Khudoyor Rаhmatov¹ , Normurot Fayzullaev² , Firdavsiy Buronov¹ , Shavkat Matmuratov³ , Yuldash Takhirov³ , Mohamed Rifky⁴ , Kasun Dissanayake¹ and Murodjon Samadiy¹

¹Karshi Engineering-Economics Institute, Qarshi, 180100, Uzbekistan

²Samarkand State University, Samarkand, 140100, Uzbekistan

³Urgench State University, Urgench, 220100, Uzbekistan

⁴Eastern University, Sri Lanka, Chenkalady, 30350, Sri Lanka

Abstract

In this article, methods of preparation of catalysts in analogues of in high-silica zeolite, conversion of n-hexane in the catalysts keeping in high-silica zeolite, of n-hexane to aromatic hydrocarbons, n-hexane to aromatic hydrocarbons in catalysts with high catalytic activity and selectivity modified with copper, 2%Cu*8%Zn/Н-High silica zeolite-40 conversion of n-hexane to aromatic hydrocarbons in the composition catalyst, activity in chain branching and aromatization processes to obtain high-octane components of fuels 2%Cu*8%Zn/Н- High silica zeolite-40 high silicon, A mesoporous aluminosilicate catalyst with high catalytic activity and selectivity was studied for the catalytic Aromatization of nhexane to aromatic hydrocarbons. H-High silica zeolite-40 and 2%Cu*8 %Zn/H-High silica zeolite-40 catalysts with high catalytic activity and selectivity selected for catalytic Aromatization of n-hexane to aromatic hydrocarbons, Aromatization, chain branching and carbon-carbon by hydrogen action activity in the process of breaking the bond was studied.