Transport Phenomena and Fluid Mechanics
Heat and mass transfer in calcination of limestone particles
Article first published online: 20 OCT 2011
DOI: 10.1002/aic.12774
Copyright © 2011 American Institute of Chemical Engineers (AIChE)
Additional Information
How to Cite
Takkinen, S., Saastamoinen, J. and Hyppänen, T. (2012), Heat and mass transfer in calcination of limestone particles. AIChE J., 58: 2563–2572. doi: 10.1002/aic.12774
Publication History
- Issue published online: 5 JUL 2012
- Article first published online: 20 OCT 2011
- Accepted manuscript online: 12 SEP 2011 11:18AM EST
- Manuscript Revised: 13 AUG 2011
- Manuscript Received: 14 MAR 2011
Funded by
- Academy of Finland. Grant Numbers: 124368, 123938
- Abstract
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- Cited By
Keywords:
- mass transfer;
- mathematical modeling;
- heat transfer;
- reaction kinetics;
- circulating fluidized beds
Abstract
The heat and mass-transfer phenomena occurring during the calcination of limestone particles was studied by means of modeling. The applicability of two modeling methods for calcination was compared under different conditions. An unsteady numerical particle model with mass, momentum, energy balance, and shrinking core models were chosen for the study. The influence of different phenomena (chemical kinetics, advective and diffusive mass transfer, and heat transfer) in different conditions was evaluated with the aid of dimensionless parameters, and their relative importance was shown in a regime chart. Especially, the significance of advection was studied and its importance in high CO2 concentration was observed. Local temperatures inside the particle were obtained by solving a dynamic energy balance in each particle layer including calcination reaction energy and conduction heat transfer. Noticeable temperature differences between constant ambient conditions and the particle were observed. © 2011 American Institute of Chemical Engineers AIChE J, 58: 2563–2572, 2012

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