ISSN: 0304-128X ISSN: 2233-9558
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Publication history
Received October 8, 2022
Revised March 3, 2023
Accepted March 8, 2023
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Effects of Geometry and Operating Fluid on the Expansion Behavior of Liquid-Solid Fluidized Beds

1Department of Engineering, Meybod University, 8961699557, Meybod, Iran 2Department of Mechanical Engineering, Yazd University, 8915818411, Yazd, Iran 3Department of Mechanical Engineering, Tarbiat Modares University, 14115111, Tehran, Iran 4Department of Mechanical Engineering, Payam-e-Noor University, Tehran, Iran
Korean Chemical Engineering Research, May 2023, 61(2), 312-321(10), 10.9713/kcer.2023.61.2.312 Epub 31 May 2023
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Abstract

Fluidized beds have been widely used in industrial applications, which in most of them, the operating fluid is non-Newtonian. In this study, the combination of the lattice Boltzmann method (LBM) and the smoothed profile method has been developed for non-Newtonian power-law fluids. The validation of the obtained model were investigated by experimental correlations. This model has been used for numerical studying of changing the operating fluid and geometrical parameters on the expansion behavior in liquid-solid beds with both Newtonian and nonNewtonian fluids. Investigations were performed for seven different geometries, one Newtonian, and two nonNewtonian fluids. The power-law index was in the range of 0.8 to 1, and the results for the Newtonian fluidized beds show more porosity than the non-Newtonian ones. Furthermore, increasing the power-law index resulted in enhancing the bed porosity. On the other hand, bed porosity was decreased by increasing the initial bed height and the density of the solid particles. Finally, the porosity ratio in the bed was decreased by increasing the solid particle diameter.

References

1. Weber, E., Crown Ethers. Ullmann's Encyclopedia of Industrial Chemistry, 2000.
2. Mehrabi Gohari, E., et al., “Hydrodynamic Simulation of a Liquid–solid Fluidized Bed Using Lattice Boltzmann and Smoothed Profile Methods,” Asia-Pacific J. Chemical Engineering, 12(2),196-211(2017).
3. Lali, A., et al., “Behaviour of Solid Particles in Viscous Nonnewtonian Solutions: Settling Velocity, Wall Effects and Bed Expansion in Solid-liquid Fluidized Beds,” Powder Technology,57(1), 39-50(1989).
4. Yu, Y., C. Wen, and R. Bailie, “Power-law Fluids Flow Through Multiparticle System,” The Canadian Journal of Chemical Engineering, 46(3), 149-154(1968).
5. Mishra, P., Singh, D. and Mishra, I., “Momentum Transfer to Newtonian and Non-newtonian Fluids Flowing Through Packed and Fluidized Beds,” Chemical Engineering Science, 30(4), 397-405(1975).
6. Brea, F., Edwards, M. and Wilkinson, W., “The Flow of Nonnewtonian Slurries Through Fixed and Fluidised Beds,” Chemical Engineering Science, 31(5), 329-336(1976).
7. Kumar, S. and Upadhyay, S., “Mass and Momentum Transfer to Newtonian and Non-newtonian Fluids in Fixed and Fluidized Beds,” Industrial & Engineering Chemistry Fundamentals, 20(3),186-195(1981).
8. Kawase, Y. and Ulbrecht, J., “Mass and Momentum Transfer with Non-newtonian Fluids in Fluidized Beds,” Chemical Engineering Communications, 32(1-5), 263-288(1985).
9. Benedict, R. F., Kumaresan, G. and Velan, M., “Bed Expansion and Pressure Drop Studies in a Liquid-solid Inverse Fluidised Bed Reactor,” Bioprocess Engineering, 19(2), 137-142(1998).
10. Lakshmi, A. V., et al., “Minimum Fluidization Velocity and Friction Factor in a Liquid-solid Inverse Fluidized Bed Reactor,”Bioprocess Engineering, 22(5), 461-466(2000).
11. Richardson, J. and Zaki, W., “This Week’s Citation Classic,”Trans. Inst. Chem. Eng., 32, 35-53(1954).
12. Christopher, R. H. and Middleman, S., “Power-law Flow Through a Packed Tube,” Industrial & Engineering Chemistry Fundamentals, 4(4), 422-426(1965).
13. Machač, I., Ulbrichova, I., Elson, T. P. and Cheesman, D. J., “Fall of Spherical Particles Through Non-newtonian Suspensions,”Chemical Engineering Science, 50(20), 3323-3327(1995).
14. Ergun, S. and Orning, A. A., “Fluid Flow Through Randomly Packed Columns and Fluidized Beds,” Industrial & Engineering
Chemistry, 41(6), 1179-1184(1949).
15. Mehrabi Gohari, E., Sefid, M. and Jahanshahi Javaran, E.,“Numerical Simulation of the Hydrodynamics of An Inverse Liquid–solid Fluidized Bed Using Combined Lattice Boltzmann and Smoothed Profile Methods,” Journal of Dispersion Science and Technology, 38(10), 1471-1482(2017).
16. Boyd, J., Buick, J. and Green, S., “A Second-order Accurate Lattice Boltzmann Non-newtonian Flow Model,” Journal of Physics A: Mathematical and General, 39(46), 14241(2006).
17. Chhabra, R. P., Comiti, J. and Machač, I., “Flow of Non-newtonian Fluids in Fixed and Fluidised Beds,” Chemical Engineering
Science, 56(1), 1-27(2001).

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