For
the regenerative flue gas desulfurization method based on basic
aluminum sulfate (BAS), efficiently inhibiting the oxidation of desulfurization
by-products is extremely critical to reuse the absorbents and recover
SO2. In this paper, the macrokinetics of S(IV) antioxidation
procedure was systematically investigated by varying inhibitors, aluminum
content, pH, S(IV) concentration, ethylene glycol (EG) concentration,
temperature, oxygen partial pressure, and air flow in a bubbling reactor
with magnetic stirring. EG was environmentally considered to be an
ideal inhibitor by screening. Furthermore, the S(IV) oxidization speed
inhibited by EG was significantly accelerated when the aluminum content
rose and was correlated to 10–0.6pH with a coefficient
of 0.98. The general oxidization speed of S(IV) was determined to
be 1.1, −2.4, and 0.96 order in oxygen partial pressure, EG
content, and total S(IV) level, respectively. The apparent activity
energy of S(IV) oxidation process was obtained to be 52.0 kJ/mol.
On the basis of a two-step model, kinetic analysis proved that the
general S(IV) oxidation rate in the BAS desulfurization liquid was
decided by the intrinsic oxidation reaction. Meanwhile, the mechanism
of S(IV) oxidation reaction with EG was demonstrated and the products
in reaction solution were detected by gas chromatography–mass
spectrometry. The experimental findings will contribute to industrial
design and procedure optimization related to the BAS regenerative
desulfurization process.