Current coal combustion models are a useful tool in research but they use s
implified coal particle devolatilisation and combustion steps in order to m
eet computational limitations. The availability of more advanced computers
enables the use of more detailed steps for devolatilisation and the use of
more realistic char combustion processes. In the present work the devolatil
isation rates were calculated using the coal devolatilisation model FG-DVC.
In this way devolatilisation rates and the yields of char and volatile wer
e obtained. A drop tube reactor was operated at 1623 K to collect char samp
les, from Thoresby coal, at different sampling positions or residence times
, and proximate and ultimate analysis were conducted on these char samples
to confirm the results. The detailed char combustion sub-models being devel
oped for CFD codes require char properties such as densities, surface areas
and pore size distributions but a simplified model was used here. In this
case the use of a simple global char oxidation model together with an empir
ical derived 'volatile' and FG-DVC predicted devolatilisation rate data see
m to give good agreement with the experimental results available for the ch
ar burnout. However, there still remains considerable uncertainty in the us
e of char burnout models including the one used here is not sufficiently ac
curate in predicting carbon burnout in all conditions. (C) 1999 Elsevier Sc
ience Ltd. All rights reserved.