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

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PP-IV-24From <strong>the</strong> data displayed in Fig. 2, one can see that <strong>the</strong> composition <strong>of</strong> <strong>the</strong> zeoliteframework and <strong>the</strong> gallium concentration in <strong>the</strong> catalyst significantly affected <strong>the</strong> yield <strong>of</strong>liquid products. The galloaluminosilicate with M = 60 had <strong>the</strong> highest catalytic activity innatural gas conversion. The aromatic hydrocarbon yield at 600 °C and 1000 h –1 reached18.7% with a conversion <strong>of</strong> 26.0%.Conversion, Ar-C yield, %3025201510500 550 600 650Temperature, о С4536121086420Product yield, %Conversion, yield, %3025201510501,2%Ga/M=30Conversion1,2%Ga/M=401,2% Ga/M=601,2% Ga/M=802,2% Ga/M=30Yield2,2% Ga/M=402,2% Ga/M=602,2% Ga/M=80Fig. 1. (1) Conversion <strong>of</strong> natural gas on 2.2% Ga-AS(M = 60) and (2-6) yield <strong>of</strong> (2) benzene, (3) toluene, (4)naphthalene, (5) Ar-C 11-12 , and (6) Ar-C 6+ versusprocess temperature (W = 1000 h –1 ).Fig. 2. Natural gas conversion and aromatichydrocarbon yield over galloaluminosilicates withdifferent silica ratios and different gallium oxideconcentrations (T = 600 °C, W = 1000 h –1 ).This evolution <strong>of</strong> <strong>the</strong> catalytic properties <strong>of</strong> galloaluminosilicates during natural gasconversion is due to <strong>the</strong> fact that <strong>the</strong> aluminum concentration decreases with increasing silicaratio, thus increasing <strong>the</strong> ratio between <strong>the</strong> Lewis and BrØnsted acid sites on <strong>the</strong> catalyst. Inaddition, gallium doping generates new strong aprotic acid sites in <strong>the</strong> zeolite, while <strong>the</strong>density <strong>of</strong> protic acid sites, which are associated with lattice aluminum, decreases.Thus, galloaluminosilicates have a high catalytic activity in natural gas conversion toaromatic hydrocarbons. The most active catalysts have <strong>the</strong> silica ratio equal to 30 or 60 andcontain 1.2 or 2.2 wt % gallium oxide, respectively. These catalytic systems make it possibleto carry out <strong>the</strong> chemical conversion <strong>of</strong> gaseous hydrocarbons to liquid products in one stage;thus, <strong>the</strong> in addition make it possible to produce valuable organic compounds from alternativesources for use in petrochemical and chemical industries.References1. Kuznetsov B.N. Motor fuels from alternative sources // Sorovsk. Obrazovat. Zh. 2000. Vol. 6. № 4. P. 51.2. Rozovskii A.Ya. Syn<strong>the</strong>sis <strong>of</strong> motor fuels from natural gas // Khim. Prom-st. 2000. № 3. P. 3.439

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