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Modeling Granular Material Mixing and Segregation Using a Multi-Scale Model Yu Liu, Prof. Marcial Gonzalez, Prof. Carl Wassgren School of Mechanical Engineering, Purdue University, West Lafayette, IN Motivation Granular material mixing and segregation Granular material mixing and segregation plays an important role in many industries ranging from pharmaceuticals to agrochemicals Predictive engineering design of industrial powder blenders remains underdeveloped due to the lack of quantitative modeling tools Objective Develop a predictive model of granular material mixing and segregation for industrial equipment Quantitatively predict the magnitude and rate of powder mixing and segregation Be capable of modeling industrial-scale equipment Demonstrate understanding to regulators in particle mixing and segregation Multi-Scale Model Diffusion correlations (3-D) is an anisotropic tensor instead of an isotropic value Off-diagonal components and are an order of magnitude smaller than the diagonal components and Utter et al. (2004, Phys Rev Lett, Vol. 69); Hsiau et al. (1999, J. Rheol, Vol. 43) = 1 2 + 2 ( + ) 2 2 = 1.9 1 according to Utter et al. (2004 , Phys Rev Lett, Vol. 69) 1 can be calibrated from DEM simulations or experiments Segregation correlations (2-D) Percolation is one of the most important mechanisms causing segregation acts in the direction of gravity According to Fan et al. (2014, J. Fluid Mech, Vol. 741): , = (1 − ) & , = − (1 − ) can be calibrated from DEM simulations or experiments FEM Model Model implementations The commercial FEM package Abaqus V6.14 is used to perform the simulations The Coupled Eulerian-Lagrangian (CEL) approach in Abaqus is applied to handle highly deformable material elements Within the Eulerian domain, the material stress-strain behavior is modeled using the Mohr-Coulomb elastoplastic (MCEP) model Material properties can be measured from independent, standard tests Bulk internal friction angle and cohesion => Shear test Bulk wall friction angle => Shear test Young’s Modulus and Poisson’s ratio => Uniaxial compression test FEM simulation results – velocity profile Rotating drum Conical and wedge-shaped hopper V blender and Tote blender 3-D Tote blender - mixing Compared with published experiments of binary mixing of glass beads in an industrial- scale Tote blender from Sudah et al. (2005, AIChE J., Vol. 51) All the parameters were calibrated from independent experiments Predictions of the mixing rate (relative standard deviation, RSD) from the multi-scale model compare well quantitatively to the published experimental data 2-D rotating drum - segregation Compared with published DEM simulations of binary segregation in a lab-scale rotating drum from Schlick et al. (2015, J. Fluid Mech, Vol. 765) All the parameters were derived directly from the published work Predictions compare well quantitatively to DEM results 2-D conical hopper - segregation Compared with published experiments of binary segregation of glass beads in different conical hoppers from Ketterhagen et al. (2007, Chem Eng Sci, Vol. 62) All the parameters were calibrated directly from the published work Predictions from the multi-scale model compare well quantitatively to experiments Macroscopic scale model Predicts: advective flow field Depends on: system geometries material bulk properties boundary conditions Method used: FEM Microscopic scale model Predicts: local diffusion / segregation rates Depends on: particle properties local material concentration local shear rate and and solid fraction Method used: DEM / Experiments Advection-diffusion-segregation equation = − ∙ +∙ −∙ Predicts: global material concentration Depends on: advective velocity (macro scale) diffusion and segregation rates (micro scale) Conical Wedge-shaped FEM simulations Conical Wedge-shaped DEM simulations FEM simulation DEM simulation V blender Tote blender Initial loading conditions Side-Side Top-Bottom Results 2-D rotating drum - mixing Compared with DEM simulations of binary mixing in a lab-scale rotating drum All the parameters were derived from published work by Fan et al. (2015, Phys Rev Lett, Vol. 115) Predictions of concentration profiles from the multi-scale model compare well quantitatively to DEM results Multi-scale model predictions FEM simulations Concentration of red particles Concentration of small particles DEM simulation Multi-scale model Concentration of red particles Concentration of small particles Concentration of small particles B. Utter, R.P. Behringer, Self-diffusion in dense granular shear flows, Phys. Rev. E - Stat. Nonlinear, Soft Matter Phys. 69 (2004) 1–12. O.S. Sudah, P.E. Arratia, A. Alexander, F.J. Muzzio, Simulation and experiments of mixing and segregation in a tote blender, AIChE J. 51 (2005) 836–844. S.-S. Hsiau, Y.-M. Shieh, Fluctuations and self-diffusion of sheared granular material flows, J. Rheol. (N. Y. N. Y). 43 (1999) 1049–1066. C.P. Schlick, Y. Fan, P.B. Umbanhowar, J.M. Ottino, R.M. Lueptow, Granular segregation in circular tumblers: Theoretical model and scaling laws, J. Fluid Mech. 765 (2015) 632–652. Y. Fan, C.P. Schlick, et al., Modelling size segregation of granular materials: The roles of segregation, advection and diffusion, J. Fluid Mech. 741 (2014) 252–279. Y. Liu, M. Gonzalez, C. Wassgren, Modeling Granular Material Blending in a Rotating Drum using a Finite Element Method and Advection-Diffusion Equation Multi-Scale Model, AIChE J. (2018). doi:10.1002/aic.16179. Y. Fan, P.B. Umbanhowar, J.M. Ottino, R.M. Lueptow, Shear-Rate-Independent Diffusion in Granular Flows, Phys. Rev. Lett. 115 (2015) 1–5. Y. Liu, A.T. Cameron, M. Gonzalez, C. Wassgren, Modeling granular material blending in a Tote blender using a finite element method and advection-diffusion equation multi-scale model, Powder Technol. (under review).
Transcript
PowerPoint PresentationModeling Granular Material Mixing and Segregation Using a Multi-Scale Model Yu Liu, Prof. Marcial Gonzalez, Prof. Carl Wassgren
School of Mechanical Engineering, Purdue University, West Lafayette, IN
Motivation Granular material mixing and segregation • Granular material mixing and segregation plays an important role in many
industries ranging from pharmaceuticals to agrochemicals • Predictive engineering design of industrial powder blenders remains
underdeveloped due to the lack of quantitative modeling tools
Objective Develop a predictive model of granular material mixing and segregation for industrial equipment • Quantitatively predict the magnitude and rate of powder mixing and segregation • Be capable of modeling industrial-scale equipment • Demonstrate understanding to regulators in particle mixing and segregation
Multi-Scale Model
Diffusion correlations (3-D) • is an anisotropic tensor instead of an isotropic value • Off-diagonal components and are an order of magnitude smaller than the
diagonal components and
Utter et al. (2004, Phys Rev Lett, Vol. 69); Hsiau et al. (1999, J. Rheol, Vol. 43)
• = 1 2 + 2( + ) 2
2 = 1.91 according to Utter et al. (2004 , Phys Rev Lett, Vol. 69) 1 can be calibrated from DEM simulations or experiments
Segregation correlations (2-D) • Percolation is one of the most important mechanisms causing segregation • acts in the direction of gravity
• According to Fan et al. (2014, J. Fluid Mech, Vol. 741): , = (1 − ) & , = − (1 − )
can be calibrated from DEM simulations or experiments
FEM Model Model implementations • The commercial FEM package Abaqus V6.14 is used to perform the simulations • The Coupled Eulerian-Lagrangian (CEL) approach in Abaqus is applied to handle
highly deformable material elements • Within the Eulerian domain, the material stress-strain behavior is modeled using
the Mohr-Coulomb elastoplastic (MCEP) model • Material properties can be measured from independent, standard tests
Bulk internal friction angle and cohesion => Shear test Bulk wall friction angle => Shear test Young’s Modulus and Poisson’s ratio => Uniaxial compression test
FEM simulation results – velocity profile • Rotating drum
• Conical and wedge-shaped hopper
• V blender and Tote blender
3-D Tote blender - mixing • Compared with published experiments of binary mixing of glass beads in an industrial-
scale Tote blender from Sudah et al. (2005, AIChE J., Vol. 51) • All the parameters were calibrated from independent experiments • Predictions of the mixing rate (relative standard deviation, RSD) from the multi-scale
model compare well quantitatively to the published experimental data
2-D rotating drum - segregation • Compared with published DEM simulations of binary segregation in a lab-scale rotating
drum from Schlick et al. (2015, J. Fluid Mech, Vol. 765) • All the parameters were derived directly from the published work • Predictions compare well quantitatively to DEM results
2-D conical hopper - segregation • Compared with published experiments of binary segregation of glass beads in different
conical hoppers from Ketterhagen et al. (2007, Chem Eng Sci, Vol. 62) • All the parameters were calibrated directly from the published work • Predictions from the multi-scale model compare well quantitatively to experiments
Macroscopic scale model • Predicts: advective flow field • Depends on: system geometries material bulk properties boundary conditions
• Method used: FEM
Microscopic scale model • Predicts: local diffusion / segregation rates • Depends on: particle properties local material concentration local shear rate and and solid fraction
• Method used: DEM / Experiments
Advection-diffusion-segregation equation
= − + −
Conical Wedge-shaped
FEM simulations
Conical Wedge-shaped
DEM simulations
Side-Side Top-Bottom
Results 2-D rotating drum - mixing • Compared with DEM simulations of binary mixing in a lab-scale rotating drum • All the parameters were derived from published work by Fan et al. (2015, Phys Rev
Lett, Vol. 115) • Predictions of concentration profiles from the multi-scale model compare well
quantitatively to DEM results
Multi-scale model predictionsFEM simulations
DEM simulation Multi-scale model
Concentration of red particles
Concentration of small particles
Concentration of small particles

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