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Aromatization patterns of hexane in high silicon zeolite

Khudoyor RahmatovKarshi Engineering-Economics Institute, Qarshi, 180100, UzbekistanNormurot FayzullaevSamarkand State University, Samarkand, 140100, UzbekistanFirdavsiy BuronovKarshi State Technical UniversityShavkat MatmuratovUrgench State University, Urgench, 220100, UzbekistanYuldash TakhirovUrgench State University, Urgench, 220100, UzbekistanMohamed RifkyEastern University, Sri Lanka, Chenkalady, 30350, Sri LankaKasun DissanayakeKarshi State Technical UniversityMurodjon SamadiyKarshi Engineering-Economics Institute, Qarshi, 180100, Uzbekistan
E3S Web of Conferencesjournal2024en
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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 n-hexane 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.

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