CATALYTIC HIGHLY SELECTIVE METHOD FOR PRODUCING OLEFINS WITH A LOW NUMBER OF CARBON ATOMS APPLYING A HETEROATOM-ALLOYED MOLECULAR SIEVE AND SYNTHESIS GAS Russian patent published in 2022 - IPC B01J29/84 B01J29/85 B01J23/06 B01J23/34 B01J23/26 B01J23/08 B01J23/74 B01J23/10 B01J23/18 B01J21/06 C07C1/04 C07C11/02 

Abstract RU 2778293 C1

FIELD: catalysts.

SUBSTANCE: invention relates to a catalyst for producing C2-4 olefins from synthesis gas and to a method for producing C2-4 olefins applying synthesis gas as a raw material for the reaction in conditions of a fixed layer or a mobile layer in the presence of said catalyst. The catalyst contains component I and component II; the active component of said component I constitutes a metal oxide, and component II constitutes a heteroatom-alloyed molecular sieve. Said metal oxide constitutes one, two, or more of MnOx, MnaCr(1-a)Ox, MnaAl(1-a)Ox, MnaZr(1-a)Ox, MnaIn(1-a)Ox, ZnOx, ZnaCr(1-a)Ox, ZnaAl(1-a)Ox, ZnaGa(1-a)Ox, ZnaIn(1-a)Ox, CeOx, CoaAl(1-a)Ox, FeaAl(1-a)Ox, GaOx, BiOx, InOx, InaAlbMn(1-a-b)Ox, InaGabMn(1-a-b) x; the range of values of x herein is 0.7 to 3.7, the range of values of a is 0 to 1; the range of values of a+b is 0 to 1. The specific surface area of MnOx, ZnOx, CeOx, GaOx, BiOx, InOx is 1 to 100 m2/g. The specific surface area of MnaCr(1-a)Ox, MnaAl(1-a)Oх, MnaZr(1-a)Ox, MnaIn(1-а)Oх, ZnOx, ZnaCr(1-a)Ox, ZnaAl(1-a)Ox, ZnaGa(1-a)Ox, ZnaIn(1-a)Ox, CoaAl(1-a)Ox, FeaAl(1-a)Ox, InaAlbMn(1-a-b)Ox, InaGabMn(1-a-b)Ox is 5 to 150 m2/g. The molecular sieve constitutes a molecular sieve with a CHA or AEI topological structure, wherein the framework atoms provide for Al-P-O or Si-Al-P-O; and the heteroatoms constitute one, two, or more of divalent metals Mg, Ca, Cr, Mn, Fe, Co, Ni, Cu, Zn, Sr, Zr, Mo, Cd, Ba, Ce, trivalent Ti, Ga, and tetravalent Ge; said heteroatoms in said heteroatom-alloyed molecular sieve are added to said molecular sieve framework and replace Al, P, or Si in the molecular sieve framework.

EFFECT: effective increase in the activity and selectivity with respect to the product in the course of the reaction of direct conversion of synthesis gas with the production of olefins.

10 cl, 8 tbl, 12 ex

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RU 2 778 293 C1

Authors

Jiao, Feng

Li, Gen

Pan, Xiulian

Bao, Xinhe

Dates

2022-08-17Published

2019-12-10Filed