Binary Cu-Cr-O and Cu-Ce-O oxides were studied in thiswork as regenerable sorbents forhigh-temperature fuel gas desulfurization.CuO-Cr
2O
3 and CuO-CeO
2sorbents can removeH
2S from simulated coal-derived fuel gas to less than5-10 ppmv in the temperature range of650-850
C. The presence of stableCuCr
2O
4 in CuO-Cr
2O
3so
lids retains some copper in theCu
2+ or Cu
1+ oxidation state, which canaccount for the high H
2S removal efficiency. InCuO-CeO
2 sorbents, however, CuO is easily reduced to coppermetal. Participation of reduced ceriumoxide in sulfidation can explain the observed high desulfurizationefficiency. TGA tests andXRD analysis indicate that sulfidation proceeds through partial initialreduction of the CuO-Cr
2O
3 sorbents: CuO
Cu/Cu
2O
Cu
xS (
x < 2). Reductionkinetics were studied in the TGAover temperature ranges of 550-850 and 350-850
C, respectively,for the CuO-Cr
2O
3 andCuO-CeO
2 materials. The sulfidation kineticparameters were measured in the temperaturerange of 450-850
C after prereduction of both sorbents. Thesulfidation of metal copper inCr
2O
3 and CeO
2-xmatrices is a fast reaction with low activation energy, 19.8 and 16.6kJ/mol,respectively. Both types of sorbents can be fully regenerated withdiluted air. The regenerationtemperature affects the reaction pathway and the regenerabi
lity of theso
lid composition.