A transient kinetic model has been developed for the simultaneous adsorption of SO 2 -NO x on Na/γ-Al 2 O 3 sorbent, using step response experimental data from a fixed-bed microreactor. The reactor temperature ranges from 367 to 407 K, and the molar SO 2/ NO ratio from 2 to 8 with and without NO 2 . SO 2 and NO 2 readily adsorb on the sorbent surface, producing SO 2 * and NO 2 * species. However, NO and O 2 only adsorb simultaneously and in the presence of sufficient SO 2 * on the surface. The proposed mechanism consists of chemisorption steps for SO 2 and NO 2 , whereas NO and O 2 are adsorbed simultaneously via an Eley-Rideal step involving a surface species derived from SO 2 *. The latter is followed by several consecutive steps involving more SO 2 * species as well as O 2 , leading to the formation of a complex with a stoichiometry of SO 2 / O 2 /NO of 10/5.5/1. The enhanced SO 2 sorption capacity in the presence of NO 2 is described adequately by considering that the adsorbed NO 2 * opens a new reaction path for SO 2 adsorption. Both the Langmuir ideal surface and the Elovich nonuniform surface kinetics were considered for the steps involving free sites. The latter were found to simulate the experimental data more closely, indicating that the interaction among various species and intrinsic surface nonuniformity are important.