An experimental insight of the hydrodynamics of microjet assisted fluidized bed of ultrafine particles

Strong interparticle forces (IPFs) in ultrafine powders lead to agglomeration and poor fluidization quality posing a major challenge in many industrial processes. This study investigates the use of a high-energy microjet to improve the fluidization of nanosilica. A 200 μm nozzle was used to inject a secondary flow at a sonic velocity of 312 m/s, creating intense, localized turbulence. Analysis of local pressure drop transients confirmed that this energy input effectively de-agglomerated the powder, particularly in the lower bed. The combination of the microjet with a primary inlet gas flow produced a substantial improvement in fluidization, achieving a maximum bed expansion of approximately ten times the initial height. Furthermore, by conducting successive runs, we demonstrated a significant persistence effect. The bed retained its improved hydrodynamic characteristics, responding more rapidly in subsequent runs, implying an irreversible microjet-induced change in the powder's agglomerate structure.

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Journal
Scientific Reports
Published
2025-11-11
DOI
https://doi.org/10.1038/s41598-025-22982-4
Primary Topic
Granular flow and fluidized beds
Type
article
Field-Weighted Citation Impact
0.00

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article

An experimental insight of the hydrodynamics of microjet assisted fluidized bed of ultrafine particles

Mohammad Asif, Syed Sadiq Ali, M. E. Ali Mohsin, S. K. Safdar Hossain
Scientific Reports
Granular flow and fluidized beds
article

An experimental insight of the hydrodynamics of microjet assisted fluidized bed of ultrafine particles

Mohammad Asif, Syed Sadiq Ali, M. E. Ali Mohsin, S. K. Safdar Hossain
article en

Abstract

Strong interparticle forces (IPFs) in ultrafine powders lead to agglomeration and poor fluidization quality posing a major challenge in many industrial processes. This study investigates the use of a high-energy microjet to improve the fluidization of nanosilica. A 200 μm nozzle was used to inject a secondary flow at a sonic velocity of 312 m/s, creating intense, localized turbulence. Analysis of local pressure drop transients confirmed that this energy input effectively de-agglomerated the powder, particularly in the lower bed. The combination of the microjet with a primary inlet gas flow produced a substantial improvement in fluidization, achieving a maximum bed expansion of approximately ten times the initial height. Furthermore, by conducting successive runs, we demonstrated a significant persistence effect. The bed retained its improved hydrodynamic characteristics, responding more rapidly in subsequent runs, implying an irreversible microjet-induced change in the powder's agglomerate structure.

Scientific ReportsVol. 15(1)
King Saud University (SA), King Faisal University (SA)
King Faisal University
Openalex Percentile: Top 65%
Granular flow and fluidized beds
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