One technological process employing ozone and heterogeneous catalyst-sorbents was proposed for removal of SO 2 from flue gas. The catalyst-sorbents were developed and tested especially for adsorption and oxidation of SO 2 . Alternative catalyst-supporters including γ -Al 2 O 3 , permutite, silica gel, activated carbon and diatomite combined with different metal oxides (MnO 2 , Cr 2 O 3 , Fe 2 O 3 , CuO, CoO and NiO) were evaluated and tested. It was found that γ -Al 2 O 3 doped with MnO 2 can be considered as removal-effective sorbent for adsorption and oxidation of SO 2 . The synergetic effect between ozone and catalyst was found to be dominated. Effects of catalyst preparation parameters like calcination temperature, metal loaded and reaction temperature, etc. were investigated based on the MnO 2 /Al 2 O 3 catalyst-sorbents. Results show that γ -Al 2 O 3 combined with 8% Mn, calcinated under 573 K and reacted at 413 K are the optimal parameters for removal of SO 2 . Extra NO in flue gas can slightly enhance the capture efficiency of SO 2 .