A numerical study of the flow of Bingham-like fluids in two-dimensional vane and cylinder rheometers using a smoothed particle hydrodynamics (SPH) based method

In this paper, a Lagrangian formulation of the Navier–Stokes equations, based on the smoothed particle hydrodynamics (SPH) approach, was applied to determine how well rheological parameters such as plastic viscosity can be determined from vane rheometer measurements. First, to validate this approach, a Bingham/Papanastasiou constitutive model was implemented into the SPH model and tests comparing simulation results to well established theoretical predictions were conducted. Numerical simulations for the flow of fluids in vane and coaxial cylinder rheometers were then performed. A comparison to experimental data was also made to verify the application of the SPH method in realistic flow geometries. Finally, results are presented from a parametric study of the flow of Bingham fluids with different yield stresses under various applied angular velocities of the outer cylindrical wall in the vane and coaxial cylinder rheometers. The stress, strain rate and velocity profiles, especially in the vicinity of the vane blades, were computed. By comparing the calculated stress and flow fields between the two rheometers, the validity of the assumption that the vane could be approximated as a cylinder for measuring the rheological properties of Bingham fluids at different shear rates was tested.

[1]  D. V. Griffiths,et al.  Finite element analysis of the shear vane test , 1990 .

[2]  Mahesh Prakash,et al.  Discrete–element modelling and smoothed particle hydrodynamics: potential in the environmental sciences , 2004, Philosophical Transactions of the Royal Society of London. Series A: Mathematical, Physical and Engineering Sciences.

[3]  J. Morris,et al.  Modeling Low Reynolds Number Incompressible Flows Using SPH , 1997 .

[4]  J. F. Milthorpe,et al.  On the shearing zone around rotating vanes in plastic liquids: theory and experiment , 1985 .

[5]  A. Colagrossi,et al.  Numerical simulation of interfacial flows by smoothed particle hydrodynamics , 2003 .

[6]  J. Monaghan,et al.  SPH elastic dynamics , 2001 .

[7]  J. Monaghan SPH without a Tensile Instability , 2000 .

[8]  J. Morris Simulating surface tension with smoothed particle hydrodynamics , 2000 .

[9]  J. Monaghan Simulating Free Surface Flows with SPH , 1994 .

[10]  Chiara F. Ferraris,et al.  Comparison of Concrete Rheometers , 2003 .

[11]  L. Lucy A numerical approach to the testing of the fission hypothesis. , 1977 .

[12]  V. S. Vaidhyanathan,et al.  Transport phenomena , 2005, Experientia.

[13]  Ian Frigaard,et al.  Stability and instability of Taylor–Couette flows of a Bingham fluid , 2006, Journal of Fluid Mechanics.

[14]  David V. Boger,et al.  Yield Stress Measurement for Concentrated Suspensions , 1983 .

[15]  Georgios C. Georgiou,et al.  Cessation of Couette and Poiseuille flows of a Bingham plastic and finite stopping times , 2005 .

[16]  Peter Domone,et al.  Comparison of concrete rheometers: International tests at MBT (Cleveland OH, USA) in May 2003 , 2004 .

[17]  S. Cummins,et al.  An SPH Projection Method , 1999 .

[18]  J. Monaghan,et al.  SPH simulation of multi-phase flow , 1995 .

[19]  A. James,et al.  The yield surface of viscoelastic and plastic fluids in a vane viscometer , 1997 .

[20]  T. Papanastasiou Flows of Materials with Yield , 1987 .

[21]  J. Monaghan,et al.  Smoothed particle hydrodynamics: Theory and application to non-spherical stars , 1977 .

[22]  Nikolaus A. Adams,et al.  A multi-phase SPH method for macroscopic and mesoscopic flows , 2006, J. Comput. Phys..

[23]  A numerical study for the cessation of Couette flow of non-Newtonian fluids with a yield stress , 2007 .

[24]  S. Hess,et al.  Viscoelastic flows studied by smoothed particle dynamics , 2002 .

[25]  H. A. Barnes,et al.  The vane‐in‐cup as a novel rheometer geometry for shear thinning and thixotropic materials , 1990 .

[26]  R. G. Owens,et al.  A numerical study of the SPH method for simulating transient viscoelastic free surface flows , 2006 .

[27]  F. Bertrand,et al.  Analysis of the vane rheometer using 3D finite element simulation , 2007 .

[28]  G. Georgiou,et al.  Flow instabilities of Herschel–Bulkley fluids , 2003 .

[29]  J. Monaghan Smoothed particle hydrodynamics , 2005 .

[30]  J. Sherwood,et al.  The torque on a rotating n-bladed vane in a newtonian fluid or linear elastic medium , 1992, Proceedings of the Royal Society of London. Series A: Mathematical and Physical Sciences.

[31]  Luc Oger,et al.  Smoothed particle hydrodynamics for cohesive grains , 1999 .

[32]  Howard A. Barnes,et al.  Rotating vane rheometry — a review , 2001 .

[33]  Maria Chatzimina,et al.  Wall Shear Rates in Circular Couette Flow of a Herschel-Bulkley Fluid , 2009 .

[34]  F. A. Seiler,et al.  Numerical Recipes in C: The Art of Scientific Computing , 1989 .

[35]  C. Antoci,et al.  Numerical simulation of fluid-structure interaction by SPH , 2007 .

[36]  Pep Español,et al.  Incompressible smoothed particle hydrodynamics , 2007, J. Comput. Phys..

[37]  Fabrice Colin,et al.  Computing a null divergence velocity field using smoothed particle hydrodynamics , 2006, J. Comput. Phys..

[38]  R. Tanner,et al.  SPH simulations of transient viscoelastic flows at low Reynolds number , 2005 .

[39]  Gilmer R. Burgos,et al.  On the determination of yield surfaces in Herschel-Bulkley fluids , 1999 .