Martin Blunt, Branko Bijeljic, Tara C LaForce, Stefan Iglauer, Ran Qi, Saleh Al-Mansoori, Chris Pentland and Erica Thompson - PowerPoint PPT Presentation

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Martin Blunt, Branko Bijeljic, Tara C LaForce, Stefan Iglauer, Ran Qi, Saleh Al-Mansoori, Chris Pentland and Erica Thompson

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Title: Martin Blunt, Branko Bijeljic, Tara C LaForce, Stefan Iglauer, Ran Qi, Saleh Al-Mansoori, Chris Pentland and Erica Thompson


1
Impact of capillary trapping on geological
CO2 storage
  • Martin Blunt, Branko Bijeljic, Tara C LaForce,
    Stefan Iglauer, Ran Qi, Saleh Al-Mansoori, Chris
    Pentland and Erica Thompson

2
Outline
  • Field scale Streamline Simulation
  • Core scale Column Experiment
  • Pore scale CT scan

3
Background
  • Long term fate, how can you be sure that the CO2
    stays underground?

4
Field scale - The streamline method
5
Streamline method for CO2 transport
6
Streamline method for CO2 transport
  • Trapping model
  • Pore-scale model matches experimental data.
  • Kr is from Berea sandstone, which matches Oak
    (1990)s
  • experiments.
  • CO2/water system is weakly water-wet (Chiquet et
    al., 2007)
  • contact angle (?) 65º.
  • New trapping model (Juanes et al., 2006)

7
Design of carbon dioxide storage
The ratio of the mobility of injected brine and
CO2 to the formation brine as a function of the
injected CO2-phase volume fraction, fgi.
8
Design of carbon dioxide storage
  • 1D analysis Numerical simulation vs. analytical
    solution

9
Design of carbon dioxide storage
10
Design of carbon dioxide storage
  • 3D simulation Storage efficiency vs. trapping
    efficiency

Trapping efficiency the fraction of the
injected mass of CO2 that is either trapped or
dissolved
Storage efficiency the fraction of the
reservoir pore volume filled with CO2
The storage efficiency is highest for fgi 0.85,
which also requires minimum mass of chase brine
to trap 95 of CO2.
11
Design Criterion
  • Inject CO2brine where mobility ratio 1.0
  • (fgi0.85 in this example).
  • Inject chase brine that is 25 of the initially
    injected CO2 mass.
  • 90-95 of the CO2 is trapped.

12
Issues arising from field scale simulation
  • Streamline-based simulator has been extended to
    model CO2 storage in aquifers and oil reservoir
    by incorporating a Todd-Longstaff model,
    equilibrium transfer between phases (dissolution)
    and rate-limited reaction
  • Trapping is an important mechanism to store CO2
    as an immobile phase. Our study showed that WAG
    CO2 injection into aquifer can trap more than 90
    of the CO2 injected
  • We have proposed a design strategy for CO2
    storage in aquifers, in which CO2 and formation
    brine are injected simultaneously followed by
    chase brine.
  • Streamline-based simulation combined with
    pore-scale network modeling can capture both the
    large-scale heterogeneity of the reservoir and
    the pore-scale effects of trapping.

13
Future work
  • Injection strategy design
  • Require better experimental data, since the
    trapping model used has a significant impact on
    the results.
  • Design of an injection strategy to maximize CO2
    storage and oil recovery.

14
CT Scanning
  • A homogeneous sandpack was compressed and the
    porosity was determined via mass balance (F
    38,93).
  • n-Heptane was injected when no more brine was
    produced, another CT scan was performed at the
    irreducible water saturation, Swi.
  • CO2 was injected again. Gas injection was stopped
    when no more liquid production was observed.
    Another CT scan was taken.
  • 30 pore volumes (PV) of brine were injected and a
    final CT scan was taken at the residual gas
    saturation Sgr .
  • resolution 9 µm

15
Sandpack at irreducible water saturation
Brine blue Sand red Oil - orange
  • Oil penetrates on average mainly into the larger
  • pores as expected by capillary pressure
  • considerations.
  • Thin water layer is visible on the rock surface
    as
  • expected for quartz.
  • Oil has penetrated into the middle of some
    pores.

16
Sandpack at residual gas saturation
Brine blue Sand red CO2 - yellow
  • The largest CO2 ganglia is continuously spread
    over the
  • largest available pore.
  • Though overall gas accumulates in the larger
    pores, a random
  • distribution between large and medium size
    pores is
  • observable.
  • Several tiny gas bubbles are randomly
    distributed in
  • the pore volume. Though they might originate
    from
  • the segmentation process, it is thought that
    they are real.

17
Vertical column experiments Sor vs. Soi
  • Sand-packed columns were oriented vertically.
  • 5 pore volumes of de-aired brine were injected to
    reach full saturation.
  • Decane reservoir connected to top of columns and
    brine allowed to drain under gravity from the
    base. Decane enters the top of the column. No
    pumping.
  • Equilibrium reached where both columns have a
    (theoretically) identical oil saturation profile
    versus height.
  • One column removed for slicing and sampling
    Soi.
  • Second column has brine injected from the base,
    Brine sweeps oil leaving an Sor. Coulmn sliced
    and sampled.

18
Vertical column experiments Sor vs. Soi -
results
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