Flue gas S0O(2) removal at 200 degrees C over Mo and Co doped V2O5/AC catalyst-so rben ts and regeneration of the used catalyst-sorbents in H-2 at 380 degrees C in the same reactor are studied in this paper. Compared with V2O5/AC, the catalyst-sorbents containing Co show higher SO2 uptake while the one containing Mo shows a slightly lower SO2 uptake. Elemental sulfur is produced during H-2-regeneration of the used catalyst-sorbents when effluent gas of the regeneration is recycled back to the reactor. H-2-regeneration of the used V2O5/AC produces little elemental sulfur, but the Mo and Co doped ones show high elemental sulfur yields with an elemental sulfur selectivity of 50% for a catalyst-sorbent containing 2% V2O5, 0.5% MoO3 and 0.5% CoO, V2Mo0.5 Co0.5/AC. Molybdenum and cobalt sulfides are likely formed in the regeneration, which catalyze the elemental sulfur formation but reduce the SO2 uptake of the catalyst-sorbents in the subsequent SO2 removal stage. (C) 2007 Elsevier Ltd. All rights reserved.