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method of preparing CATALYST FOR COMPLETE OXIDATION OF HYDROCARBON, the catalyst prepared by this method AIR CLEANING METHOD AND FROM HYDROCARBON USING CATALYST OBTAINED
method of preparing CATALYST FOR COMPLETE OXIDATION OF HYDROCARBON, the catalyst prepared by this method AIR CLEANING METHOD AND FROM HYDROCARBON USING CATALYST OBTAINED
1. A process for the preparation of complete oxidation of hydrocarbons, particularly hydrocarbon impurities in the air of a catalyst to air purification, comprising applying the platinum or palladium on zirconium oxide volframatsoderzhaschy calcined carrier by impregnation with a water solution of a platinum or palladium compound, followed by calcination in air at a temperature of 300-500 ° C and reducing in a hydrogen stream at 300-500 ° C, characterized in that the carrier further volframatsoderzhaschy zirconium oxide modified with gallium ions by their n aneseniya of galliya.2 nitrate aqueous solution. A method according to claim 1, characterized in that the gallium is applied to a zirconium oxide carrier volframatsoderzhaschy platinoy.3 simultaneously. A method according to claim 1, characterized in that the gallium is applied to the carrier volframatsoderzhaschy zirconium oxide prior to the application of platinum, followed by further thermal treatment at a temperature of 300-500 ° C.4. A method according to claim 1, characterized in that as a zirconium oxide carrier is used tsirkoniya.5 hydroxide. A method according to claim 1, characterized in that as a zirconium oxide carrier is used tsirkoniya.6 oxide. A catalyst for complete oxidation of hydrocarbons, including for air purification from impurities hydrocarbons prepared by p.1.7. The catalyst according to claim 6, characterized in that it contains from 0.5 to 5 wt.% Platinum or palladiya.8. The catalyst according to claim 6, characterized in that it contains 1 to 5 wt.% Galliya.9. A method of purifying air from hydrocarbons by their complete oxidation in the presence of a catalyst, characterized in that a catalyst prepared according to claims 1-5 or a catalyst according pp.6-9 and the process is carried out in Fr.
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