Fluidized combustion of char and volatiles from coal
- 1 November 1984
- journal article
- research article
- Published by Wiley in AIChE Journal
- Vol. 30 (6) , 881-889
- https://doi.org/10.1002/aic.690300602
Abstract
This paper reviews the literature about fluidized combustion of char and volatiles from coal. While the rate of combustion of particles bigger than about 2 mm is mainly limited by the rate of diffusion of oxygen, there is usually an effect of chemical rate. As particle diameter decreases, the influence of chemical rate increases. Char particles are porous and combustion occurs in pores near their exterior. Char reactivity can be modelled by an effective pore area for combustion.At high bed temperatures (>1,150 K), the rate of combustion of volatiles is limited by the rate of mixing of fuel and oxygen. At low bed temperatures (<1,000 K), combustion reactions are inhibited by the inert particles in the bed.Keywords
This publication has 23 references indexed in Scilit:
- Particle size and density changes during fluidized-bed combustionThe Canadian Journal of Chemical Engineering, 1983
- Elutriation of attrited carbon fines in the fluidized combustion of a coalSymposium (International) on Combustion, 1982
- Model of solid gas reaction phenomena in the fluidized bed freeboardAIChE Journal, 1982
- The combustion rates of coal chars: A reviewSymposium (International) on Combustion, 1982
- The ignition and combustion of propane/air mixtures in a fluidised bedSymposium (International) on Combustion, 1982
- Fluidized bed combustion of wet brown coalFuel, 1980
- Coal devolatilization studies in support of the Westinghouse fluidized-bed coal gasification processFuel, 1979
- Carbon load and gas composition in a fluidized bed combustorSymposium (International) on Combustion, 1979
- The intrinsic reactivity of carbons to oxygenFuel, 1978
- Burning rate of carbon in fluidized bedsFuel, 1977