Volume 89
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Yan, C., Yuan, Y., Wei, X., & Zhu, J. (2024). Micro-flow structure at regime transition from bubbling to turbulent fluidization in a fluidized bed. Particuology, 89, 117-130. https://doi.org/10.1016/j.partic.2023.09.021
Micro-flow structure at regime transition from bubbling to turbulent fluidization in a fluidized bed
Chaoyu Yan a, Yue Yuan b c, Xiaoyang Wei b, Jesse Zhu c *
a State Key Laboratory of Heavy Oil Processing, Beijing Key Laboratory of Process Fluid Filtration and Separation, College of Mechanical and Transportation Engineering, China University of Petroleum, Beijing 102249, China
b China Beacons Institute, The University of Nottingham, Ningbo, 315100, China
c Department of Chemical and Biochemical Engineering, University of Western Ontario, London, Ontario, N6A 5B9, Canada
10.1016/j.partic.2023.09.021
Volume 89, June 2024, Pages 117-130
Received 2 March 2023, Revised 18 September 2023, Accepted 26 September 2023, Available online 26 October 2023, Version of Record 6 December 2023.
E-mail: jzhu@uwo.ca

Highlights

• A coupling data processing methodology was proposed for fluidization analysis.

• Studied multiscale hydrodynamics during bubbling-turbulent fluidization transition.

• Micro-scale signals majorly reflected the bubbling fluidization behavior.

• Meso-scale signals majorly highlighted the flow behavior of turbulent fluidization.


Abstract

Gas-solid fluidized beds have found extensive utilization in frontline manufacturing, in particular as low-velocity beds. The fluidization status, the bubbling or turbulent flow regime and the transition in between, determine the system performance in practical applications. Though the convoluted hydrodynamics are quantitively evaluated through numerous data-processing methodologies, none of them alone can reflect all the critical information to identify the transition from the bubbling to the turbulent regime. Accordingly, this study was to exploit a coupling data processing methodology, in the combination of standard deviation, power spectrum density, probability density function, wavelet transform, and wavelet multiresolution method, to jointly explain the micro-flow structure at the regime transition from bubbling to turbulent fluidization. The transient differential pressure fluctuation was measured for the evaluation in a fluidized bed (0.267 m i.d. × 2.5 m height) with FCC catalysts () at different superficial gas velocities (0.02–1.4 m/s). The results show that the onset of turbulent fluidization starts earlier in the top section of the bed than in the bottom section. The wavelet decomposition displays that the fluctuation of differential pressure mainly concentrates on the sub-signals with an intermediate frequency band. These sub-signals could be synthesized into three types of scales (micro-scale, meso-scale, and macro-scale), representing the multi-scale hydrodynamics in the fluidized bed. The micro-scale signal has the characteristic information of bubbling fluidization, and the characteristic information of turbulent fluidization is mainly represented by the meso-scale signal. This work provides a systematic comprehension of fluidization status assessment and serves as an impetus for more coupling analysis in this sector.


Graphical abstract
Keywords
Flow regime transition; Bubbling fluidization; Turbulent fluidization; Micro-flow structure; Differential pressure fluctuation