catalytic compositions for u0432u044bu0441u043eu043au043eu0441u0435u043bu0435u043au0442u0438u0432u043du043eu0433u043e u0433u0438u0434u0440u043eu0434u0435u0430u043bu043au0438u043bu0438u0440u043eu0432u0430u043du0438u044f u0430u043bu043au0438u043bu0430u0440u043eu043cu0430u0442u0438u0447u0435u0441u043au0438u0445 hydrocarbons

摘要

method of u0433u0438u0434u0440u043eu0434u0435u0430u043bu043au0438u043bu0438u0440u043eu0432u0430u043du0438u044f exclusively hydrocarbon mixtures consisting of c - Cu0430u043bu043au0438u043bu0430u0440u043eu043cu0430u0442u0438u0447u0435u0441u043au0438u0435 compounds mixed with c - Cu0430u043bu0438u0444u0430u0442u0438u0447u0435u0441u043au0438u043cu0438 and qi u043au043bu043eu0430u043bu0438u0444u0430u0442u0438u0447u0435u0441u043au0438u043cu0438 productsin the conditions of the reaction were u0430u0440u043eu043cu0430u0442u0438u0437u0430u0446u0438u044e and subsequent u0433u0438u0434u0440u043eu0434u0435u0430u043bu043au0438u043bu0438u0440u043eu0432u0430u043du0438u0435 consisting of continuous processing of the hydrocarbon are the presence of hydrogenwith the use of a catalyst consisting of a u0446u0435u043eu043bu0438u0442u0430 zsm - 5, as such or in the form of a si / al mole ratio in the zsm - 5 from 5 to 100.and modified by a combination of platinum and molybdenum, at a temperature of from 400 to 650u00b0u0441, at a pressure of from 2 to 4 mpa and the molar against mr. / raw materials from 3 to 6.the presence of raw material of organic compounds containing u0433u0435u0442u0435u0440u043eu0430u0442u043eu043cu044b, such as sulfur, nitrogen or oxygen, doesn't change the efficiency of catalyst the proposed method.