Drying of solid fuel particles in hot gases (50-200 degrees C) is stud
ied both theoretically and experimentally. The measurements are carrie
d out by using a thermobalance reactor constructed for drying and pyro
lysis studies of particles up to 30 mm by diameter. The model is based
on the solution of the conservation equations for mass and energy. Th
e drying is considered to consist of three successive periods: a short
initial heating period, period of constant rate of drying and period
of falling rate of drying. It is assumed that the particle moisture di
stribution is uniform during the constant rate of drying. Shrinking co
re model is assumed for the falling rate period. Besides fuel particle
s, the model is applicable also for other solid particle drying proces
ses. Model calculations are compared to measurements for wood chips. T
he model can predict the effect of the main parameters reasonably well
. These main parameters affecting the drying rate are: particle size,
particle shape, initial particle moisture content, gas temperature and
gas moisture content, temperature of the reactor walls and slip veloc
ity. The irregular shape of practical fuel particles can approximately
be simulated as one-dimensional case (plate, cylinder, sphere) by usi
ng an equivalent volume to surface area ratio.