SPE 106179 Multiscale Mixed Finite Element Modeling of Coupled - - PowerPoint PPT Presentation

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SPE 106179 Multiscale Mixed Finite Element Modeling of Coupled - - PowerPoint PPT Presentation

SPE 106179 Multiscale Mixed Finite Element Modeling of Coupled Wellbore / Near- Well Flow Stein Krogstad 1 , Louis J. Durlofsky 2 1 SINTEF ICT, 2 Stanford University RSS07 Feb 26-28, 2007 1 Motivation: Near-well region extremely


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RSS07 1 Feb 26-28, 2007

SPE 106179 Multiscale Mixed Finite Element Modeling of Coupled Wellbore / Near- Well Flow

Stein Krogstad1, Louis J. Durlofsky2

1SINTEF ICT, 2Stanford University

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RSS07 2 Feb 26-28, 2007

Motivation:

 Near-well region

extremely important

 Cannot fully resolve

all scales in typical simulation

 Multiscale methods

incorporate fine scales in coarse scale equations

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Outline

Motivation Multiscale Mixed Methods Drift-Flux Wellbore Flow Modeling Multiscale – Drift-Flux Coupling Numerical Experiments Conclusions / Further Work

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Multiscale Methods for Reservoir Simulation

 Multiscale Finite Element Method

T. Hou, X. H. Wu, 1997

 Multiscale Mixed FEM

Z. Chen, T. Hou, 2003 T. Arbogast et al., 2000 J. Aarnes et al., 2004 (group at SINTEF)

 Multiscale Finite Volume Method

P. Jenny, S. H. Lee, H.A. Tchelepi, 2003+

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Standard / Multiscale Discretization

Local flow: Solve coarse equations Solve coarse equations / form fine scale flow Standard Local flow: Multiscale

Coarse model Fine model

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Mixed Finite Elements (MFEM)

      =       −       q p v B B A

T

q p = ⋅ ∇ ∇ − = u k u λ Model equations: Weak formulation: for all Mixed discretization: ∑ ≈ ∑ ≈

j j i i

p p v ϕ ψ u Choose basis: . ) ˆ , ˆ ( V U p × ∈ u ∫ ∫ = ⋅ ∇ = ∫ ⋅ ∇ − ∫ ⋅

q p p p ˆ ˆ ˆ ˆ ) (

1

u u u k u λ

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Mixed / Mimetic / Multiscale

1 = ∆p

 Raviart-Thomas  Multiscale Mixed FEM  Mimetic Finite Differences

1 − = ∆p

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Flux basis function, :

Multiscale MFEM (MsMFEM)

ψ

 Initially compute basis

functions for n=1 to N

 Solve coarse system

based on current saturation

 Form fine scale fluxes  Advance fine scale

saturation by end

p ∇ − = k ψ    ∈ − ∈ = ⋅ ∇

j j i i

T x w T x w for for ψ ) (

  • n

j i

T T ∂ = ⋅n ψ

t ∆

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Drift-Flux Wellbore Flow Model

d m

  • V

m V C V ) ( θ + =

w w

  • m

V V V α α + =

so

V

sw

V

A Ao

  • /

= α

A Aw

w

/

= α 1

0 =

C ) 1 ( 53 . 1

  • c

d

V V α − =

 Mixture velocity (oil/water):  Oil velocity:

Shi et al. (2005): Vw Vo

07 . 1 ) ( = m

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Governing Equations for Wellbore Flow

 Wellbore pressure:

  • so
  • q

x V t = ∂ ∂ − ∂ ∂α A V q D V f g x p

m m m m m tp m

ρ ρ θ ρ 2 2 ) cos(

2

+ + = ∂ ∂

 In-situ volume fraction:

θ hydrostatic friction acceleration

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Well – Reservoir Linkage

Fine grid to the annulus, well segments included in the grid Well segments treated as coarse blocks - no well model is used

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Well – Reservoir Coupling

Pressure:

 Linearize wellbore

pressure equation

 Couple to MsMFEM

equations

 Fixed-point iteration for

initial pressure

Saturation / Holdup:

 Implicit finite volume  Optimal ordering of

cells

Newton iteration in

sequence for each cell / small cluster Prototype implementation: Enhancements required for full generality

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Numerical Example 1: Validation

 Homogeneous permeability  Compressibility (psi -1), 3x10-4  Wellbore radius (inch), 2.0  Pipe roughness (inch), 0.001  Initial saturation, 0.5  Quadratic relative perms, µo/

µw = 1

  • 4200 ft

4 2 f t 600 ft

 7056 fine cells  284 coarse blocks  12 well segments

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Numerical Example 1:

5200 5300 5400 5500 5600 5700 1 3 5 7 9 11 Segment number

Wellbore pressure (psia)

GPRS Fine MsMFEM

4200 4400 4600 4800 5000 5200 5400 1 3 5 7 9 11 Segment number

Wellbore pressure (psia)

GPRS Fine MsMFEM

Total rate: 1,600 STB/d Total rate: 20,000 STB/d

Pressure profiles:

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Total rate: 1,600 STB/d Total rate: 20,000 STB/d

Numerical Example 1:

0.000 0.100 0.200 0.300 0.400 0.500 0.600 1 3 5 7 9 11 Segment number In-situ oil fraction GPRS Fine MsMFEM 0.000 0.100 0.200 0.300 0.400 0.500 0.600 1 3 5 7 9 11 Segment number In-situ oil fraction GPRS Fine MsMFEM

In-situ oil fraction:

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Numerical Example 2:

Long inclined producer in heterogeneous reservoir

 Two-phase oil/water

incompressible flow

 Prescribed total flowrate  Quadratic relative perms, µo/

µw = 10

 Initially saturated with oil

600 ft 3500 ft 5 f t

 85,000 fine cells  62 well segments  θ between 70° and 80°

producer injector

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Numerical Example 2:

4400 4500 4600 4700 4800 4900 5000 1 11 21 31 41 51 61 Segment number Wellbore pressure (psia)

Fine MsMFEM

1000 2000 3000 4000 5000 1 11 21 31 41 51 61 Segment number Wellbore pressure (psia)

Fine MsMFEM

Pressure profiles at 0.12 PVI:

 Coarse grid: 2856 blocks (factor of 30 coarsening)

Flowrate: 4,000 STB/d Flowrate: 60,000 STB/d

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Numerical Example 2:

0.2 0.4 0.6 0.8 1 1 11 21 31 41 51 61 Segment number In-situ oil fraction

Fine - low rate MsMFEM - low rate Fine - high rate MsMFEM - high rate

High flowrate: In-situ oil fraction: Low flowrate:

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Numerical Example 2:

0.2 0.4 0.6 0.8 1 1 11 21 31 41 51 61 Segment number In-situ oil fraction

Fine 17x24x21 5x5x4

4600 4650 4700 4750 4800 4850 4900 4950 1 11 21 31 41 51 61 Segment number Wellbore pressure (psia)

Fine 17x24x21 5x5x4

 Coarsening factor varied from 10 to 850  Accuracy degrades with coarsening, but

physically reasonable results in all cases

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Conclusions / Further Work

 Extended MsMFEM for oil-water systems to

include drift-flux wellbore flow model

 Demonstrated and validated through

numerical experiments involving vertical and deviated wells

 Achieved accurate results for significantly

coarsened models

 Extend to three-phase flow