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In relation to this article, we declare that there is no conflict of interest.
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Received May 9, 2003
Accepted October 6, 2003
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Modeling Percolative Fragmentation during Conversion of Entrained Char Particles

Istituto Ricerche sulla Combustione - CNR, via Metastasio 17 80125 Napoli, Italy
miccio@irc.na.cnr.it
Korean Journal of Chemical Engineering, March 2004, 21(2), 404-411(8), 10.1007/BF02705428
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Abstract

A numerical model of carbonaceous particle conversion under chemical and external diffusion control is proposed. The model accounts for different classes of particles which undergo chemical conversion in parallel with percolative fragmentation. It applies to typical conditions of entrained flow reactors. The system of algebraic and differential equations has been numerically solved. Results include the total carbon conversion as well as the determination of particle properties along the reactor. The model correctly predicts the change of the conversion rate at varying temperature, initial oxidant concentration and excess oxidant ratio. The influence of percolation parameters is also relevant and claims further investigations for more accurate determination. A comparison with experimental data available in literature is also provided.

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