Se-catalyzed disproportionation of bisulfite (HSO 3 −) is a facile and potential wet flue gas desulfurization. In this paper, the kinetics and mechanism of Se-catalyzed disproportionation of HSO 3− were systematically investigated. The Se-catalyzed disproportionation of HSO 3 − is found to be pseudo-first-order with respect to the HSO 3 − and Se concentrations, and is zeroth-order with respect to the initial pH value. More importantly, the kinetics of Se-catalyzed disproportionation of HSO 3− can be divided into two stages, i.e., a rate-controlling stage and an acceleration stage. In the rate-controlling stage, the reaction rate is slow and the intermediate HSeSO 3− forms. This intermediate is decisive to accelerate the HSO 3 − disproportionation, and thus, it plays an important role in the Se-catalyzed process. Furthermore, a kinetic equation is determined according to the results:94 [Se] 1.13 , where k 1 = (10.88 ± 0.04) × 10 −2 M −1.07 •min −1 . This kinetics prediction model is fitted well with the experimental data, indicating that this model can satisfactorily describe the experimental kinetic data of Se-catalyzed disproportionation of HSO 3 − .