Wet limestone scrubbing is the most common flue gas desulfurization pr
ocess, and in this process sulfite oxidation plays a major role determ
ining the dewatering properties of the sludge produced and leading to
the production of gypsum of high quality. A literature analysis showed
that the results obtained for sulfite oxidation under homogeneous con
ditions are relatively easily interpreted, while the results relative
to heterogeneous reaction conditions (i.e. conditions in which gaseous
oxygen and a sulfurous solution are brought in contact) are much more
difficult to interpret, owing to the interaction between mass transfe
r and chemical reaction, In this work a model is proposed to describe
the interaction between oxygen absorption and the oxidation reaction u
nder heterogeneous conditions, which takes into account the peculiar c
haracteristics of absorption with zero order reaction, A kinetic equat
ion of order zero in dissolved O-2,3/2 in HSO3- and 3/2 in the catalys
t concentration was used to match experimental results presented in th
e literature and model results, Integration of the model equations led
to evaluation of the oxygen absorption rate as a function of the cata
lyst concentration together with the concentration profiles in the liq
uid film for the different species. (C) 1997 Elsevier Science S.A.