Fly ash consists of various metal oxides which can remove SO2 gas by the catalyst effect. When fly ash is added in the preparation process of pitch-based activated carbon, the pitch particles aggregate and fly ash is embedded in the activated carbon. To increase SO2 gas removal performance, activated carbon was prepared by surface-treated fly ash and petroleum-based pitch. Carboxyl groups were introduced into the fly ash by malic acid treatment. The introduced carboxyl groups acted as an activation agent to create micropore around the fly ash, and created micropores were exposed to the fly ash outside of the activated carbon. The exposed fly ash increased removal amount of SO2 gas by a catalytic effect of the metal oxides. The SO2 gas removal performance improved by 34% because of the catalyst effect of the exposed fly ash and improvement in the micropore structure in the activated carbon.

A membrane contactor technique is proposed to selectively remove the SO2 gas from the ship exhaust gas. Membrane contactor system operates with two independent streams of liquid and gaseous phase, with a large contact area between the streams, resulting in high mass transfer coefficient values. In this study, hydrophobic polypropylene substrate was used to greatly minimize the wetting of the membranes. The performance of three absorbents -distilled water, NaOH, and Na2SO3 aqueous solution- was investigated in terms of SO2 removal efficiency within a specific range of different parameters (gas flow rate, absorbent molarities, liquid flow rate, L/G ratio). Finally, optimum operating parameters for a high SO2 removal efficiency were suggested; and the overall mass transfer coefficient and HTU values were examined.

To remove SO2 from flue gas, a thin film nanocomposite (TFN) hollow fiber membrane was decorated with Nafion/TiO2 nanoparticles. Morphological and structural analyses of the TFN membranes were performed using FTIR, SEM, EDX, TEM, and AFM. The gas permeation experiments were performed with pure gases and a mixed gas within a pressure range of 1-3 bar and feed gas flow rate of 0.03-0.15 L/min. The obtained experimental results suggest that the addition of Nf/TiO2 nanoparticles improved the membrane performance by introducing sulfonate and hydroxyl functional groups to the membrane, and thus increased SO2 permeability and selectivity. The SO2 permeability was found to be 411-1671 GPU, while the ideal selectivities achieved for SO2/N2 and SO2/CO2 were 2928 and 72, respectively. Overall, an SO2 removal efficiency of 93% was achieved by using the Nf/TiO2 incorporated TFN membrane.