Catalyst with non-noble metal nanoclusters confined and stabilized in silicalite-1 molecular sieve pore channels, and preparation method and application thereof

A non-precious metal, nano-cluster technology, used in molecular sieve catalysts, catalyst activation/preparation, carbon-based compound preparation, etc., can solve the problems of reducing the catalytic activity of metal nanoclusters, reducing the structural stability of molecular sieves, etc., to achieve excellent thermal stability , excellent catalytic performance, high yield effect

Pending Publication Date: 2019-10-25
DALIAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the ZSM-5 molecular sieve framework contains aluminum atoms, and the acidity brought by aluminum atoms to the molecular sieve sometimes reduces the catalytic activity of metal nanoclusters, and the introduction of too many aluminum atoms also greatly reduces the structural stability of the molecular sieve itself.

Method used

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  • Catalyst with non-noble metal nanoclusters confined and stabilized in silicalite-1 molecular sieve pore channels, and preparation method and application thereof
  • Catalyst with non-noble metal nanoclusters confined and stabilized in silicalite-1 molecular sieve pore channels, and preparation method and application thereof
  • Catalyst with non-noble metal nanoclusters confined and stabilized in silicalite-1 molecular sieve pore channels, and preparation method and application thereof

Examples

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Embodiment 1

[0034] For any person skilled in the art, without departing from the scope of the technical solution of the present invention, the technical content disclosed above can be used to make many possible changes and modifications to the technical solution of the present invention, or be modified into equivalent changes, etc. effective example. Therefore, any simple modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention should still fall within the protection scope of the technical solution of the present invention.

[0035] The present invention is described in detail below through specific examples, but the present invention is not limited to these examples.

[0036] Example 1

[0037] Add 8g of tetraethyl orthosilicate (TEOS) into a mixed solution of 13g of tetrapropylammonium hydroxide (TPAOH) aqueous solution and 13g of water, stir at 25°C for 3h to obtain a transparent solution A; add 0.01g...

Embodiment 2

[0039] Add 8g of tetraethyl orthosilicate (TEOS) into a mixed solution of 15g of tetrapropylammonium hydroxide (TPAOH) aqueous solution and 15g of water, stir at 25°C for 3h to obtain a transparent solution A; add 0.01g of ferric nitrate Add it to the mixture of 0.1mL ethylenediamine and 1mL aqueous solution, and continue stirring at 25°C for 3h to obtain a transparent solution B; after that, slowly add the obtained solution B into solution A under stirring at 25°C, and then Continue to stir for 3h; after adding 0.05g of sodium hydroxide solid, continue to stir for 3h, the molar ratio of each component in the initial mixture solution in the reaction system is SiO 2 :TPAOH:H 2 O:Fe:NaOH=1:0.435:35.781:0.0049:0.026. The resulting mixture solution was transferred to a 100mL stainless steel reaction kettle, and then the reaction kettle was placed in a 170°C oven for crystallization for 168 hours; after the crystallization was completed, the solid product was separated by centrifu...

Embodiment 3

[0041] Add 8g of tetraethyl orthosilicate (TEOS) into a mixed solution of 18g of tetrapropylammonium hydroxide (TPAOH) aqueous solution and 18g of water, stir at 25°C for 3h to obtain a transparent solution A; add 0.01g of cobalt nitrate Add to the mixture of 0.2mL ethanolamine and 1mL aqueous solution, and continue to stir at 25°C for 3h to obtain a transparent solution B; after that, slowly add the obtained solution B into solution A under stirring at 25°C, and then continue to stir 3h; After adding 0.15g potassium hydroxide solid, continue stirring for 3h, the molar ratio of each component in the initial mixture solution in the reaction system is SiO 2 :TPAOH:H 2 O:Co:KOH=1:0.482:38.954:0.0052:0.039. The resulting mixture solution was transferred to a 100mL stainless steel reaction kettle, and then the reaction kettle was placed in a 170°C oven for crystallization for 168 hours; after the crystallization was completed, the solid product was separated by centrifugation, and...

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Abstract

The invention discloses a catalyst with non-noble metal nanoclusters confined and stabilized in silicalite-1 molecular sieve pore channels, and a preparation method and an application thereof, and belongs to the technical field of molecular sieves. The molecular sieve loaded catalyst provided by the invention has a single nanoparticle with a shape of a hexagonal prism, a length of about 200 nm, awidth of about 200 nm and a thickness of about 100 nm. Non-noble metal nanoclusters contained in the molecular sieve pore channels of the catalyst provided by the invention have good dispersity whichis larger than 80%, comprise non-noble metal elements of Cu, Fe, Co, Ni and Ag, and have a particle size of 1 to 2 nm. The catalyst provided by the invention has ultrahigh single product selectivity in a solvent-free liquid-phase oxidation of toluene, and has good conversion efficiency compared with catalysts of a same kind. Meanwhile, the pore channel structure of the catalyst provided by the invention also has a certain selective redox function for aromatic compounds.

Description

technical field [0001] The invention belongs to the technical field of molecular sieves, and specifically relates to a synthesis method for confining and stabilizing non-noble metal nanoclusters in the pores of Silicalite-1 molecular sieves, a series of preparations of molecular sieve-loaded non-noble metal catalysts, and the use of such catalysts in toluene in a solvent-free liquid phase Applications in oxidation reactions or selective redox reactions of other aromatic compounds. Background technique [0002] In the oxidation reaction of toluene, the methyl group of toluene is not easy to be activated, and an initiator needs to be added to make it undergo a series of chemical reactions. However, the initiator contains toxic elements such as bromine, which limits the application environment of the product and generally has low economic value. At the same time, in the toluene oxidation reaction, a large amount of solvents are required to participate, such as acetic acid, ace...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/035B01J37/10B01J37/08B01J37/18B82Y30/00B82Y40/00C07C45/36C07C47/54
CPCB01J29/0354B01J29/0356B01J37/0018B01J37/10B01J37/18B01J2229/18B82Y30/00B82Y40/00C07C45/36C07C47/54
Inventor 吕荣文黄河叶婉玥
Owner DALIAN UNIV OF TECH
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