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CFD DEM investigation on effects of particle size distribution a 2025 Partic

Wei Long, Jingbo Jia

2026enpyritefluidized bedparticle sizegas temperatureCFD-DEMminimum fluidization velocity

Abstract

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The multiphase reactive flow behavior of pyrites in fluidized roasters is closely related to particle size distribution (PSD) and gas temperature. The coupled computational fluid dynamics-discrete element method (CFD-DEM) is used to stress the effect of PSD and gas temperature on the minimum fluidization velocity (Umf). Firstly, the accuracy of the model is verified via the previously well-established correlations. Then, the influence of four types of PSD (Gaussian-type, Mono-type, Flat-type and Binary-type) and three temperatures on Umf is explored. Numerical results show that the Umf for the Flat-type PSD is the smallest among the four while the one for the Mono-type PSD is the largest. The minimum fluidization velocities for the Mono-type and Gaussian-type PSD share quite similar values. With the same PSD, increasing the gas temperature results in a decrease in the minimum fluidization velocity. Finally, predictive correlations for the minimum fluidization velocity of the gas-solid fluidized bed reactors are established based on the numerical results.

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Cite This Work

@article{3f7f4d57-da12-4dec-8fc5-5a61ba6f69e1,
  title={CFD DEM investigation on effects of particle size distribution a 2025 Partic},
  author={Wei Long and Jingbo Jia},
  year={2026},
  language={en}
}
TY  - JOUR
TI  - CFD DEM investigation on effects of particle size distribution a 2025 Partic
AU  - Wei Long
AU  - Jingbo Jia
PY  - 2026
LA  - en
ER  -

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