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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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PP-IV-22INFLUENCE OF COMPOSITION OF THE SECONDARY CARRIER ONTHE BASE OF TRANSITION METALS SUPPORTED ON A BLOCKMETAL SCELETON IN REACTION OF OXIDATION OF METHANEK. Dossumov, Sh.A. GilmundinovD.V. Sokolsky <strong>Institute</strong> <strong>of</strong> Organic <strong>Catalysis</strong> and Electrochemistry, 142, D.Kunaev str.,Almaty, 050010, Kazakhstan. Fax: +7(727)2915722, E-mail: tungatarova58@mail.ruNow natural gas basically is used in <strong>the</strong> power and household purposes. A level <strong>of</strong> chemicalprocessing <strong>of</strong> natural gas into industrial useful products is very low. Numerous researches onprocessing <strong>of</strong> natural gas represent scientific and practical interest as allow receiving valuablechemical compounds. Despite <strong>of</strong> huge opportunities in conversion <strong>of</strong> methane researchers andmanufacturers show interest to <strong>the</strong> following processes: direct catalytic oxidation <strong>of</strong> methaneinto oxygen-containing products such as formaldehyde, methanol, acetic acid, formic acid,syn<strong>the</strong>sis gas, catalytic dimerization <strong>of</strong> methane to ethylene.Syn<strong>the</strong>sis gas is initial raw material for production <strong>of</strong> many chemical and petrochemicalproducts. It is used in metallurgy for reduction <strong>of</strong> metals. Natural gas is <strong>the</strong> main raw materialfor production <strong>of</strong> syn<strong>the</strong>sis gas. Steam conversion <strong>of</strong> natural gas is carried out at hightemperature (900 °C). It is power consuming process. Steam conversion <strong>of</strong> natural gas is <strong>the</strong>main method for obtaining <strong>of</strong> syn<strong>the</strong>sis gas. It is more advisable production <strong>of</strong> syn<strong>the</strong>sis gasby direct oxidation <strong>of</strong> methane by oxygen <strong>of</strong> air at 500-700 °C and atmospheric pressure.We carried out investigation on influence <strong>of</strong> <strong>the</strong> composition <strong>of</strong> secondary carrier onpartial oxidation <strong>of</strong> methane by oxygen <strong>of</strong> air on such carriers as Cr 2 O 3 , NiO 2 , V 2 O 5 , Al 2 O 3 ,W 2 O 3 . Copper and nickel oxides were used as active components <strong>of</strong> catalysts. Preparationmethod <strong>of</strong> catalyst includes <strong>the</strong> following sages: supporting <strong>of</strong> secondary carrier on a metalskeleton block, calcination <strong>of</strong> carrier, impregnation <strong>of</strong> a surface <strong>of</strong> secondary carrier by <strong>the</strong>salts <strong>of</strong> nickel and copper with subsequent drying and calcination <strong>of</strong> catalysts. Theinvestigations were carried out at 500-700°C and space velocity 2000h –1 . Reaction productswere determined by chromatographically on fluoroplastic column filled by Polysorb-1processed by apiezone.It was detected <strong>the</strong> influence <strong>of</strong> <strong>the</strong> composition <strong>of</strong> secondary carrier on direction <strong>of</strong>catalytic reaction. Such formaldehyde, methanol, and water were formed on <strong>the</strong> alumina,vanadium and tungsten oxides. Catalytic surface is covered by carbon and activity <strong>of</strong> catalystis sharply decreased after short time. Carbon acids were determined on <strong>the</strong> catalysts withsecondary carrier on <strong>the</strong> base <strong>of</strong> titanium oxide at 600 °C with 100% selectivity. Carbon wasnot found on <strong>the</strong> surface <strong>of</strong> catalyst during long time exploitation due to influence <strong>of</strong> <strong>the</strong>composition <strong>of</strong> secondary carrier.The work was supported by ISTC grant K-1266.436

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