In this study, phenomenon of bubbling is investigated using CFD-DEM and experiments. A CFD-DEM simulation is setup to model the fluidized beds of different sizes. Geldart D particles of 1.2 mm diameter and 1000 Kg/m3 density are modelled. Study revealed different types of fluidization regimes as stated in the literature. An experimental setup is built to obtain the results for the comparison. Comparison revealed that results obtained from both methodologies; CFD-DEM and experiments are in reasonable agreement.
References
1.
DavidsonJ.F. and HarrisonD., Fluidized Particles (first ed.).1963: Cambridge University Press, Cambridge, New York.
2.
KuniiD. and LevenspielO., Fluidization Engineering.1991: Butterworth-Heinemann.
3.
DaviesR.M. and TaylorG., The Mechanics of Large Bubbles Rising through Extended Liquids and through Liquids in Tubes. Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences1950. 200(1062): p. 375–390.
4.
StewartP.S.B. and DavidsonJ.F., Slug flow in fluidised beds. Powder Technology1967. 1(2): p. 61–80.
5.
RudolphV. and JuddM.R.. Circulation and slugging in a fluid bed gasifier fitted with a draft tube. in Circulating Fluidized Bed Technology.1985. Pergamon Press, New York.
6.
YatesJ.G., Fundamentals of fluidized-bed chemical processes.1983, London: Butterworths.
7.
MüllerC.R., Oscillations in gas-fluidized beds: Ultra-fast magnetic resonance imaging and pressure sensor measurements. Powder Technology2007. 177(2): p. 87–98.
8.
LimK.S. and AgarwalP.K., Bubble velocity in fluidized beds: The effect of non-vertical bubble rise on its measurement using submersible probes and its relationship with bubble size. Powder Technology1992. 69(3): p. 239–248.
9.
GeldartD., Types of gas fluidization. Powder Technology1973. 7(5): p. 285–292.
10.
MATLAB®, version 7.14.0.739.2012, The MathWorks Inc.: Natick, Massachusetts.
11.
AndersonT.B. and JacksonR., Fluid Mechanical Description of Fluidized Beds. Equations of Motion. Industrial & Engineering Chemistry Fundamentals1967. 6(4): p. 527–539.
12.
CroweC.T.SommerfeldM., and TsujiY., Multiphase Flows With Droplets and Particles.1998: CRC Press.
13.
KhawajaH., Quantitative Analysis of Accuracy of Voidage Computations in CFD-DEM Simulations. The Journal of Computational Multiphase Flows2012. 4(2): p. 183–192.
14.
PatankarS.V., Numerical Heat Transfer and Fluid Flow.1980: Taylor & Francis.
15.
AndersonJ.D., Computational fluid dynamics: the basics with applications.1995: McGraw-Hill.
16.
CourantR.FriedrichsK., and LewyH., Über die partiellen Differenzengleichungen der mathematischen Physik. Mathematische Annalen1928. 100(1): p. 32–74.
17.
HirschC., Numerical Computation of Internal and External Flows: Fundamentals of Computational Fluid Dynamics.2007: Elsevier/Butterworth-Heinemann.
18.
ErgunS., Fluid flow through packed columns. Chem. Process Eng. London1952. 1: p. 89–94.
19.
WenC.Y. and YuY.H., Mechanics of fluidization. Chem. Eng. Prog. Symp. Series., 1966(62): p. 100–111.
20.
Di FeliceR., The voidage function for fluid-particle interaction systems. International Journal of Multiphase Flow1994. 20(1): p. 153–159.
21.
BeetstraR.van der HoefM.A., and KuipersJ.A.M., Numerical study of segregation using a new drag force correlation for polydisperse systems derived from lattice-Boltzmann simulations. Chemical Engineering Science2007. 62(1–2): p. 246–255.
22.
MüllerC.R., Granular temperature: Comparison of Magnetic Resonance measurements with Discrete Element Model simulations. Powder Technology2008. 184(2): p. 241–253.
23.
GearC.W., Numerical initial value problems in ordinary differential equations.1971: Prentice-Hall.
24.
HairerE.NørsettS.P., and WannerG., Solving Ordinary Differential Equations: Nonstiff problems.1993: Springer.
25.
van der HoefM.A., Numerical simulation of dense gas-solid fluidized beds: A multiscale modeling strategy, in Annual Review of Fluid Mechanics.2008, Annual Reviews: Palo Alto. p. 47–70.
26.
CundallP.A. and StrackO.D.L., A discrete numerical model for granular assemblies. Geotechnique1979. 29(1): p. 47–65.
27.
ThirdJ., Tangential velocity profiles of granular material within horizontal rotating cylinders modelled using the DEM. Granular Matter2010. 12(6): p. 587–595.
28.
TsujiY.TanakaT., and IshidaT., Lagrangian numerical simulation of plug flow of cohesionless particles in a horizontal pipe. Powder Technology1992. 71(3): p. 239–250.
29.
TsujiY.KawaguchiT., and TanakaT., Discrete particle simulation of two-dimensional fluidized bed. Powder Technology1993. 77(1): p. 79–87.
30.
van der HoefM.A.van Sint AnnalandM., and KuipersJ.A.M., Computational fluid dynamics for dense gas–solid fluidized beds: a multi-scale modeling strategy. Chemical Engineering Science2004. 59(22–23): p. 5157–5165.
31.
HertzH., Über die Berührung fester elastischer Körper. J. Reine Angew. Mat., 1882(92): p. 156–171.
32.
MindlinR.D. and DeresiewiczH., Elastic Spheres in Contact Under Varying Oblique Forces. J. of Appl. Mech.1953. 20: p. 327.
33.
KhawajaH. and ParvezK., Validation of normal and frictional contact models of spherical bodies by FEM analysis. The International Journal of Multiphysics2010. 4(2): p. 175–185.
34.
BaryshevG.KhawajaH., and MoatamediM., Optimization of Particle Search Algorithm for CFD-DEM Simulations. The Journal of Computational Multiphase Flows2013. 5(3): p. 223–230.
35.
KhawajaH., CFD-DEM Simulation of Minimum Fluidisation Velocity in Two Phase Medium. The International Journal of Multiphysics2011. 5(2): p. 89–100.
36.
KhawajaH. and ScottS., CFD-DEM Simulation of Propagation of Sound Waves in Fluid Particles Fluidised Medium. The International Journal of Multiphysics2011. 5(1): p. 47–60.
37.
BoyceC.M., Novel fluid grid and voidage calculation techniques for a discrete element model of a 3D cylindrical fluidized bed. Computers & Chemical Engineering2014. 65: p. 18–27.