H2S sorption by 18-35 mesh particles (average mass radius of 0.40 mm) of three different calcium-based sorbents (limestone, CaC03; dolomitic limestone, dolomite, MgC03-CaC03) was tested under simulated coal gas in a differential tube reactor.Two fundamentally different behaviors were observed. Above the calcination temperature of CaC03, complete conversion of CaC03 to C a s can be achieved with all three sorbents; the reaction rate increases as the magnesium-to-calcium ratio increases in the sorbent and the reaction rate is controlled by the diffusion of H2S through the Cas product layer and by the kinetics of the calcination of CaC03 to CaO. However, below the calcination temperature of CaC03 (about 900 "C under 1 bar of C o d , less than 20% of the CaC03 in limestone can be converted to C a s compared t o 100% in dolomite. For the dolomitic limestone, all the calcium atoms associated with the dolomite regions can be converted to C a s whereas only 20% of those associated with the limestone regions can be converted. Above 710 "C, the sulfidation rate of dolomite and dolomitic limestone is controlled by the diffusion of H2S through the product layer. Below 710 "C, the kinetics of calcination of MgC03 as well as the rate of the chemical reaction between CaC03 and H2S become the limiting steps in the overall reaction kinetics.