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Drying Kinetics in the Riser of Circulat

N. Balasubramanian, C. Srinivasanakkann

2026endryingfluidized bedkineticschemical engineering

Abstract

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This study investigates the drying kinetics within the riser of a circulating fluidized bed equipped with internals, aiming to enhance the understanding of drying processes in such systems. Experiments were conducted using particle sizes to analyze the impact of particle size on drying rates. The methodology involved varying the initial moisture content of solids and measuring the outlet moisture content after processing. Results indicated a clear correlation between particle size and drying efficiency, revealing that larger particles exhibited reduced drying rates due to decreased surface area per unit weight. Additionally, an increase in the initial moisture content of the solids resulted in higher outlet moisture levels, suggesting that moisture retention is influenced by the initial condition of the pellets. The findings demonstrate the efficacy of circulating fluidized beds for drying applications, particularly for materials with high moisture or fluidization challenges, offering insights into potential operational improvements for industrial drying processes.

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Cite This Work

@article{364652b0-d476-4ada-af5e-130404a452b9,
  title={Drying Kinetics in the Riser of Circulat},
  author={N. Balasubramanian and C. Srinivasanakkann},
  year={2026},
  language={en}
}
TY  - JOUR
TI  - Drying Kinetics in the Riser of Circulat
AU  - N. Balasubramanian
AU  - C. Srinivasanakkann
PY  - 2026
LA  - en
ER  -

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