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Core-shell structure multi-level porous cobalt-based Fischer-Tropsch synthesis catalyst and preparation method thereof

A core-shell structure and catalyst technology, which is applied in the field of core-shell structure multi-level channel cobalt-based Fischer-Tropsch synthesis catalyst and its preparation, can solve the problems of reduced conversion rate, low CO conversion rate, and inability to solve the pore size distribution of molecular sieves. Effects of preventing agglomeration, prolonging service life, and strong anti-carbon deposition ability

Active Publication Date: 2018-06-19
WUHAN KAIDI ENG TECH RES INST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the limitation of the micropores of the molecular sieve membrane in this method leads to an extremely low CO conversion rate of only about 40%.
Moreover, neither of the above two methods can solve the problem that the molecular sieve pore size distribution is too concentrated in the micropores, resulting in a decrease in conversion rate.

Method used

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  • Core-shell structure multi-level porous cobalt-based Fischer-Tropsch synthesis catalyst and preparation method thereof

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Embodiment 1

[0040] A core-shell structure multi-stage porous cobalt-based Fischer-Tropsch synthesis catalyst, comprising a catalyst carrier S, a metal active component Co loaded on the catalyst carrier S, and a shell molecular sieve membrane M wrapped on the surface of the catalyst carrier S, wherein, Catalyst support S is SiO 2 , SiO 2 The microstructure is spherical, and the average specific surface area is 210m 2 / g, the particle size range is 20-40 mesh; the shell molecular sieve membrane M is a cluster aggregate with uniform dispersion of H-ZSM-5 nanoparticles, and the average particle size range of H-ZSM-5 nanoparticles is 10-30nm. The pore diameter of its own micropores is less than or equal to 2.0nm, and the gap between adjacent H-ZSM-5 nanoparticles is less than or equal to 100nm; the loading amount of the metal active component Co accounts for 2% of the sum of the weight of the catalyst carrier S and the metal active component Co 15%.

[0041] Its preparation method comprises...

Embodiment 2

[0052] A core-shell structure multi-stage porous cobalt-based Fischer-Tropsch synthesis catalyst, comprising a catalyst carrier S, a metal active component Co loaded on the catalyst carrier S, and a shell molecular sieve membrane M wrapped on the surface of the catalyst carrier S, wherein, Catalyst support S is Al 2 o 3 , Al 2 o 3 The microstructure is spherical, and its average specific surface area is 290m 2 / g, the particle size range is 10-50 mesh; the shell molecular sieve membrane M is a cluster aggregate with evenly dispersed H-ZSM-5 nanoparticles, and the average particle size range of H-ZSM-5 nanoparticles is 10-30nm. The pore diameter of its own micropores is less than or equal to 2.0nm, and the gap between adjacent H-ZSM-5 nanoparticles is less than or equal to 100nm; the loading amount of the metal active component Co accounts for 2% of the sum of the weight of the catalyst carrier S and the metal active component Co 20%.

[0053] Its preparation method compri...

Embodiment 3

[0064] A core-shell structure multi-stage porous cobalt-based Fischer-Tropsch synthesis catalyst, comprising a catalyst carrier S, a metal active component Co loaded on the catalyst carrier S, and a shell molecular sieve membrane M wrapped on the surface of the catalyst carrier S, wherein, Catalyst support S is SiO 2 , SiO 2 The microstructure is spherical, and its average specific surface area is 170m 2 / g, the particle size range is 10-50 mesh; the shell layer molecular sieve membrane M is a cluster aggregate with evenly dispersed H-ZSM-5 nanoparticles, and the average particle size range of H-ZSM-5 nanoparticles is between 10-30nm , its own micropore diameter is less than or equal to 2.0nm, and the gap between adjacent H-ZSM-5 nanoparticles is less than or equal to 100nm; the loading amount of the metal active component Co accounts for the weight of the catalyst carrier S and the metal active component Co and 15%.

[0065] Its preparation method comprises the following s...

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Abstract

Provided are a multi-level channel-type cobalt-based Fischer-Tropsch synthetic catalyst with a core-shell structure and a preparation method therefor. The catalyst comprises a catalyst carrier S, a metal active component Co loaded on the catalyst carrier S and a shell layer molecular sieve membrane M which wraps the surface of the catalyst carrier S, wherein the catalyst carrier S is one of or a mixture of two of SiO2 and Al2O3 in any proportion, the microstructure morphology of SiO2 and Al2O3 is spherical, the specific surface area thereof is 160-290 m2 / g, and the average particle size ranges between 10 and 50 meshes; the shell layer molecular sieve membrane M is a cluster aggregate of uniformly dispersed H-ZSM-5 nanoparticles, the particle size of the H-ZSM-5 nanoparticles ranges between 10-30 nm, the micropore aperture thereof is less than or equal to 2.0 nm, and the gap between adjacent H-ZSM-5 nanoparticles is less than or equal to 100 nm; and the loading amount of the metal active component Co accounts for 10-30% of the sum of the weights of the catalyst carrier S and the metal active component Co. The shell layer of the Fischer-Tropsch synthetic catalyst has a multi-level channel and a high catalytic efficiency. Meanwhile, the preparation method is simple in process and low in energy consumption.

Description

technical field [0001] The invention belongs to the technical field of Fischer-Tropsch synthesis, and specifically refers to a core-shell structure multi-stage channel type cobalt-based Fischer-Tropsch synthesis catalyst and a preparation method thereof. Background technique [0002] The Fischer-Tropsch synthesis reaction refers to the synthesis of coal, natural gas, biomass and other resources through synthesis gas (CO and H 2 ) Catalyzed conversion into hydrocarbons. The products of Fischer-Tropsch synthesis are sulfur-free, nitrogen-free and aromatic-free, so the liquid fuels generated by Fischer-Tropsch synthesis can meet the increasingly stringent environmental protection requirements. key raw material. Therefore, the Fischer-Tropsch synthesis reaction is one of the important ways for the indirect conversion of non-oil-based resources to high-quality liquid fuels and chemical raw materials. Low-carbon olefins are important organic chemical raw materials, and their pr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/46C10G2/00
CPCB01J29/46B01J35/08C10G2/00
Inventor 海国良宋德臣李昌元刘倩倩饶莎莎詹晓东
Owner WUHAN KAIDI ENG TECH RES INST CO LTD
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