Transformation of n-hexane over Al 2 O 3 and SiO 2 supported Pt, Pt+Ga and Ir+Pt+Ga catalysts was studied in a continuous-flow reactor operated under slugpulse mode at 520°C. Bimetallic catalysts were prepared by introducing first Ga(OEt) 3 and then diallylplatinum as precursor compounds. Iridium was then introduced via decomposition of Ir 4 (CO) 12 adsorbed onto Pt+Ga catalysts. The addition of Ga to Pt/SiO 2 catalyst decreased hydrogenation, aromatization and hydrogenolysis selectivity. Over Pt/Al 2 O 3 catalyst Ga increased hydrogenolysis selectivity and decreased isomerization and C 5 -cyclization. The main effect of Ir was to increase hydrogenolysis selectivity and the stability of catalysts.