The removal of low concentrations of hydrogen sulfide (H 2 S) from hydrogen-rich gaseous fuels by selective catalytic oxidation, using activated carbon as the catalyst, was studied. The capacities of four activated carbons for reducing the H 2 S concentration down to the parts per billion (ppb) level were determined to be strongly related to their microstructures and impurities, even though their activity and selectivity were strongly dependent on the test conditions, such as reaction temperature, O 2:H 2 S ratio, space velocity, and length-to-diameter (L/D) ratio of the catalyst bed. Because the side reactions that form COS and SO 2 are sometimes unavoidable under real fuel processing conditions, the complete and exclusive conversion of H 2 S to elemental sulfur (S) requires that activated carbon has catalytic activities not only for the oxidation of H 2 S, but also for the oxidation of COS and the reaction between H 2 S and SO 2 . Because one of the activated carbons (sample W-22) had such catalytic functions and a relatively large capacity of trapping sulfur in its micropores, this carbon showed a combination of excellent activity and selectivity on removing H 2 S from both hydrogen and simulated reformate streams at a reaction temperature of ∼150 °C.
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Wu et al. (2005) studied this question.
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