Since 1963
ARTICLE
Numerical simulation of the particle settling in a Bingham fluid using the two-way coupling CFD-DEM scheme
1
Federal University of Technology – Paraná (UTFPR), Mechanical Engineering, Curitiba, Paraná, Brazil
Submission date: 2021-11-22
Final revision date: 2022-03-24
Acceptance date: 2022-04-21
Online publication date: 2022-06-12
Publication date: 2022-07-30
Corresponding author
Joviano Janjar Casarin
Mechanical Engineering, Technological Federal University of Paraná, Curitiba, Brazil
Mechanical Engineering, Technological Federal University of Paraná, Curitiba, Brazil
Journal of Theoretical and Applied Mechanics 2022;60(3):409-422
KEYWORDS
TOPICS
ABSTRACT
The computational fluid dynamics coupled with the discrete element method is widely employed
to simulate particle-fluid interactions in solid-liquid flows. The restrictions imposed
by the CFD-DEM scheme to very fine meshes contribute to a scant amount of numerical
results of particle settling in viscoplastic fluids. This paper presents the two-way coupling
CFD-DEM simulation of the particle sedimentation in a quiescent Bingham fluid. The results
for terminal particle velocity showed good agreement with the experimental data.
Owing to the viscoplastic behavior of the fluid, low values of the relaxation parameter of
the solid-phase must be specified to obtain accurate results.
REFERENCES (25)
1.
Akhshik S., Behzad M., Rajabi M., 2016, CFD-DEM simulation of the hole cleaning process in a deviated well drilling: the effects of particle shape, Particuology, 25, 72-82.
2.
Atapattu D.D., Chhabra R.P., Uhlherr P.H.T., 1995, Creeping sphere motion in Herschel-Bulkley fluids: flow field and drag, Journal of Non-Newtonian Fluid Mechanics, 59, 245-265.
3.
Beverly C.R., Tanner R.I., 1989, Numerical analysis of extrudate swell in viscoelastic materials with yield stress, Journal of Rheology, 33, 989-1009.
4.
Bird R.B., Dai G.C., Yarusso B.J., 1983, The rheology and flow of viscoplastic materials, Reviews in Chemical Engineering, 1, 1-70.
6.
Cocco R., Fullmer W.D., Liu P., Hrenya C.M., 2017, CFD-DEM modeling the small to understand the large, Chemical Engineering Progress, 113, 38-45.
7.
Coussot P., 2005, Rheometry of Pastes, Suspensions, and Granular Materials: Applications in Industry and Environment, John Wiley & Sons, Inc., Hoboken, NJ, USA.
8.
Crowe C.T., Schwarzkopf J.D., Sommerfeld M., Tsuji Y., 2012, Multiphase Flows with Droplets and Particles, 2nd ed. CRC Press.
9.
Cundall P.A., Strack O.D.L., 1979, A discrete numerical model for granular assemblies, Géotechnique, 29, 47-65.
10.
Deb S., Tafti D.K., 2013, A novel two-grid formulation for fluid-particle systems using the discrete element method, Powder Technology, 246, 601-616.
11.
Dedegil M.Y., 1987, Drag coefficient and settling velocity of particles in non-Newtonian suspensions, Journal of Fluids Engineering, 109, 319-323.
12.
Deen N.G.,Van Sint Annaland M., Van der Hoef M.A., Kuipers J.A.M., 2007, Review of discrete particle modeling of fluidized beds, Chemical Engineering Science, 62, 28-44.
13.
Glowinski R., Wachs A., 2011, On the numerical simulation of viscoplastic fluid flow, [In:] Handbook of Numerical Analysis, Elsevier, 483-717.
14.
Kohnen G., Rüger M., Sommerfeld M., 1994, Convergence behaviour for numerical calculations by the Euler/Lagrange method for strongly coupled phases, ASME-PUBLICATIONS-FED, 185, 191-202.
15.
Lali A.M., Khare A.S., Joshi J.B., Nigam K.D.P., 1989, Behaviour of solid particles in viscous non-Newtonian solutions: settling velocity, wall effects and bed expansion in solid-liquid fluidized beds, Powder Technology, 57, 39-50.
16.
Macosko C.W., 1994, Rheology Principles, Measurements, and Applications. Advances in Interfacial Engineering Series, VCH, New York.
17.
Oliveira G.M., Franco A.T., Negrão C.O.R., Martins A.L., Silva R.A., 2013, Modeling and validation of pressure propagation in drilling fluids pumped into a closed well, Journal of Petroleum Science and Engineering, 103, 61-71.
18.
Patankar S.V., 1980, Numerical Heat Transfer and Fluid Flow. Series in Computational Methods in Mechanics and Thermal Sciences, Hemisphere Pub. Corp., McGraw-Hill,Washington, New York.
19.
Prashant, Derksen J.J., 2011, Direct simulations of spherical particle motion in Bingham liquids, Computers and Chemical Engineering, 35, 1200-1214.
20.
Saha G., Purohit N.K., Mitra A.K., 1992, Spherical particle terminal settling velocity and drag in Bingham liquids, International Journal of Mineral Processing, 36, 273-281.
21.
Sosnowski M., Gnatowska R., Sobczyk J., Wodziak W., 2019, Computational domain discretization for CFD analysis of flow in a granular packed bed, Journal of Theoretical and Applied Mechanics, 57, 833-842.
22.
Thompson R.L., Soares E.J., 2016, Viscoplastic dimensionless numbers, Journal of Non-Newtonian Fluid Mechanics, 238, 57-64.
23.
Tsuji Y., Kawaguchi T., Tanaka T., 1993, Discrete particle simulation of two-dimensional fluidized bed, Powder Technology, 77, 79-87.
24.
Valentik L.,Whitmore R.L., 1965, The terminal velocity of spheres in Bingham plastics, British Journal of Applied Physics, 16, 1197-1203.
25.
Yao L.M., Xiao Z.M., Liu J.B., Zhang Q., Wang M., 2020, An optimized CFD-DEM method for fluid-particle coupling dynamics analysis, International Journal of Mechanical Sciences, 174, 105503.
Share
RELATED ARTICLE
| eISSN: | 2543-6309 |
| ISSN: | 1429-2955 |
