The effects of the presence of CO2, O-2, and NOx in the flue gas on the kinetics of the sulfation of blast furnace slag/hydrated lime sorbents at low temperatures were studied using a differential fixed-bed reactor. When O-2 and NOx were not present simultaneously, the reaction kinetics was about the same as that under the gas mixtures containing SO2, H2O, and N-2 only, being affected mainly by the relative humidity. The sulfation of sorbents can be described by the surf-ace coverage model and the model equations derived for the latter case. When both O-2 and NOx, were present, the sulfation of sorbents was greatly enhanced, forming a great amount Of Sulfate in addition to sulfite. The surface coverage model is still valid in this case, but the model equations obtained show a more marked effect of relative humidity and negligible effects of SO2 concentration and temperature on the reaction. The effect of sorbent composition on the reaction kinetics was entirely represented by the effects of the initial specific Surface area (S-g0) and the Ca molar content (M-1) of sorbent. The initial conversion rate of sorbent increased linearly with increasing S-g0, and the ultimate conversion increased linearly with increasing Sg0M-1. The model equations obtained in this work are applicable to describe the kinetics of the sulfation of the sorbents in the low-temperature dry and semidry fine gas desulfurization processes either with an upstream NOx, removal unit or without.