The effects of operating conditions linear gas velocity, Ca/S molar ra
tio, type of coal and limestone, etc.) on sulfur retention efficiency
in a circulating fluidized bed combustor were studied. The operating c
onditions affect the sulfur retention differently. To explain this, a
mathematical model was developed. To determine axial voidage profiles,
the model uses a modified exponential decay hydrodynamic model, which
divides the bed into a dense region at the bottom of the bed and a di
lute region above. In the dilute region a core-annulus structure with
solid dispersion from core to annulus is considered. The SO2 retention
rate is considered to depend on the bed height through the SO2 profil
es generated by the coal devolatilization and char combustion rates, w
hich change with the bed height. The model gives good predictions of t
he effect of the operating variables on sulfur retention in a CFB pilo
t plant of 20 cm i.d. and 6.5 m height, burning two different lignites
and an anthracite with four types of Limestone.