Alkaline treatment using sodium hydroxide was introduced to obtain a hierarchical pore structure in H-ZSM-5 zeolite.Fe-exchanged zeolite catalysts were prepared by impregnation on the original and alkali-treated zeolites,and were evaluated for NOx reduction by NH3,NO oxidation,and NH3 oxidation reactions.The highly dispersed iron species as active sites can be obtained by controlling the pore structure and particle size of zeolite.Therefore,the Fe/ZSM-5 catalyst treated mildly by sodium hydroxide before iron exchange,which contains amounts of highly dispersed Fe species,obtains over80% NOx conversion at a wide temperature range of 250-500℃. Alkaline treatment using sodium hydroxide was introduced to obtain a hierarchical pore structure in H-ZSM-5 zeolite. Fe-exchanged zeolite catalysts were prepared by impregnation on the original and alkali-treated zeolites, and were evaluated as NOx reduction by NH3, NO oxidation , and NH3 oxidation reactions. The highly dispersed iron species as active sites can be obtained by controlling the pore structure and particle size of zeolite. Therefore, the Fe / ZSM-5 catalyst treated mildly by sodium hydroxide before iron exchange, which contains amounts of highly dispersed Fe species, obtain over 80% NOx conversion at a wide temperature range of 250-500 ° C.