Modelling of fluidised-bed coal gasifiers: elimination of the combustion product distribution coefficient by considering homogeneous combustion

Author:

Yan Hong-ming,Zhang Dong-ke

Publisher

Elsevier BV

Subject

Industrial and Manufacturing Engineering,Process Chemistry and Technology,Energy Engineering and Power Technology,General Chemical Engineering,General Chemistry

Reference34 articles.

1. J.R. Arthur, Reactions Between Carbon and Oxygen., Trans. Faraday. Soc. (1950) 164–178.

2. M.A. Field, D.W. Gill, B.B. Morgan, P.G.W. Hawksley, Combustion of Pulverized Coal, BCURA, Leaherhead, UK, 1967.

3. The temperature of burning carbon particles in fluidised beds;Ross;Trans. Inst. Chem. Eng.,1981

4. R.D. La Nauze, K. Jung, The kinetics of combustion of petroleum coke particles in a fluidised-bed combustor, 19th Symp. (International) on Combustion, The Combustion Institute, Pittsburgh, 1982, pp. 1087–1092.

5. G.B. Schluter, T.M. Linjewile, D.K. Zhang, Measurement of CO/CO2 Product Ratio from Single Particle Combustion in an Incipiently Fluidised Bed and Char Reactivity, 3rd Asian-Pacific Int. Symposium on Combustion and Energy Utilisation, 1995, pp. 366–371.

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