SIMULATION OF THE FRICTION FACTOR IN A YIELD-STRESS SLURRY FLOW WHICH EXHIBITS TURBULENCE DAMPING NEAR THE PIPE WALL

The paper deals with the mathematical modelling of fully developed turbulent flow of a Bingham hydromixture in a pipe. The mathematical model is based on time averaged Navier-Stokes equations and uses the apparent viscosity concept. The problem of closure of the turbulence stress tensor was solved by the two-equation turbulence model in which a modified turbulence damping function was taken into account. The final form of the mathematical model constitutes a set of three non-linear partial differential equations. The main aim of the paper is to demonstrate a significant decrease of turbulence near the pipe wall, as the friction factor is below that for a water flow. The paper presents results of numerical simulation of the frictional head loss and friction factor for slurry flows with low, moderate, and high yield stresses. Predicted frictional head losses have been compared with experimental data showing satisfying agreement. It is demonstrated that the frictional head loss and the friction factor substantially depend on the yield stress. The results of numerical simulation are presented as figures and conclusions. Possible causes of turbulence damping near the pipe wall are discussed.

[1]  A. Bartosik Application of Rheological Models in Prediction of Turbulent Slurry Flow , 2010 .

[2]  R. Kuboi,et al.  Fluid and particle motion in turbulent dispersion—II , 1974 .

[3]  M. Roco,et al.  Multi‐Dimensional Flow Analysis of Solid‐Liquid Mixtures , 1985 .

[4]  M. C. Roco,et al.  Modeling of slurry flow: The effect of particle size , 1983 .

[5]  S. L. Soo,et al.  Multiphase fluid dynamics , 1990 .

[6]  A. Bartosik Modelling of a turbulent flow using the herschel-bulkley rheological model , 2006 .

[7]  A. Bartosik Laminarisation effect in fine-dispersive slurry flow , 2008 .

[8]  P. Slatter Transitional and turbulent flow of non-Newtonian slurries in pipes , 1995 .

[9]  Ak-ɛ-PDF two-phase turbulence model for simulating sudden-expansion particle-laden flows , 1996 .

[10]  B. Launder,et al.  Application of the energy-dissipation model of turbulence to the calculation of flow near a spinning disc , 1974 .

[11]  Kenneth C. Wilson,et al.  A new analysis of the turbulent flow of non‐newtonian fluids , 1985 .

[12]  Cheng-Xian Lin,et al.  Numerical investigations of liquid-solid slurry flows in a fully developed turbulent flow region , 2003 .

[13]  Jamshid M. Nouri,et al.  Particle velocity characteristics of dilute to moderately dense suspension flows in stirred reactors , 1992 .

[14]  S. Kleis,et al.  Modification of grid-generated turbulence by solid particles , 1993, Journal of Fluid Mechanics.

[15]  Rakesh Mishra,et al.  Improved model for the prediction of pressure drop and velocity field in multi-sized particulate slurry flow through horizontal pipes , 1998 .

[16]  P. Slatter,et al.  Laminar/turbulent transition in large pipes , 2000 .

[17]  John R. Grace,et al.  Flow of pulp fibre suspension and slurries: A review , 2007 .

[18]  J. Kadambi,et al.  Discrimination between solid and liquid velocities in slurry flow using laser Doppler velocimeter , 1995 .

[19]  G. Hetsroni,et al.  Numerical calculations of two-phase turbulent round jet , 1977 .

[20]  Dvora Barnea,et al.  Flow pattern maps for solid-liquid flow in pipes , 1996 .

[21]  Mihail C. Roco,et al.  Slurry flow : principles and practice , 1991 .

[22]  D. Koch,et al.  Appendix 2: Report of study group on disperse flow ☆ , 2003 .

[23]  J. Hinze,et al.  TURBULENT FLUID AND PARTICLE INTERACTION , 1972 .