Wet limestone scrubbing is the most common flue gas desulfurization pr
ocess for control of sulfur dioxide emissions from combustion of fossi
l fuels. Forced oxidation in the scrubber loop improves the dewatering
properties of the sludge, leading to the formation of gypsum (Ca50 .
2H(2)O). A literature analysis revealed that uncertainties on the mech
anisms of the oxidation reaction and on the values of the kinetic para
meters still remain. In the present work the oxidation rate was experi
mentally studied by contacting pure oxygen or mixtures of oxygen and n
itrogen with a calcium bisulfite solution. The experiments were carrie
d out in a well-mixed bubbling reactor varying temperature, oxygen par
tial pressure and sulfite concentration, in the absence of solid calci
um sulfite and of catalytic species. It was shown that the rate of the
process is controlled by reaction kinetics, and that the reaction rat
e is zero order in dissolved oxygen and 3/2-order in bisulfite ion. Co
pyright (C) 1996 Elsevier Science Ltd