Comparisons of PEPT derived charge features in wet milling environments with a friction-adjusted DEM model

Abstract The extent to which the discrete element method (DEM) represents particulate flow in wet tumbling mill environments is investigated by adjusting the friction coefficient in the simulation to best match positron emission particle tracking (PEPT) experiments of the same media in steady-state, re-circulating fluids of water and slurry. Porosity and velocity distributions of 5 mm, mono-sized glass spheres in a 300 mm diameter mill are statistically compared to an equivalent dry DEM model. These show a very high degree of spatial agreement with RMS differences of only 0.11%. Typically, around 80% of the mill volume is found to have identical results. Similar levels of agreement are found for a range of operating speeds from 31% to 75% of critical speed. These demonstrate that a solid particle DEM model of the charge, without an explicit representation of the slurry, is able to accurately capture the motion of the solid charge. Agreement is improved by calibration of the wet friction coefficient. The DEM results indicate that the flow is not particularly sensitive to the exact choice. Small differences between DEM and PEPT are observed in the free surface part of the flow. The presence of fluid slightly slows the fall and compaction of the charge leading to a more slowly moving and higher free surface in the middle of the mill. The flow is also found to be highly three dimensional with significant axial flow generated by the end walls of the mill.

[1]  Colin Thornton,et al.  A Theoretical Study of the Liquid Bridge Forces between Two Rigid Spherical Bodies , 1993 .

[2]  G. C. Barker Computer Simulations of Granular Materials , 1994 .

[3]  Keizo Yabumoto,et al.  Spontaneous structures in three-dimensional bubbling gas-fluidized bed by parallel DEM–CFD coupling simulation , 2008 .

[4]  Paul W. Cleary,et al.  Comparative study by PEPT and DEM for flow and mixing in a ploughshare mixer , 2012 .

[5]  Paul W. Cleary,et al.  Predicting charge motion, power draw, segregation and wear in ball mills using discrete element methods , 1998 .

[6]  P. Fowles,et al.  Developments in particle tracking using the Birmingham Positron Camera , 1997 .

[7]  A. McBride,et al.  Improved experimental tracking techniques for validating discrete element method simulations of tumbling mills , 2004 .

[8]  Paul W. Cleary,et al.  Recent advances in dem modelling of tumbling mills , 2001 .

[9]  Runyu Yang,et al.  CFD–DEM modelling of particle flow in IsaMills – Comparison between simulations and PEPT measurements , 2011 .

[10]  Paul W. Cleary,et al.  DEM 2007 Editorial , 2009 .

[11]  C. Mac Namara,et al.  Dynamics of textile motion in a front-loading domestic washing machine , 2012 .

[12]  P. W. Cleary,et al.  Comparative Study of DEM and Experimental Results of Flow Patterns in a Ploughshare Mixer , 2002 .

[13]  J. M. Huntley,et al.  Experimental measurements and modelling of rapid granular flows , 2008 .

[14]  Paul W. Cleary,et al.  Using DEM to model ore breakage within a pilot scale SAG mill , 2004 .

[15]  Using Positron Emission Particle Tracking (PEPT) to Study Mixing in Stirred Vessels: Validation and Tackling Unsolved Problems in Opaque Systems , 2009 .

[16]  Parker,et al.  Single-particle motion in three-dimensional vibrofluidized granular beds , 2000, Physical review. E, Statistical physics, plasmas, fluids, and related interdisciplinary topics.

[17]  Jpk Seville,et al.  Solids motion in rolling mode rotating drums operated at low to medium rotational speeds , 2001 .

[18]  Indresan Govender,et al.  Towards a mechanistic model for slurry transport in tumbling mills , 2011 .

[19]  P. Cundall,et al.  A discrete numerical model for granular assemblies , 1979 .

[20]  Malcolm Powell,et al.  Power draw estimations in experimental tumbling mills using PEPT , 2011 .

[21]  Paul W. Cleary,et al.  Modelling comminution devices using DEM , 2001 .

[22]  Paul W. Cleary,et al.  Prediction of slurry transport in SAG mills using SPH fluid flow in a dynamic DEM based porous media , 2006 .

[23]  Paul W. Cleary,et al.  Modelling confined multi-material heat and mass flows using SPH , 1998 .

[24]  David Parker,et al.  Flow patterns in granulating systems , 2001 .

[25]  Brahmeshwar Mishra,et al.  The discrete element method for the simulation of ball mills , 1992 .

[26]  David Parker,et al.  Non-equilibrium particle motion in the vicinity of a single blade , 2003 .

[27]  Paul W. Cleary,et al.  Advances in discrete element methods for geomechanics , 2009 .

[28]  Paul W. Cleary,et al.  Charge behaviour and power consumption in ball mills: sensitivity to mill operating conditions, liner geometry and charge composition , 2001 .

[29]  Colin Thornton Special Issue on Discrete Element Methods , 2009 .

[30]  Paul W. Cleary,et al.  Comparison of DEM and experiment for a scale model SAG mill , 2003 .

[31]  David Parker,et al.  Using positron emission particle tracking (PEPT) to study nearly neutrally buoyant particles in high solid fraction pipe flow , 2001 .

[32]  Paul W. Cleary,et al.  How well do discrete element granular flow models capture the essentials of mixing processes , 1998 .

[33]  Paul W. Cleary,et al.  Towards a virtual comminution machine , 2008 .

[34]  Brahmeshwar Mishra,et al.  Simulation of charge motion in ball mills. Part 1: experimental verifications , 1994 .

[35]  Paul W. Cleary,et al.  Large scale industrial DEM modelling , 2004 .

[36]  Masao Sakamoto,et al.  Quasi-three-dimensional numerical simulation of spouted beds in cylinder , 2000 .

[37]  Paul W. Cleary,et al.  An investigation and optimization of the 'OLDS' elevator using Discrete Element Modeling , 2009 .

[38]  Charles S. Campbell,et al.  RAPID GRANULAR FLOWS , 1990 .

[39]  Jpk Seville,et al.  Attrition of porous glass particles in a fluidised bed , 1998 .

[40]  Paul W. Cleary,et al.  Prediction of 3D slurry flow within the grinding chamber and discharge from a pilot scale SAG mill , 2012 .

[41]  Paul W. Cleary,et al.  An investigation of the comparative behaviour of alternative contact force models during elastic collisions , 2011 .

[42]  Paul W. Cleary,et al.  Industrial particle flow modelling using discrete element method , 2009 .

[43]  Paul W. Cleary,et al.  Modelling comminution patterns within a pilot scale AG/SAG mill , 2006 .

[44]  Paul W. Cleary,et al.  DEM prediction of particle flows in grinding processes , 2008 .

[45]  Indresan Govender,et al.  Circulation rate modelling of mill charge using position emission particle tracking , 2011 .

[46]  Paul W. Cleary,et al.  Centrifugal mill charge motion and power draw: comparison of DEM predictions with experiment , 2000 .