CHANG Qi, LIU Yujun, XU Ji, et al. Particle-scale study on scale-up criteria for spout-fluidized beds: from geometric similarity to functional similarity[J/OL]. CIESC Journal, 2026.
DOI:
CHANG Qi, LIU Yujun, XU Ji, et al. Particle-scale study on scale-up criteria for spout-fluidized beds: from geometric similarity to functional similarity[J/OL]. CIESC Journal, 2026.DOI: 10.11949/0438-1157.20260468.
Particle-scale study on scale-up criteria for spout-fluidized beds: from geometric similarity to functional similarity
The industrial scale-up of spout-fluidized beds has long been hindered by the failure of traditional dimensionless group similarity criteria
partly due to inherent instabilities such as the spout deflection that break the geometric similarity. From the particle-scale perspective
CFD-DEM simulations are conducted for spout-fluidized beds before and after geometric scaling
investigating the particle motion and mixing behavior under six operating conditions (the base bed
the strictly similarity-scaled bed
and the non-strictly similarity-scaled bed) across three flow regimes: intermediate
spouting
and jet. The results reveal that spout deflection disrupts the three-zone structure and enhances mixing
compensating for the loss of mixing performance caused by scale-up. A linear correlation is observed between the mixing time and effective circulation time
confirming that the macro-circulation dominates the mixing process. Based on these findings
a quantitative relationship between the mixing time and effective circulation time is established
and the effective circulation time is proposed as a similarity criterion for scale-up
shifting the scale-up objective from pursuing the geometric similarity to ensuring the functional similarity in the mixing performance.
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