Investigation of Gas-Solid Flows in a Spout Fluidized Bed on Drag and Solid Stress: CFD-DEM, TFM, and Experimental Validation
PDF

Keywords

spout fluidized bed
drag model
friction stress model
CFD-DEM
TFM

How to Cite

1.
Guo X, Liu G, Zhao J, Wang R, He Y. Investigation of Gas-Solid Flows in a Spout Fluidized Bed on Drag and Solid Stress: CFD-DEM, TFM, and Experimental Validation. J. Chem. Eng. Res. Updates. [Internet]. 2021 Sep. 22 [cited 2024 Nov. 21];8:1-23. Available from: https://avantipublisher.com/index.php/jceru/article/view/1004

Abstract

In this work, experimental and numerical simulation methods are used to study the gas-solid two-phase flow in a three-dimensional rectangular spouted bed. In particular, the TFM and the CFD-DEM simulation results are compared with experimental data of the spouted bed. The influence of different drag models and friction stress models on the applicability of the simulation technology, Gidaspow, BVK, Koch-Hill, and Syamal-O'Brein drag models are investigated, respectively. Besides, the influence of the Syamal (S-R-O) and Srivastava-Sundaresan (S-S) friction stress models considering different transition points on the flow characteristics of particles in a spouted bed is also studied. Experimental verification shows that the Gidaspow drag, and S-S friction stress models are more consistent with experimental results. The fountain height predicted by CFD-DEM is closer to the experiment. It is found that the heterogeneous flow structure resulted in such a phenomenon in that the bubble cap blocked the gas flow pathway and increased the drag coefficient, while the bypass of the gas phase near the walls in the bubble reduced the drag coefficient.

https://doi.org/10.15377/2409-983X.2021.08.1
PDF

References

Kunii D, Levenspiel O. Fluidization engineering [M]. Butterworth-Heinemann, 1991.

Mathur KB, Epstein N. Dynamics of spouted beds,Advances in Chemical Engineering: Elsevier, 1974; 111-191. https://doi.org/10.1016/S0065-2377(08)60286-0

Belhocine A. Numerical study of heat transfer in fully developed laminar flow inside a circular tube [J]. The International Journal of Advanced Manufacturing Technology, 2016; 85 (9): 2681-2692. https://doi.org/10.1007/s00170-015-8104-0

Ding J, Gidaspow D. A bubbling fluidization model using kinetic theory of granular flow [J]. AIChE journal, 1990; 36 (4): 523-538. https://doi.org/10.1002/aic.690360404

Gidaspow D, Jung J, Singh RK. Hydrodynamics of fluidization using kinetic theory: an emerging paradigm: 2002 Flour-Daniel lecture [J]. Powder Technology, 2004; 148 (2-3): 123-141. https://doi.org/10.1016/j.powtec.2004.09.025

Cundall PA, Strack OD. A discrete numerical model for granular assemblies [J]. geotechnique, 1979; 29 (1): 47-65. https://doi.org/10.1680/geot.1979.29.1.47

Tsuji Y, Kawaguchi T, Tanaka T. Discrete particle simulation of two-dimensional fluidized bed [J]. Powder technology, 1993; 77 (1): 79-87. https://doi.org/10.1016/0032-5910(93)85010-7

Moliner C, Marchelli F, Spanachi N, et al. CFD simulation of a spouted bed: Comparison between the Discrete Element Method (DEM) and the Two Fluid Model (TFM) [J]. Chemical Engineering Journal, 2019; 377: 120466. https://doi.org/10.1016/j.cej.2018.11.164

Zhao X-L, Li S-Q, Liu G-Q, et al. DEM simulation of the particle dynamics in two-dimensional spouted beds [J]. Powder Technology, 2008; 184 (2): 205-213. https://doi.org/10.1016/j.powtec.2007.11.044

Saidi M, Tabrizi HB, Grace JR, et al. Hydrodynamic investigation of gas-solid flow in rectangular spout-fluid bed using CFD-DEM modeling [J]. Powder Technology, 2015; 284: 355-364. https://doi.org/10.1016/j.powtec.2015.07.005

Marchelli F, Moliner C, Bosio B, et al. A CFD-DEM sensitivity analysis: The case of a pseudo-2D spouted bed [J]. Powder Technology, 2019; 353: 409-425. https://doi.org/10.1016/j.powtec.2019.05.035

Li L, Li B, Liu Z. Modeling of spout-fluidized beds and investigation of drag closures using OpenFOAM [J]. Powder Technology, 2017; 305: 364-376. https://doi.org/10.1016/j.powtec.2016.10.005

Koch D L, Hill R J. Inertial effects in suspension and porous-media flows [J]. Annual Review of Fluid Mechanics, 2001; 33 (1): 619-647. https://doi.org/10.1146/annurev.fluid.33.1.619

Gidaspow D. Multiphase flow and fluidization: continuum and kinetic theory descriptions[M]. Academic press, 1994.

Beetstra R, Van Der Hoef MA, Kuipers J. Drag force of intermediate Reynolds number flow past mono-and bidisperse arrays of spheres [J]. AIChE journal, 2007; 53 (2): 489-501. https://doi.org/10.1002/aic.11065

Pietsch S, Heinrich S, Karpinski K, et al. CFD-DEM modeling of a three-dimensional prismatic spouted bed [J]. Powder technology, 2017; 316: 245-255. https://doi.org/10.1016/j.powtec.2016.12.046

Estiati I, Tellabide M, Saldarriaga J, et al. Fine particle entrainment in fountain confined conical spouted beds [J]. Powder Technology, 2019; 344: 278-285. https://doi.org/10.1016/j.powtec.2018.12.035

Du W, Bao X, Xu J, et al. Computational fluid dynamics (CFD) modeling of spouted bed: Assessment of drag coefficient correlations [J]. Chemical Engineering Science, 2006; 61 (5): 1401-1420. https://doi.org/10.1016/j.ces.2005.08.013

Du W, Bao X, Xu J, et al. Computational fluid dynamics (CFD) modeling of spouted bed: Influence of frictional stress, maximum packing limit and coefficient of restitution of particles [J]. Chemical Engineering Science, 2006; 61(14): 4558-4570. https://doi.org/10.1016/j.ces.2006.02.028

Moliner C, Marchelli F, Ong L, et al. Sensitivity analysis and validation of a Two Fluid Method (TFM) model for a spouted bed [J]. Chemical Engineering Science, 2019; 207: 39-53. https://doi.org/10.1016/j.ces.2019.06.008

Stroh A, Alobaid F, Hasenzahl MT, et al. Comparison of three different CFD methods for dense fluidized beds and validation by a cold flow experiment [J]. Particuology, 2016; 29: 34-47. https://doi.org/10.1016/j.partic.2015.09.010

Lun C, Savage S B, Jeffrey D, et al. Kinetic theories for granular flow: inelastic particles in Couette flow and slightly inelastic particles in a general flowfield [J]. Journal of fluid mechanics, 1984; 140: 223-256. https://doi.org/10.1017/S0022112084000586

Carnahan NF, Starling KE. Equation of state for nonattracting rigid spheres [J]. The Journal of chemical physics, 1969; 51 (2): 635-636. https://doi.org/10.1063/1.1672048

Johnson PC, Jackson R. Frictional-collisional constitutive relations for granular materials, with application to plane shearing [J]. Journal of fluid Mechanics, 1987; 176: 67-93. https://doi.org/10.1017/S0022112087000570

Xu B, Yu A. Numerical simulation of the gas-solid flow in a fluidized bed by combining discrete particle method with computational fluid dynamics [J]. Chemical Engineering Science, 1997; 52 (16): 2785-2809. https://doi.org/10.1016/S0009-2509(97)00081-X

GoTz SR. Gekoppelte CFD/DEM-simulation blasenbildender wirbelschichten[M]. Shaker, 2006.

Liu G, Yu F, Lu H, et al. CFD-DEM simulation of liquid-solid fluidized bed with dynamic restitution coefficient [J]. Powder Technology, 2016; 304: 186-197. https://doi.org/10.1016/j.powtec.2016.08.058

Liu G, Yu F, Wang S, et al. Investigation of interstitial fluid effect on the hydrodynamics of granular in liquid-solid fluidized beds with CFD-DEM [J]. Powder Technology, 2017; 322: 353-368. https://doi.org/10.1016/j.powtec.2017.08.048

Zhao J, Shan T. Coupled CFD-DEM simulation of fluid-particle interaction in geomechanics [J]. Powder technology, 2013; 239: 248-258. https://doi.org/10.1016/j.powtec.2013.02.003

Ergun S. Fluid flow through packed columns [J]. Chem. Eng. Prog., 1952; 48: 89-94.

Wen CY. Mechanics of fluidization [C]. Chem. Eng. Prog. Symp. Ser., 1966: 100-111.

Syamlal M, O'brien T. Simulation of granular layer inversion in liquid fluidized beds [J]. International Journal of Multiphase Flow, 1988; 14 (4): 473-481. https://doi.org/10.1016/0301-9322(88)90023-7

Ancey C. Plasticity and geophysical flows: a review [J]. Journal of Non-Newtonian Fluid Mechanics, 2007; 142 (1-3): 4-35. https://doi.org/10.1016/j.jnnfm.2006.05.005

Syamlal M, Rogers W, Obrien TJ. MFIX documentation theory guide[R]. USDOE Morgantown Energy Technology Center, WV (United States), 1993. https://doi.org/10.2172/10145548

Schaeffer DG. Instability in the evolution equations describing incompressible granular flow [J]. Journal of differential equations, 1987; 66 (1): 19-50. https://doi.org/10.1016/0022-0396(87)90038-6

Srivastava A, Sundaresan S. Analysis of a frictional-kinetic model for gas-particle flow [J]. Powder technology, 2003; 129 (1-3): 72-85. https://doi.org/10.1016/S0032-5910(02)00132-8

Geldart D. Types of gas fluidization [J]. Powder technology, 1973; 7 (5): 285-292. https://doi.org/10.1016/0032-5910(73)80037-3

Lungu M, Siame J, Mukosha L. Comparison of CFD-DEM and TFM approaches for the simulation of the small scale challenge problem 1 [J]. Powder Technology, 2021; 378: 85-103. https://doi.org/10.1016/j.powtec.2020.09.071

Almohammed N, Alobaid F, Breuer M, et al. A comparative study on the influence of the gas flow rate on the hydrodynamics of a gas-solid spouted fluidized bed using Euler-Euler and Euler-Lagrange/DEM models [J]. Powder technology, 2014; 264: 343-364. https://doi.org/10.1016/j.powtec.2014.05.024

Belhocine A, Omar WZW. Analytical solution and numerical simulation of the generalized Levèque equation to predict the thermal boundary layer [J]. Mathematics and Computers in Simulation, 2021; 180: 43-60. https://doi.org/10.1016/j.matcom.2020.08.007

Moliner C, Marchelli F, Bosio B, et al. Modelling of Spouted and Spout-Fluid Beds: Key for Their Successful Scale Up [J]. Energies, 2017; 10 (11): 1729. https://doi.org/10.3390/en10111729

Zhao J, Liu G, Li W, et al. A comprehensive stress model for gas-particle flows in dense and dilute regimes [J]. Chemical Engineering Science, 2020; 226: 115833. https://doi.org/10.1016/j.ces.2020.115833

Goldschmidt M, Kuipers J, Van Swaaij WPM. Hydrodynamic modelling of dense gas-fluidised beds using the kinetic theory of granular flow: effect of coefficient of restitution on bed dynamics [J]. Chemical Engineering Science, 2001; 56 (2): 571-578. https://doi.org/10.1016/S0009-2509(00)00262-1

Jinghai L, Musun G. Heterogeneity in Vertical Cocurrent-Up Particle-Fluid Two Phase Flow [J]. Journal of Chemical Industry and Engineering (China), 1993; 1.

Yang N, Wang W, Ge W, et al. CFD simulation of concurrent-up gas-solid flow in circulating fluidized beds with structure-dependent drag coefficient [J]. Chemical Engineering Journal, 2003; 96 (1-3): 71-80. https://doi.org/10.1016/j.cej.2003.08.006

Creative Commons License

This work is licensed under a Creative Commons Attribution-NonCommercial 4.0 International License.

Copyright (c) 2021 Xinyao Guo, Guodong Liu, Junnan Zhao, Runchun Wang, Yurong He