Segregation of binary particles in gas-solid fluidized bed

  • Yaxiong Yu 1 ,
  • Feng Lu 1 ,
  • Xuan He 2 ,
  • Fei Wei 1,3 ,
  • Chenxi Zhang , 1,3,4
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  • 1. Beijing Key Laboratory of Green Chemical Reaction Engineering and Technology, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
  • 2. School of Chemical Engineering and Technology, Xi’an Jiaotong University, Xi’an 710049, China
  • 3. Ordos Laboratory, Ordos 017010, China
  • 4. Institute for Carbon Neutrality, Tsinghua University, Beijing 100084, China
cxzhang@mail.tsinghua.edu.cn

Received date: 13 Dec 2023

Accepted date: 31 Jan 2024

Copyright

2024 Higher Education Press

Abstract

Particle segregation and mixing behavior play a crucial role in industrial processes. This study investigates the saturated jetsam fraction, which indicates the maximum capacity of flotsam to entrain jetsam, in an initially separated binary fluidized bed with particle size differences. According to the value of saturated jetsam fraction, three distinct regimes—segregation, mixing, and an intermediate regime—are identified. Moreover, intriguing relationships between the saturated jetsam fraction and superficial gas velocity are observed, exhibiting monotonic trends in both the segregation and mixing regimes, while a unique volcano-shaped curve in the intermediate regime. Additionally, a comprehensive entrainment model based on two-fluid model elucidates the observed phenomena, emphasizing the significance of mixing behavior in fluidized layer on the saturated jetsam fraction. This work offers potential insights for evaluating segregation in industrial applications.

Cite this article

Yaxiong Yu , Feng Lu , Xuan He , Fei Wei , Chenxi Zhang . Segregation of binary particles in gas-solid fluidized bed[J]. Frontiers of Chemical Science and Engineering, 2024 , 18(6) : 68 . DOI: 10.1007/s11705-024-2426-0

Competing interests

The authors declare that they have no competing interests.

Acknowledgements

We would like to thank the financial support from the National Natural Science Foundation of China (Grant Nos. 22308187, 22208186, 22278238, and 22238004), the Beijing Nova Program (Grant No. 2022118), the Key Research and Development Program of Inner Mongolia and Ordos, and the Ordos-Tsinghua Innovative & Collaborative Research Program in Carbon Neutrality (Ordos Laboratory). We would also like to express our gratitude to Fan Duan of Xi’an Jiaotong University for his valuable discussions on the manuscript.

Electronic Supplementary Material

Supplementary material is available in the online version of this article at https://doi.org/10.1007/s11705-024-2426-0 and is accessible for authorized users.
1
Burtally N , King P , Swift M R . Spontaneous air-driven separation in vertically vibrated fine granular mixtures. Science, 2002, 295(5561): 1877–1879

DOI

2
Javier Brey J , Moreno F , Garcia-Rojo R , Ruiz-Montero M J . Hydrodynamic maxwell demon in granular systems. Physical Review E: Statistical Physics, Plasmas, Fluids, and Related Interdisciplinary Topics, 2001, 65(1): 011305

DOI

3
McLaren C P , Kovar T M , Penn A , Müller C R , Boyce C M . Gravitational instabilities in binary granular materials. Proceedings of the National Academy of Sciences of the United States of America, 2019, 116(19): 9263–9268

DOI

4
Galvin J E , Dahl S R , Hrenya C M . On the role of non-equipartition in the dynamics of rapidly flowing granular mixtures. Journal of Fluid Mechanics, 2005, 528: 207–232

DOI

5
Yu Y , Lu F , Bai H , Wei F , Zhang C . Discovery of asymmetric distribution of fine particles in fluidization using signal deflection reconstruction measurement. Chemical Engineering Science, 2024, 285: 119564

DOI

6
Jiang Z , Tsuji T , Oshitani J , Washino K , Tanaka T . Reverse to forward density segregation depending on gas inflow velocity in vibrated fluidized beds. Physics of Fluids, 2023, 35(3): 033313

DOI

7
Di Maio F P , Di Renzo A , Vivacqua V . Extension and validation of the particle segregation model for bubbling gas-fluidized beds of binary mixtures. Chemical Engineering Science, 2013, 97: 139–151

DOI

8
Yu Y , Lu F , Bai H , Wei F , Zhang C . Effect of fines addition on heat transfer performance in gas-solid fluidized bed: an integrated experimental, simulation, and theoretical study. Chemical Engineering Journal, 2023, 476: 146806

DOI

9
Du B , Fan L S , Wei F , Warsito W . Gas and solids mixing in a turbulent fluidized bed. AIChE Journal, 2002, 48(9): 1896–1909

DOI

10
Chen J L P , Keairns D L . Particle segregation in a fluidized bed. Canadian Journal of Chemical Engineering, 1975, 53(4): 395–402

DOI

11
Duan F , Zhao L , Chen X , Zhou Q . Fluid-particle drag and particle-particle drag in low-reynolds-number bidisperse gas-solid suspensions. Physics of Fluids, 2020, 32(11): 113311

DOI

12
Mehrabadi M , Tenneti S , Subramaniam S . Importance of the fluid-particle drag model in predicting segregation in bidisperse gas-solid flow. International Journal of Multiphase Flow, 2016, 86: 99–114

DOI

13
Gray J M N T . Particle segregation in dense granular flows. Annual Review of Fluid Mechanics, 2018, 50(1): 407–433

DOI

14
Kennedy S , Bretton R . Axial dispersion of spheres fluidized with liquids. AIChE Journal, 1966, 12(1): 24–30

DOI

15
Duan F , Yu Y , Chen X , Zhou Q . Particle-particle drag force in inertial bidisperse gas-particle suspensions. Journal of Fluid Mechanics, 2022, 952: A11

DOI

16
Shi K , He M , Zhang L , Zhao B , Wang J . Critical comparison of polydisperse kinetic theories using bidisperse dem data. Chemical Engineering Science, 2022, 263: 118062

DOI

17
Hoffmann A , Janssen L , Prins J . Particle segregation in fluidised binary mixtures. Chemical Engineering Science, 1993, 48(9): 1583–1592

DOI

18
Gibilaro L G , Rowe P N . A model for a segregating gas fluidised bed. Chemical Engineering Science, 1974, 29(6): 1403–1412

DOI

19
Kunii D , Levenspiel O . Bubbling bed model. Model for flow of gas through a fluidized bed. Industrial & Engineering Chemistry Fundamentals, 1968, 7(3): 446–452

DOI

20
Fan L T , Chang Y . Mixing of large particles in two-dimensional gas fluidized beds. Canadian Journal of Chemical Engineering, 1979, 57(1): 88–97

DOI

21
Moritomi H , Yamagishi T , Chiba T . Prediction of complete mixing of liquid-fluidized binary solid particles. Chemical Engineering Science, 1986, 41(2): 297–305

DOI

22
Chew J W , Hrenya C M . Link between bubbling and segregation patterns in gas-fluidized beds with continuous size distributions. AIChE Journal, 2011, 57(11): 3003–3011

DOI

23
Chew J W , Wolz J R , Hrenya C M . Axial segregation in bubbling gas-fluidized beds with gaussian and lognormal distributions of geldart group B particles. AIChE Journal, 2010, 56(12): 3049–3061

DOI

24
Geldart D , Baeyens J , Pope D , Van De Wijer P . Segregation in beds of large particles at high velocities. Powder Technology, 1981, 30(2): 195–205

DOI

25
Formisani B , Girimonte R , Longo T . The fluidization process of binary mixtures of solids: development of the approach based on the fluidization velocity interval. Powder Technology, 2008, 185(2): 97–108

DOI

26
Olivieri G , Marzocchella A , Salatino P . Segregation of fluidized binary mixtures of granular solids. AIChE Journal, 2004, 50(12): 3095–3106

DOI

27
Marzocchella A , Salatino P , Di Pastena V , Lirer L . Transient fluidization and segregation of binary mixtures of particles. AIChE Journal, 2000, 46(11): 2175–2182

DOI

28
Rao A , Curtis J S , Hancock B C , Wassgren C . Classifying the fluidization and segregation behavior of binary mixtures using particle size and density ratios. AIChE Journal, 2011, 57(6): 1446–1458

DOI

29
Zhang C , Li P , Lei C , Qian W , Wei F . Experimental study of non-uniform bubble growth in deep fluidized beds. Chemical Engineering Science, 2018, 176: 515–523

DOI

30
Bouillard J X , Gidaspow D . On the origin of bubbles and geldart’s classification. Powder Technology, 1991, 68(1): 13–22

DOI

31
Taylor G I . The formation of a blast wave by a very intense explosion i: theoretical discussion. Proceedings of the Royal Society of London Series A: Mathematical and Physical Sciences, 1950, 201(1065): 159–174

DOI

32
Taylor G I . The formation of a blast wave by a very intense explosion. ii. The atomic explosion of 1945. Proceedings of the Royal Society of London Series A: Mathematical and Physical Sciences, 1950, 201(1065): 175–186

DOI

33
Avillez M A , Mac Low M M . Mushroom-shaped structures as tracers of buoyant flow in the galactic disk. Astrophysical Journal, 2001, 551(1): L57–L61

DOI

34
Alghamdi Y A , Peng Z , Almutairi Z , Alibrahim H , Al-Alweet F M , Moghtaderi B , Doroodchi E . Assessment of correlations for minimum fluidization velocity of binary mixtures of particles in gas fluidized beds. Powder Technology, 2021, 394: 1231–1239

DOI

35
Andreux R , Gauthier T , Chaouki J , Simonin O . New description of fluidization regimes. AIChE Journal, 2005, 51(4): 1125–1130

DOI

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