FIELD: chemical industry.
SUBSTANCE: inventions relate to the conversion of synthesis gas. A catalyst for the direct conversion of synthesis gas to produce liquid fuel is described, which contains a component Ⅰ and a component Ⅱ; these components Ⅰ and component Ⅱ are combined with each other by mechanical mixing; the active component of component Ⅰ is metal oxide, and component II is a molecular sieve with one-dimensional channels formed by ten-membered rings; the specified metal oxide is one, two or more of MnOx, MnCryO(x+1,5y), MnAlyO(x+1,5y), MnZryO(x+2y), MnInyO(x+1,5y), ZnO, ZnCryO(1+1,5y), ZnAlyO(1+1,5y), ZnGayO(1+1,5y), ZnInyO(2+1,5y), CeO2, CoAlyO(1+1,5y), FeAlyO(1+1,5y), Ga2O3, Bi2O3, In2O3, InyAlzMnO(x+1,5y+1,5z), InyGazMnO(x+1,5y+1,5z); the range of values of the specified x is 1-3.5; the range of values of y is 0.1-10; the range of values of z is 0.1-10; the specific surface area of the specified MnOx, ZnO, CeO2, Ga2O3, Bi2O3, In2O3 is 1-100 m2/g; the specific surface area of the specified MnCryO(x+1,5y), MnAlyO(x+1,5y), MnZryO(x+2y), MnInyO(x+1,5y), ZnCryO(1+1,5y), ZnAlyO(1+1,5y), ZnGayO(1+1,5y), ZnInyO(2+1,5y), CoAlyO(1+1,5y), FeAlyO(1+1,5y), InyAlzMnO(x+1,5y+1,5z), InyGazMnO(x+1,5y+1,5z) is 5-150 m2/g; in this case, the specified molecular sieve is a molecular sieve with a topological structure of TON, AEL, MTT or MRE, and is one of SAPO-11, ZSM-23 or ZSM-48. A method for direct conversion of synthesis gas to obtain liquid fuel is described, in which a conversion reaction is carried out with synthesis gas as a raw material for the reaction under conditions of a stationary layer or a mobile layer, while the above-mentioned catalyst is used.
EFFECT: production of liquid fuel with a reduced content of aromatic compounds.
21 cl, 7 tbl, 2 ex
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Authors
Dates
2022-05-19—Published
2019-12-10—Filed