文摘
Se-catalyzed disproportionation of bisulfite (HSO3–) is a facile and potential wet flue gas desulfurization. In this paper, the kinetics and mechanism of Se-catalyzed disproportionation of HSO3– were systematically investigated. The Se-catalyzed disproportionation of HSO3– is found to be pseudo-first-order with respect to the HSO3– and Se concentrations, and is zeroth-order with respect to the initial pH value. More importantly, the kinetics of Se-catalyzed disproportionation of HSO3– 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 HSeSO3– forms. This intermediate is decisive to accelerate the HSO3– disproportionation, and thus, it plays an important role in the Se-catalyzed process. Furthermore, a kinetic equation is determined according to the results: r0 = k1[HSO3–]0.94[Se]1.13, where k1 = (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 HSO3–.