modeling transport phenomena on fluid interfaces in combination … · 2011. 7. 5. · conclusion...
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CHAIR FOR
COMPUTATIONAL
ANALYSIS OF
TECHNICAL
SYSTEMS
Modeling transport phenomena on fluid
interfaces in combination with the XFEM
H. Sauerland and T.-P. Fries
March 23, 2011
16. Internat. Conference on Finite Elements in Flow ProblemsMunich, Germany
Motivation
Topic of increasing interest in the scientific community.
Transport of quantities on moving surfaces is not intuitive.
Various applications
Surfactant transport (fluid dynamics).
Texture synthesis (computer graphics).
Species diffusion along grain boundaries (material science).
Pattern formation on growing organisms (biology).
[1] [2] [3]
[1] Bertalmio, JCP 2001; [2] Brown University, Gao Group; [3] Leung, JCP 2003
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 2
Motivation
Here: Two-phase/free-surface flow problems.
Flow field
Advection/deformationof the interface
Variable surface tension
Scalar transporton the interface
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 3
Outline
Governing equationsInterface description
Challenges in two-phase flows
XFEM
Modeling transport phenomena on hypersurfacesImplicit approach
Numerical examples
Conclusion
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 4
Governing equationsInterface description
Challenges in two-phase flows
XFEM
Modeling transport phenomena on hypersurfacesImplicit approach
Numerical examples
Conclusion
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 5
Governing equations
Incompressible and isothermal Navier-Stokes equations foreach phase j = 1, 2 in Ω:
ρj
(∂u
∂t+ u · ∇u− f
)
−∇ · σ = 0 in Ωj × [0,T ],
∇ · u = 0 in Ωj × [0,T ].
Constitutive equation:
σ(u, p) = −pI+ µj
[
∇u+ (∇u)T]
.
Boundary conditions:
u = u on Γu × [0,T ],
n · σ = h on Γh × [0,T ].
Interface conditions:
[u]Γd = 0 on Γd (t) × [0,T ],
[n · σ]Γd = γκn on Γd (t) × [0,T ].
Ω1
Ω2
Ω2
n
n
n
Γd
Γ
Initial condition:
u(x, 0) = u0(x) in Ω.
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 6
Interface description
The Level-set method offers a flexible representation of themoving interface.
Zero-level of the scalar level-set function φ implicitly describesthe interface:
φ(x) = ± minx⋆∈Γd
‖x− x⋆‖ , ∀x ∈ Ω.
Motion of the interface Γd is covered by the level-settransport equation:
∂φ
∂t+ u(x, t) · ∇φ = 0 in Ω× [0,T ].
→ Strongly coupled problem of the fluid and level-set field.
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 7
Governing equationsInterface description
Challenges in two-phase flows
XFEM
Modeling transport phenomena on hypersurfacesImplicit approach
Numerical examples
Conclusion
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 8
Challenges in two-phase flows
Discontinuous field variables:
Density differences
→ Kink in the velocity/pressure field.Viscosity differences
Surface tension → Jump in the pressure field.
→ XFEM
up
ρ2, µ2
ρ1, µ1
u
p
ρ2, µ2
ρ1, µ1
γ
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 9
Governing equationsInterface description
Challenges in two-phase flows
XFEM
Modeling transport phenomena on hypersurfacesImplicit approach
Numerical examples
Conclusion
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 10
XFEM
Discontinuities inside elements can be accounted for.
Here: Pressure approximation space is locally enriched:
ph(x) =∑
i∈I
Ni (x)pi
︸ ︷︷ ︸
strd. FE approx.
+∑
i∈I⋆
Ni (x) · [ψ(x, t)− ψ(xi , t)] ai
︸ ︷︷ ︸
enrichment
.
Sign-enrichment:
ψ(x, t) = sign (φ(x, t)) =
−1 : φ < 0,
0 : φ = 0,
1 : φ > 0.
I ⋆
φ(x, t) = 0
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 11
XFEM
Topics worth talking about:
Numerical integration of enriched elements.
Choice of enrichment functions[Sauerland and Fries, JCP 2011].
Time-integration[Fries and Zilian, IJNME 2009].
Adaptive mesh refinement at the interface[Fries et al., IJNME 2010].
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 12
Governing equationsInterface description
Challenges in two-phase flows
XFEM
Modeling transport phenomena on hypersurfacesImplicit approach
Numerical examples
Conclusion
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 13
Modeling transport phenomena on hypersurfaces
Physical description of transport processes is simple.
Solving PDEs on arbitrary, moving manifolds is difficult.
Explicit approach:
Moving surface mesh.
Generalized differentialoperators required(cf. Laplace-Beltramioperator).
Usual disadvantages ofexplicit descriptions.
Implicit approach:
Level-set method.
Quantities on the surfaceare extended to the wholedomain, Rn → R
n+1.
Transport equations aresolved in a fixed volume.
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 14
Implicit approach
Transport of a scalar quantity G on an implicit hypersurface:
Prerequisite: Scalar G is known in the whole domain.
Situation: Only GΓ on the interface is available.
Extend GΓ off the interface, orthogonal to φ
sign(φ)∇G · ∇φ = 0 in Ω,
G = GΓ on Γd .Ω1
Ω2
Γd
Adalsteinsson, JCP 1999; Chessa, IJNME 2002
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 15
Implicit approach
Application of the boundary condition G = GΓ on the implicit Γd :
Find intersections xintj of Γd with the element edges.
For each cut element node i ∈ I ⋆ find x⋆ = minj
‖xi − xintj ‖.
Prescribe Gi = GΓ(x⋆).
I ⋆
Γd
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 16
Implicit approach
Conservation equation for G in Ω (for brevity in 2D)
∂G
∂t=− u · ∇G
︸ ︷︷ ︸
advection
−
[
n2y∂u
∂x− nxny
(∂u
∂y+∂v
∂x
)
+ n2x∂v
∂y
]
G
︸ ︷︷ ︸
compression/expansion
+ σ
[∂2G
∂x2n2y − 2
∂2G
∂x∂ynxny +
∂2G
∂y2n2x − κ(∇G · n)
]
︸ ︷︷ ︸
diffusion
,
Adalsteinsson, JCP 2003
velocity: u = (u, v)T , diffusion coefficient: σ,
normal vector: n = (nx , ny )T =
∇φ
|∇φ|, curvature: κ.
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 17
Implicit approachAdvection in a constant flow field:
u = (−y , x , 0)T , σ = 0,GΓ = x + y + z .
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 18
Implicit approachDiffusion on a fixed surface:
u = 0, σ = 1.0,GΓ = z .
Diffusion on moving interfaces not considered here.
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 19
Implicit approach
Integration in the two-phase flow solver:
Navier-Stokes Level-set
f (G )
Hypersurface transport
u(x, t)
φ(x, t)
φ(x, t)u(x, t)
G (xΓ, t)
γ(xΓ, t)
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 20
Governing equationsInterface description
Challenges in two-phase flows
XFEM
Modeling transport phenomena on hypersurfacesImplicit approach
Numerical examples
Conclusion
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 21
Numerical examples
Importance of the compression/expansion term for generalcases.
Tank Sloshing
0 0.2 0.4 0.6 0.8 1
0.1
0.3
0.5
0.7
x
GΓ
t=20s
pure advectionadv.+compr.initial
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 22
Numerical examples3D tank sloshing (40 × 40× 60 elements)
t = [0, 40s], σ = 0,GΓ = 0.5.
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 23
Numerical examples3D rising drop (40 × 40× 80 elements)
t = [0, 0.02s], σ = 0,GΓ = 0.5,Eo = 7.64,Mo = 1.22 · 10−6.
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 24
Governing equationsInterface description
Challenges in two-phase flows
XFEM
Modeling transport phenomena on hypersurfacesImplicit approach
Numerical examples
Conclusion
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 25
Conclusion
Results of this case study:
Implict approach for hypersurface transport is easilyimplemented in an existing level-set framework.
A smooth and very accurate level-set field has to bemaintained.
Frequent “re-extension” of the scalar quantity from theinterface is required (cf. level-set reinitialization).
Outlook:
Consideration of diffusion on moving interfaces.
Variable surface tension coefficient depending on the scalarconcentration.
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 26
Thank you for your attention.
www.xfem.rwth-aachen.de
H. Sauerland and T.-P. Fries Modeling transport phenomena on fluid interfaces 27