Simulation of particles in fluid: a two-dimensional benchmark for a cylinder settling in a wall-bounded box

Abstract This paper presents numerical experiments inspired by the theoretical work of Faxen for predicting the terminal velocity of a cylinder, settling halfway between two parallel walls at low Reynolds numbers. It is demonstrated that unexpected correlations exist between Faxen's results and the relaxation of a rigid disk initially suspended in a wall-bounded square box. To this end, the 1-Fluid (1F) method is used within a frame of Direct Numerical Simulation (DNS). In first place, the assessment of 1F method in two dimensions is presented. Simulations are in good agreement with Faxen's approach in half-bounded domains, and with simulation data from literature as well. Numerical experiments are then designed in order to investigate the transient behavior of a circular disk in a wall-bounded square box. Significant ranges of particle-to-wall containment ratios, density ratios and Galileo numbers were used in simulations. In the case where the aspect ratio belongs to the range [0.005,0.4] and the Galileo number is smaller than 1, it is found that the wall correction factor based on the maximum settling velocity could be correlated directly with the Faxen's correction factor based on the terminal settling velocity. For extreme values of containment, Faxen's theory gives irrelevant predictions, and alternative approaches based on 1F simulations are suggested. Finally, an original benchmark is designed as an efficient and inexpensive tool for validating numerical approaches to fluid/particle systems.

[1]  H. Brenner The slow motion of a sphere through a viscous fluid towards a plane surface , 1961 .

[2]  Pierre Lubin,et al.  An adaptative augmented Lagrangian method for three-dimensional multimaterial flows , 2004 .

[3]  Evan Mitsoulis,et al.  Viscoplastic flow around a cylinder kept between parallel plates , 2002 .

[4]  Henk A. van der Vorst,et al.  Bi-CGSTAB: A Fast and Smoothly Converging Variant of Bi-CG for the Solution of Nonsymmetric Linear Systems , 1992, SIAM J. Sci. Comput..

[5]  R. G. Hussey,et al.  Cylinder Drag at Low Reynolds Number. , 1977 .

[6]  Khodor Khadra,et al.  Fictitious domain approach for numerical modelling of Navier–Stokes equations , 2000 .

[7]  R. Glowinski,et al.  A fictitious domain approach to the direct numerical simulation of incompressible viscous flow past moving rigid bodies: application to particulate flow , 2001 .

[8]  C. Peskin Numerical analysis of blood flow in the heart , 1977 .

[9]  Horace Lamb F.R.S. XV. On the uniform motion of a sphere through a viscous fluid , 1911 .

[10]  J. Verhelst Model evaluation and dynamics of a viscoelastic fluid in a complex flow , 2001 .

[11]  S. Zaleski,et al.  DIRECT NUMERICAL SIMULATION OF FREE-SURFACE AND INTERFACIAL FLOW , 1999 .

[12]  Stéphane P. Vincent,et al.  Sur une méthode de pénalisation tensorielle pour la résolution des équations de Navier-Stokes , 2001 .

[13]  G. Batchelor,et al.  An Introduction to Fluid Dynamics , 1968 .

[14]  Robert C. Armstrong,et al.  Viscoelastic flow of polymer solutions around a periodic, linear array of cylinders: comparisons of predictions for microstructure and flow fields , 1998 .

[15]  Jos Derksen,et al.  Assessment of the 1-fluid method for DNS of particulate flows: Sedimentation of a single sphere at moderate to high Reynolds numbers , 2007 .

[16]  A. Hamielec,et al.  a Numerical Investigation of the Efficiency with which Simple Columnar Ice Crystals Collide with Supercooled Water Drops. , 1975 .

[17]  J. Caltagirone,et al.  Numerical modelling of solid particle motion using a new penalty method , 2005 .

[18]  G. Ristow WALL CORRECTION FACTOR FOR SINKING CYLINDERS IN FLUIDS , 1997 .

[19]  J. Happel,et al.  Low Reynolds number hydrodynamics , 1965 .