Despite the large body of excellent work that has been done on the qua
ntitative description of char combustion, our ability to specify the c
onditions to be met in order to maintain the carbon loss from pulveriz
ed coal-fired boilers below a desired value is still limited. The prob
lems arise, in part, from the large number of fuel, combustion, and eq
uipment characteristics that may influence carbon burnout. Measurement
s of the concentration and size distribution of carbon in fly ash from
a 30 MW (electric) utility boiler have been used to test assumptions
regarding the factors controlling carbon conversion. The principal exp
lanation for unexpectedly high carbon lasses under the conditions inve
stigated was air leakage into the furnace and convection sections, whi
ch caused the furnace gas to be richer than expected from the flue gas
analysis. Assuming that the inleaking air made no contribution to com
bustion, a calculation of carbon burnout, using the mean char combusti
on rate of Hurt and Mitchell [Twenty-Fourth Symposium (International)
on Combustion, 1992, pp 1243-1250] and the char reactivity distributio
n of Hurt, Lunden, Brehob, and Maloney [Twenty-Sixth Symposium (intern
ational) on. Combustion, 1996, pp 3169-3177], reproduced the carbon lo
ss and size distribution of unburned particles and was within a factor
of 2 of the Babcock & Wilcox correlation of carbon loss with stoichio
metric ratio [Steam/Its Generation and Use, 37th ed., 1963, p 17-21].
According to the calculations, the distribution of char reactivities h
as a significant influence on the carbon loss and abundance of small p
articles in the unburned carbon size distribution.