LAPSE:2023.2058
Published Article

LAPSE:2023.2058
Hydrodynamic Predictions of the Ultralight Particle Dispersions in a Bubbling Fluidized Bed
February 21, 2023
Abstract
Particle and gas flow characteristics are numerically simulated by means of a proposed gas−particle second-order moment two-fluid model with particle kinetic−friction stress model in a bubbling fluidized bed. Anisotropic behaviors of gas−solid two-phase stresses and their interactions are fully considered by the two-phase Reynolds stress model and their closure correlations. The dispersion behaviors of the non-spherical expand graphite and spherical heavy particles are predicted by using the parameters of distributions of particle velocity, porosity, granular temperature, and dominant frequency. Compared to particles density 2700 kg/m3, ultralight particles exhibit the higher voidages with big bubbles and larger axial-averaged velocity of particles and stronger dispersion behaviors. Maximum granular temperature is approximately 3.0 times greater than that one, and dominant frequency for axial porosity fluctuations is 1.5 Hz that is 1/3 time as larger as that heavy particle.
Particle and gas flow characteristics are numerically simulated by means of a proposed gas−particle second-order moment two-fluid model with particle kinetic−friction stress model in a bubbling fluidized bed. Anisotropic behaviors of gas−solid two-phase stresses and their interactions are fully considered by the two-phase Reynolds stress model and their closure correlations. The dispersion behaviors of the non-spherical expand graphite and spherical heavy particles are predicted by using the parameters of distributions of particle velocity, porosity, granular temperature, and dominant frequency. Compared to particles density 2700 kg/m3, ultralight particles exhibit the higher voidages with big bubbles and larger axial-averaged velocity of particles and stronger dispersion behaviors. Maximum granular temperature is approximately 3.0 times greater than that one, and dominant frequency for axial porosity fluctuations is 1.5 Hz that is 1/3 time as larger as that heavy particle.
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Keywords
bubbling fluidized bed, gas–particle two-phase turbulent flows, non-spherical expand graphite, particle dispersions, particle kinetic-friction stress
Suggested Citation
Liu H, Li G, Liu Y. Hydrodynamic Predictions of the Ultralight Particle Dispersions in a Bubbling Fluidized Bed. (2023). LAPSE:2023.2058
Author Affiliations
Liu H: School of Aerospace Engineering, Taizhou University, Taizhou 318000, China
Li G: School of Electronic and Information Engineering, Dalian Jiaotong University, Dalian 116028, China
Liu Y: School of Aerospace Engineering, Taizhou University, Taizhou 318000, China; Department of Engineering Mechanics, Tsinghua University, Beijing 100084, China [ORCID]
Li G: School of Electronic and Information Engineering, Dalian Jiaotong University, Dalian 116028, China
Liu Y: School of Aerospace Engineering, Taizhou University, Taizhou 318000, China; Department of Engineering Mechanics, Tsinghua University, Beijing 100084, China [ORCID]
Journal Name
Processes
Volume
10
Issue
7
First Page
1390
Year
2022
Publication Date
2022-07-16
ISSN
2227-9717
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Original Submission
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PII: pr10071390, Publication Type: Journal Article
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LAPSE:2023.2058
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https://doi.org/10.3390/pr10071390
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Feb 21, 2023
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