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Gasoline fraction obtained on cobalt catalyst by FT-synthesis has insufficiently high octane number due to low content of olefins and isoparaffins. It necessary to conduct second stage of hydrotreatment of this gasoline fraction for production of marketable gasoline. Aim of present work consists of investigation of influence of FT-conditions on characteristics of fuel. At the second part of the work influence of type and content of zeolite in composition of Pt-catalysts on isomerization and cracking activity of catalysts in reaction of isomerization of n-hexane and gasoline fraction in conditions of industrial process are investigated.