Mechanical load on a particle aggregate in mono-axial elongational flow

Abstract Subject of the present contribution is the numerical simulation of the effect of a elongational flow field on a suspended particle-aggregate. The particle-aggregate consists of seven rigid spherical particles and is suspended in the flow field at low Re-numbers (Re=0.01–0.1). The ratio of particle and fluid densities varies between 1 and 15. The velocity and pressure distribution is obtained from the numerical solution of the Navier–Stokes equation and the continuity equation based on finite volume methods. The particle motion is obtained from the Euler equation of motion for rigid bodies. A comparison of classical solutions with the result of the numerical simulation for a spherical particle shows a very good agreement. It can be shown, that the interaction of the aggregate with the fluid differs clearly from that of a spherical particle. Furthermore, it has been found that the magnitude of stresses on the aggregate surface is increasing with time monotonously. Shear stress is maximum on the outer parts of the aggregate. Normal stress takes on maximum values on the upstream and downstream oriented faces. The maximum pressure drop across the particle results in an extensional force which increases in time within the considered period.

[1]  Peter A. Wilderer,et al.  Structure and function of biofilms. , 1989 .

[2]  Ko Higashitani,et al.  Simulation of deformation and breakup of large aggregates in flows of viscous fluids , 2001 .

[3]  W. R. Schowalter,et al.  Deformation of a two-dimensional drop at non-zero Reynolds number in time-periodic extensional flows: numerical simulation , 2001, Journal of Fluid Mechanics.

[4]  Howard A. Stone,et al.  The influence of initial deformation on drop breakup in subcritical time-dependent flows at low Reynolds numbers , 1989, Journal of Fluid Mechanics.

[5]  Stefan Blaser,et al.  Particles under stress , 1998 .

[6]  W. Olbricht,et al.  Experimental studies of the deformation of a synthetic capsule in extensional flow , 1993, Journal of Fluid Mechanics.

[7]  S. Blaser The hydrodynamical effect of vorticity and strain on the mechanical stability of flocs , 1998 .

[8]  R. Khayat,et al.  Influence of shear and elongation on drop deformation in convergent–divergent flows , 2000 .

[9]  Howard A. Stone,et al.  Breakup of concentric double emulsion droplets in linear flows , 1990, Journal of Fluid Mechanics.

[10]  K. Keiding,et al.  The shear sensitivity of activated sludge: an evaluation of the possibility for a standardised floc strength test. , 2002, Water research.

[11]  L. G. Leal,et al.  An experimental study of drop deformation and breakup in extensional flow at high capillary number , 2001 .

[12]  Jost Wingender,et al.  Microbial Extracellular Polymeric Substances , 1999, Springer Berlin Heidelberg.

[13]  Y. Saad,et al.  GMRES: a generalized minimal residual algorithm for solving nonsymmetric linear systems , 1986 .

[14]  G. Marchuk Methods of Numerical Mathematics , 1982 .

[15]  Jost Wingender,et al.  What are Bacterial Extracellular Polymeric Substances , 1999 .

[16]  Jacques Magnaudet,et al.  Accelerated flows past a rigid sphere or a spherical bubble. Part 1. Steady straining flow , 1995, Journal of Fluid Mechanics.

[17]  Kausik Sarkar,et al.  Deformation of a two-dimensional viscoelastic drop at non-zero Reynolds number in time-periodic extensional flows , 2000 .

[18]  L. G. Leal,et al.  Deformation and relaxation of Newtonian drops in planar extensional flows of a Boger fluid , 2001 .

[19]  W. R. Schowalter,et al.  Deformation of a two-dimensional viscous drop in time-periodic extensional flows: analytical treatment , 2001, Journal of Fluid Mechanics.

[20]  O. Gottlieb,et al.  Chaotic rotation of triaxial ellipsoids in simple shear flow , 1997, Journal of Fluid Mechanics.

[21]  J. Derby,et al.  Transient polymeric drop extension and retraction in uniaxial extensional flows , 2001 .

[22]  Higashitani,et al.  Two-Dimensional Simulation of the Breakup Process of Aggregates in Shear and Elongational Flows. , 1998, Journal of colloid and interface science.