A large-scale apparatus has been used to evaluate the effect of partic
le size on the spontaneous heating of a coal stockpile. To accomplish
this, coal with various ranges of particle size (between 2 and 50 mm i
n diameter) was oxidized in a cylinder of 3-m length and 0.3-m diamete
r. A critical range of particle size was observed, below which spontan
eous heating leads to flaming combustion. From the results of the oxyg
en consumption and the temperature of the coal bed, the influence of p
article size on the oxidation rate has been analyzed in greater depth.
The oxygen conservation equation, in which the oxygen consumption rat
e is first order in oxygen concentration and obeys the Arrhenius equat
ion, allows the determination of apparent activation energies and pree
xponential factors. Calculated values of these parameters, by fitting
the experimental data to the integrated form of the oxygen conservatio
n equation, have been used to evaluate the effect of particle size. It
was of particular interest to determine the operating regime for coal
-oxygen reaction and this was achieved by defining an empirical expone
nt for the particle diameter in the rate equation. This exponent indic
ated the oxidation regime for a change from chemical to pore diffusion
control at successively higher temperatures.