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Shear-induced migration of rigid particles near an interface

between a Newtonian and a viscoelastic fluid

Citation for published version (APA):

Jaensson, N. O., Mitrias, C., Hulsen, M. A., & Anderson, P. D. (2018). Shear-induced migration of rigid particles near an interface between a Newtonian and a viscoelastic fluid. Langmuir, 34(4), 1795-1806.

https://doi.org/10.1021/acs.langmuir.7b03482

DOI:

10.1021/acs.langmuir.7b03482

Document status and date: Published: 30/01/2018 Document Version:

Accepted manuscript including changes made at the peer-review stage Please check the document version of this publication:

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Shear-Induced Migration of Rigid Particles

near an Interface between a Newtonian and a

Viscoelastic Fluid - Supporting Information

Nick. O. Jaensson,

∗,†,‡

Christos Mitrias,

Martien A. Hulsen,

and Patrick D.

Anderson

†Department of Mechanical Engineering, Eindhoven University of Technology, P.O. Box 513, 5600 MB Eindhoven, The Netherlands

‡Dutch Polymer Institute (DPI), P.O. Box 902, 5600 AX Eindhoven, The Netherlands E-mail: n.o.jaensson@tue.nl

Numerical method

The finite element method with adaptive meshing is employed to solve the Cahn-Hilliard

equation, the mass- and momentum balance and the evolution equation for the

conforma-tion tensor. Here a short overview of the numerical method is given. For a more detailed

explanation, the reader is referred to our previous work on particles in Cahn-Hilliard fluids

in Newtonian flows1,2 and viscoelastic flows3.

At the start of the simulation, a mesh is generated using Gmsh4 which is aligned with the

particle boundary and is refined near the fluid-fluid interface, as shown in Fig. 1. Due to the

symmetry and periodic assumptions, only half of the particle is simulated. The equations are

discretized in space to yield the unknowns u,p, φ, µ and c. Tetrahedral P2P1P1 elements are

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of the domain are ∂P , Γ5 and Γ6, where no-flux and contact angle boundary conditions

are imposed for the Cahn-Hilliard problem, and no-slip is imposed for the fluid velocity.

Periodicity is enforces between the planes Γ1 and Γ2 using constraint equations, yielding

Lagrange multipliers as additional unknowns. Symmetry conditions are imposed on the

planes Γ3 and Γ4.

Fig. 1: An example of the computational mesh indicating the boundaries (note: in the actual computations the mesh is much more refined).

At the beginning of each time step, the mesh is moved using an arbitrary Lagrange

Euler approach5, which moves the mesh close to the particle with the particle, but keeps

the mesh stationary further away from the particle. When the mesh becomes too distorted,

or if the interface moves out of the refined region, a remeshing is performed. Second-order,

adaptive time stepping schemes are used, and the mass and momentum balance and

Cahn-Hilliard equation are solved in one system, with a prediction of the polymer stress according

to6. Solving the mass and momentum balance and Cahn-Hilliard equation in one system was

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use of larger time steps. The (angular) velocities of the particle are included as a additional

unknowns8 using a constraint equation, and the particle velocities are such that the

force-and torque-balance on the particle boundary are satisfied. This system is solved using a

GMRES iterative solver from the Sparskit library9, with a customized preconditioner as

described in the next section. To solve the evolution equation for the conformation tensor,

the log-conformation approach is applied10. Furthermore, SUPG stabilization is used11.

After all variables at the new time step have been computed, the simulation can continue to

the next time step.

The element size near the interface is chosen equal to ξ, which yields ten second-order points on the interface, which has been shown to be sufficient for mesh-convergence12.

Fur-thermore, the element size near the particle is chosen as2πa/64, which yields 64 elements on the particle circumference. Using an adaptive time-stepping scheme, the time step is varied

between ∆t ˙γ = 0.08 and ∆t ˙γ = 0.32, where the larger time step is used when the dynamics are slow (e.g when the particle migrates toward the interface) and the smaller time step is

used when the dynamics are fast (e.g. the adsorption of a particle at an interface).

GMRES preconditioner

The discretized version of the mass- and momentum balance and Cahn-Hilliard equation is

written as a linear system of equations:

   M11 M12 M21 M22       x y   =    f g   , (1)

where x contains the unknowns in the mass- and momentum balance (velocity, pressure and Lagrange multipliers for the particle motion/periodic boundary conditions) and y con-tains the unknowns in the Cahn-Hilliard equation (composition, chemical potential and

Langrange multipliers for the periodic boundary conditions). The vectors f and g contain information about previous time steps, needed for the integration in time. Since the full

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LU-decomposition of the system given in Eq. (1) can become too large to solve efficiently, iterative

solvers are essential. Our choice is the GMRES iterative solver from the Sparskit library9,

for which proper preconditioning is essential. However, the system as shown in Eq. (1) can

become badly conditioned and designing a suitable preconditioner is not straightforward.

Our approach is to make use of the natural block structure that arises from the separate

discretized equations to define the preconditioner P :

P =    M11 M12 0 M22   , (2)

where theM21-block was disregarded, i.e. the convection term in the Cahn-Hilliard equation.

Using the triangular shape of P , linear systems of equations with the preconditioner P can easily be solved by first solving M22y = g, followed by M11x = f − M12y. These

subsystems are solved using a direct solver from the HSL library13, which allows to reuse

the LU decompositions during the entire GMRES iteration. Moreover, the true increase

in performance arises due to the reuse of the LU decompositions across several time steps,

which was found to maintain fast convergence of the GMRES iteration. In practice, the LU

decompositions could be reused until a remeshing was performed, after which they had to

be recomputed.

Size of the domain

In this research, a domain size in the y direction (i.e. the wall-to-wall distance) of H = 40a is used. To ensure that the influence of the walls on the migration results is small, we have also performed the simulations as presented in Fig. 5

in the main article with domain sizes of H = 20a and H = 80a. The results are presented in Fig. 2, where it can be seen that the final location of the particle,

which determines the migration regime used in the morphology plots, is similar

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paper. −2 −1 0 1 2 0 100 200 300 400 500 Y /a t ˙γ Wi = 0 Wi = 1 Wi = 2 Wi = 3 H = 20a H = 40a H = 80a (a) −0.01 0 0.01 0.02 0.03 0.04 0.05 0.06 0.07 0 100 200 300 400 500 Uy /( ˙γa ) t ˙γ (b)

Fig. 2: The particle vertical position (a) and particle velocity (b). Ca = 1, θc = 90◦ and

S = 0.1 and varying wall-to-wall distance H.

References

(1) Jaensson, N.; Hulsen, M.; Anderson, P. Stokes-Cahn-Hilliard formulations and

simula-tions of two-phase flows with suspended rigid particles. Computers and Fluids 2015,

111, 1–17.

(2) Jaensson, N.; Hulsen, M.; Anderson, P. A comparison between the XFEM and a

boundary-fitted mesh method for the simulation of rigid particles in Cahn-Hilliard

fluids. Computers & Fluids 2017, 148, 121–136.

(3) Jaensson, N.; Hulsen, M.; Anderson, P. On the use of a diffuse-interface model for the

simulation of rigid particles in two-phase Newtonian and viscoelastic fluids. Computers

& Fluids 2017, 156, 81–96.

(4) Geuzaine, C.; Remacle, J.-F. Gmsh: A 3-D finite element mesh generator with

built-in pre- and post-processbuilt-ing facilities. International Journal for Numerical Methods built-in

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(5) Hu, H.; Patankar, N.; Zhu, M. Direct numerical simulations of fluid-solid systems using

the arbitrary Lagrangian-Eulerian technique. Journal of Computational Physics 2001,

169, 427–462.

(6) D’Avino, G.; Hulsen, M. Decoupled second-order transient schemes for the flow of

viscoelastic fluids without a viscous solvent contribution. Journal of Non-Newtonian

Fluid Mechanics 2010, 165, 1602–1612.

(7) Aland, S. Time integration for diffuse interface models for two-phase flow. Journal of

Computational Physics 2014, 262, 58–71.

(8) Glowinski, R.; Pan, T.; Périaux, J. Distributed Lagrange multiplier methods for

in-compressible viscous flow around moving rigid bodies. Computer Methods in Applied

Mechanics and Engineering 1998, 151, 181–194.

(9) Saad, Y. SPARSKIT: A Basic Tool Kit for Sparse Matrix Computations. NASA Ames

Research Center, Moffett Field, CA, Technical Report 2090, 2001.

(10) Hulsen, M.; Fattal, R.; Kupferman, R. Flow of viscoelastic fluids past a cylinder at

high Weissenberg number: stabilized simulations using matrix logarithms. Journal of

Non-Newtonian Fluid Mechanics 2005, 127, 27–39.

(11) Brooks, A.; Hughes, T. Streamline upwind/Petrov-Galerkin formulations for convection

dominated flows with particular emphasis on the incompressible Navier-Stokes

equa-tions. Computational Methods in Applied Mechanical Engineering 1982, 32, 199–259.

(12) Yue, P.; Feng, J.; Liu, C.; Shen, J. A diffuse-interface method for simulating two-phase

flows of complex fluids. Journal of Fluid Mechanics 2004, 515, 293–317.

(13) HSL, A collection of Fortran codes for large scale scientific computation. 2013; http:

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