Modelling multiphase flow through micro-CT images of the pore space

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Modelling multiphase flow through micro-CT images of the pore space Department of Earth Science and Engineering Imperial College Consortium on Pore-scale Modelling Ali Raeini, Branko Bijeljic and Martin Blunt

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Modelling multiphase flow through micro-CT images of the pore space. Ali Raeini , Branko Bijeljic and Martin Blunt. Department of Earth Science and Engineering Imperial College Consortium on Pore-scale Modelling. Objective. Relative permeability. Micro-CT image. - PowerPoint PPT Presentation

Transcript of Modelling multiphase flow through micro-CT images of the pore space

Page 1: Modelling multiphase flow through micro-CT images of the pore space

Modelling multiphase flow through micro-CT images of the pore space

Department of Earth Science and EngineeringImperial College Consortium on Pore-scale Modelling

Ali Raeini, Branko Bijeljic and Martin Blunt

Page 2: Modelling multiphase flow through micro-CT images of the pore space

Objective

Micro-CT image

Capillary pressure

Relative permeability

,= ,

xPPkk

q ca

a

ara

Macroscopic description of the flow

Direct numerical simulation

Microscopic description of flow

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Capillary pressure

Relative permeability

Previous studies

Pore network model

Pore network

modelling

Micro-CT

image

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Capillary pressure

Relative permeability

Methodology

Numerical

Simulation

Micro-CT

imageFinite

volume mesh

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Governing equations

Capillary pressure equation

Mass balance

Momentum balance

Advection of indicator function

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Numerical code

OpenFOAM: open source CFD toolbox

interFOAM code:Discretisation of PDEs: Finite Volume MethodCapturing interface position: Volume of Fluid methodSurface tension forces: Continuous Surface Force (CSF) model

(Brackbill et al., 1992)

www.openfoam.com

+ our modifications ......

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Test cases Modelling a static droplet

Initial conditionEquilibrium

solution

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Test cases Modelling a static droplet Original CSF formulation

(m/s)

Presence of spurious velocities in CSF formulation makes the simulations impossible at low capillary numbers

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Test cases Modelling a static droplet

Sharp Surface Force (SSF) formulation

(m/s)(Pa)

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Test cases Modelling a static droplet CSF vs. SSF results

Capillary waves Spurious currents

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Jagged solid walls

Test cases Droplet in contact with a flat plate

Smooth solid walls

solid wall

(m/s)

Non-physical velocities are generated close to the jagged solid walls in both CSF and SSF formulations

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Test cases Droplet in contact with a flat plate

Filtering capillary forces parallel to the interface

(m/s)(Pa)

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CSF formulationSSF formulation

Test cases Steady movement of a micro-scale droplet

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Filtering capillary fluxes

Test cases Steady movement of a micro-scale droplet

Filtering is necessary to obtain accurate results for the velocity field

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Novel contributions in this study

Filtering capillary forces parallel to the interface

Filtering capillary fluxes

Sharp Surface Force formulation

.....

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Primarily pore-scale simulations Transient drainage experiment

,)()()(= ,

xsPsPskk

u acaa

a

aara

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Simulation time

2/14 1

xuNt

dsim

4Ntsim High Capillary Numbers

Low Capillary Numbers

3Ntsim Single-phase flow

(>10-7)

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(Pa)

(Pa)

Future work

Pd

Obtaining Capillary pressure and relative permeability curves from transient experiments

Improving the efficiency of the numerical model for low capillary numbers

Pc

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Future work

Steady two-phase flow experiments, using cyclic boundary conditions

Multiphase micro-CT images

Transient experiments

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Thanks to:

oStephen Neethling, Peyman Mostaghimi, Christopher Pentland

and many other colleagues, for useful discussions

o Sponsors of the project:DTI, EPSRC, ENI, Saudi Aramco, BG, BHP,JOGMEC, Schlumberger, Shell, Statoil and Total

and Thank you for your attention

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References

Brackbill, J. U., Kothe, D. B., and Zemach, C. A continuum method for modeling surface tension. J. Comput. Phys., 100(2):335–354, 1992