observed
FITTED MODEL COMPARISON TO EXPERIMENTS
OTT ET AL. (SHELL) 2013 – SCA 2013-029
18October 2015
L=5.91”, d=2.95”
q=1 mL/min
Estaillades limestone
φ=0.278, k=270 mD
T=50 °C, p=100 bar
19. Copyright of Shell Global Solutions International B.V.
1
10
100
1000
10000
0.001 0.01 0.1 1 10 100 1000
PoreVolumestoBreakthrough
Interstitial Fluid Velocity (cm/min)
Model Observed
FITTED MODEL COMPARISON TO EXPERIMENTS
CAROLL ET AL. (LLNL) 2013 - IJGHGC 16S (2013) S185–S193
19October 2015
L=1.18”, d=0.59”
q=0.05 mL/min
Calculated HCl equivalent based on undersaturated CO2 molality
Weyburn limestone (59% calcite)
φ=0.15, k=0.032 mD
T=60 °C, p=248 bar, p_CO2 = 30 bar
20. Copyright of Shell Global Solutions International B.V.
1
10
100
1000
10000
0.001 0.01 0.1 1 10 100 1000
PoreVolumestoBreakthrough
Interstitial Fluid Velocity (cm/min)
Model Observed
FITTED MODEL COMPARISON TO EXPERIMENTS
VIALLE ET AL. 2014 - J. GEOPHYS. RES. SOLID EARTH, 119, 2828–2847
20October 2015
L=0.13.8”, d=3.94”
q=5 mL/min
Salinity = 25000 ppm
Calculated HCl equivalent based on undersaturated CO2 molality
Estaillades limestone
φ=0.286, k=120 mD
T=20 °C, p_CO2 = 1 bar
21. Copyright of Shell Global Solutions International B.V.
1
10
100
1000
10000
0.001 0.01 0.1 1 10 100 1000
PoreVolumestoBreakthrough
Interstitial Fluid Velocity (cm/min)
Model Observed
FITTED MODEL COMPARISON TO EXPERIMENTS
LUQUOT ET AL. 2011 - TRANSP POROUS MED (2014) 101:507–532
21October 2015
L=0.71”, d=0.35”
q=0.08 mL/min
Calculated HCl equivalent based on undersaturated CO2 molality
Alcobaa limestone
φ=0.15, k=0.24 mD
T=100 °C, p=120 bar, p_CO2 = 34 bar
22. Copyright of Shell Global Solutions International B.V.
1
10
100
1000
10000
0.001 0.01 0.1 1 10 100 1000
PoreVolumestoBreakthrough
Interstitial Fluid Velocity (cm/min)
Model Observed
FITTED MODEL COMPARISON TO EXPERIMENTS
SVEC & GRIGG 2001 - SPE 71496
22October 2015
L=20.3”, d=1.98”
q=17 mL/min
Indiana limestone
φ=0.123, k=35.7 mD
T=38 °C, p=138 bar
Salinity=86950 ppm
23. Copyright of Shell Global Solutions International B.V.
1
10
100
1000
10000
0.001 0.01 0.1 1 10 100 1000
PoreVolumestoBreakthrough
Interstitial Fluid Velocity (cm/min)
Model Observed
FITTED MODEL COMPARISON TO EXPERIMENTS
LUQUOT & GOUZE 2009 - CHEMICAL GEOLOGY 265 (2009) 148–159
23October 2015
L=0.71”, d=0.35”
q=1.14 mL/min
Mondeville limestone
φ=0.075, k=35.7 mD
T=100 °C, p=120 bar, p_CO2 = 100 bar
24. Copyright of Shell Global Solutions International B.V.
1
10
100
1000
10000
0.001 0.01 0.1 1 10 100 1000
PoreVolumestoBreakthrough
Interstitial Fluid Velocity (cm/min)
Model Observed
FITTED MODEL COMPARISON TO EXPERIMENTS
MENKE 2015 - IMPERIAL COLLEGE LONDON – PRIVATE COMM
24October 2015
L=0.47”, d=0.16”
q=0.5 mL/min
Salinity = 60000 ppm
Portland limestone
φ=0.045, k=0.096 mD
T=50 °C, p=100 bar
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∆ Pressure
Reference case: no WH’s
EFFECTIVE MODEL RESULTS (LINEAR MODEL, 1METER)
CO2-saturated brine injection: Potential for large injectivity increase
Pure CO2 injection: Short/no wormholes. Negligible impact on injectivity
25October 2015
Pure CO2 injection (1cm/min)CO2-sat brine injection (1cm/min)
WH velocity
Gas saturation
WH length
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EFFECTIVE MODEL RESULTS (RADIAL MODEL, R=50 METER)
26October 2015
Pure CO2 injection (0.5 MT/year)CO2-sat brine injection (0.5 MT/year)
Gas saturation
Injection pressure
Reference case: no WH’s
WH length
Same conclusions as for linear model
Note for pure CO2 injection: WH length decreases with distance (cf. linear: ~constant)
27. Copyright of Shell Global Solutions International B.V.
ANALYSIS OF RESULTS (RADIAL MODEL)
27October 2015
0.000001
0.000010
0.000100
0.001000
0.010000
0.100000
0.0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1.0
0 100 200 300 400 500 600
WHvelocity(cm/min),WHlength(cm),
porositychange(m3/m3),permmult-1
gassaturation(m3/m3)
Radial distance (cm)
SAT_GAS
Vwh
Lwh
DPHI
PERMX_MULT -1
0.000001
0.000010
0.000100
0.001000
0.010000
0.100000
0.0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1.0
300 320 340 360 380 400
WHvelocity(cm/min),WHlength(cm),
porositychange(m3/m3),permmult-1
gassaturation(m3/m3)
Radial distance (cm)
SAT_GAS
Vwh
Lwh
DPHI
PERMX_MULT -1
Only thin region in which conditions are favourable for WH growth
Far ahead of gas front gradual increase in acidity → always close to calcite
equillibrium → outside WH regime (too low Da#)
Note: calcite solubility in CO2-saturated brine controls final porosity change
28. Copyright of Shell Global Solutions International B.V.
1
10
100
1000
10000
0.001 0.01 0.1 1 10 100 1000
PoreVolumestoBreakthrough
Interstitial Fluid Velocity (cm/min)
Base case
Vi -> 0 (ideal compact dissol)
L/A=2
L/A = .67
T=-65
T=30
T=50
HCl=.002617
HCl=.05
HCl=.238
Estaillades exp (L/A = .34)
Model 2D (L/A=15)
best fit to 9.8 cm2/g MoReS
SENSITIVITY TO GWM PARAMETER UNCERTAINTY RANGE
28October 2015
Parameter ranges based on (wide) envelope around
experimental and model results
For radial application, base case L/A ≈1cm-1 based on acid
stimulation radial corefloods and field application experience
29. Copyright of Shell Global Solutions International B.V.
SENSITIVITY RESULTS: IMPACT ON WH LENGTH (1-PHASE)
29October 2015
0
100
200
300
400
500
600
700
800
900
1,000
0 20 40 60 80 100
Wormholelength(cm)
Distance from sandface (cm)
ref case HCld238 HCld005 LdAd67
LdA2 Tm30 T50
Strong sensitivity, especially to acid strength parameter
In all cases strong wormhole growth initiating at sandface
Hypothetical WH’s initiating ahead of sandface overtaken (shock front)
After several months of injection
30. Copyright of Shell Global Solutions International B.V.
Weaker sensitivities than in 1-phase case
Conclusions from reference case run appear robust, i.e.: short/no
wormholes (LWH < 0.05 cm)
perm multiplier < 1.01 for LWH < 5cm (2D) or 2cm (3D) [next slides]
SENSITIVITY RESULTS: IMPACT ON WH LENGTH (2-PHASE)
30October 2015
0.000
0.010
0.020
0.030
0.040
0.050
0.060
0 100 200 300 400 500
Wormholelength(cm)
Distance from sandface (cm)
ref case HCld238 HCld005 LdAd67
LdA2 Tm30 T50
31. Copyright of Shell Global Solutions International B.V.
REMARK ON EFFECTIVE PERMEABILITY MULTIPLIER
In pure CO2 injection case WH’s would
initiate away from sandface
Q: how assign effective perm?
Matrix background and high perm
WH channels
Assume random WH initiation pattern
Assume idealised dominant WH’s
Straight channel WH = 2mm
From Poiseuille flow, kWH ≈ 105 D
Control parameters ∆φ and LWH
Considered both 2D and 3D
Considered enhanced connectivity case
(~ WH angle distribution/bifurcations)
31October 2015
32. Copyright of Shell Global Solutions International B.V.
Numerical upscaling
Simple formula gives good fit, for all ∆φ , all LWH, all perm contrasts
𝑘 𝑒𝑓𝑓
𝑘 𝑚
− 1 =
𝑘 𝑔𝑒𝑜𝑚(∆φ)
𝑘 𝑚
− 1
𝐿 𝑊𝐻
𝑐1
𝑐2
(+bounded by harm and arithm)
REMARK ON EFFECTIVE PERMEABILITY MULTIPLIER
32October 2015
1.E-06
1.E-05
1.E-04
1.E-03
1.E-02
1.E-01
1.E+00
1.E+01
1.E+02
1.E+03
1.E+04
1.E+05
1.E+06
1.E-06 1.E-05 1.E-04 1.E-03 1.E-02 1.E-01 1.E+00
k_mult_harm - 1
k_mult_geom - 1
k_mult_arithm - 1
WH_kmult1Min1
WH_kmult2Min1
Fit
1.E-06
1.E-05
1.E-04
1.E-03
1.E-02
1.E-01
1.E+00
1.E+01
1.E+02
1.E+03
1.E+04
1.E+05
1.E+06
1.E-06 1.E-05 1.E-04 1.E-03 1.E-02 1.E-01 1.E+00
k_mult_harm - 1
k_mult_geom - 1
k_mult_arithm - 1
WH_kmult1Min1
WH_kmult2Min1
Fit
1.E-06
1.E-05
1.E-04
1.E-03
1.E-02
1.E-01
1.E+00
1.E+01
1.E+02
1.E+03
1.E+04
1.E+05
1.E+06
1.E-06 1.E-05 1.E-04 1.E-03 1.E-02 1.E-01 1.E+00
k_mult_harm - 1
k_mult_geom - 1
k_mult_arithm - 1
WH_kmult1Min1
WH_kmult2Min1
Series7
Example - perm contrast
𝑘 𝑊𝐻
𝑘 𝑚
= 400, LWH =100mm
log(∆φ)
log
𝐤𝐖𝐇
𝐤𝐦
−𝟏
10-6 1
10-6
10+6
Note: for pure CO2 injection: ∆φ≈10-4
33. Copyright of Shell Global Solutions International B.V.
CONCLUSIONS
At fixed brine rate, gas co-injection causes some suppression of calcite
dissolution patterns.
Modelling indicates limited suppression for any flow rate
Experiment: limited to strong suppression in dominant/conical WH regime
33October 2015
Successfully applied effective GWM model (from acid stimulation literature)
to CO2-brine system (matches fine-scale model and experiments)
Effective model predicts WH can be significant in carbonate reservoirs on
operational timescale (days-years) for CO2 & water co-injection
Good for injectivity
Potentially problematic for well/rock stability (depending on WH pattern)
Effective model predicts negligible wormhole formation for pure CO2
injection (at any scale from core scale to reservoir scale)
WH formation irrelevant for pure CO2 injection projects (‘standard’ CCS)
34.
35. Copyright of Shell Global Solutions International B.V.
REMARK ON REACTION KINETICS VS GWM PARAMETERS
35August 2015