Molecular sieve packaged core-shell catalyst and preparation method thereof

A technology of core-shell catalysts and molecular sieves, applied in the direction of molecular sieve catalysts, catalyst activation/preparation, chemical instruments and methods, etc., can solve the problems of difficult molecular dynamics diffusion of reaction molecules and products, destruction of molecular sieve channel structure, poor metal dispersion, etc. Achieve the effect of high utilization rate of active center, high catalytic activity and guaranteed dispersion

Active Publication Date: 2022-07-15
SOUTHEAST UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In the present invention, a multi-level pore pure silicon molecular sieve is used to replace the traditional silicon-aluminum molecular sieve to prepare a core-shell catalyst. The inner core can be used as a carrier to uniformly anchor metal nanoparticles, and the outer shell can act as a physical barrier to inhibit the loss of metal nanoparticles. The composite catalyst with multi-level pore structure solves the problems that the skeleton of the molecular sieve is easy to collapse during the reaction process, thus destroying the pore structure of the molecular sieve, difficult molecular dynamics diffusion of reaction molecules and products, poor metal dispersion and short catalyst life.

Method used

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  • Molecular sieve packaged core-shell catalyst and preparation method thereof
  • Molecular sieve packaged core-shell catalyst and preparation method thereof
  • Molecular sieve packaged core-shell catalyst and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0032] (1) Preparation of CuPt / SSZ-39: 3.6g Y zeolite, 23.5g 2,6-dimethyl-N,N-dimethylpiperidine, 14.8g silica sol, 4.8g γ-aminopropyltriethyl Oxysilane and 30 g of deionized water were mixed and stirred thoroughly; the above mixed solution was transferred to a high-pressure reaction kettle, and hydrothermally crystallized at 160 °C for 2 d; after the reaction was completed, filter and separate, and the filter cake was washed with deionized water to medium properties, dried at 80°C for 8h, and then calcined in air at 550°C for 6h to obtain modified SSZ-39 molecular sieve. Weigh 0.03g of chloroplatinic acid and 0.2g of copper sulfate, dissolve them in deionized water to make chloroplatinic acid solution and copper sulfate solution, add 2g of modified SSZ-39 molecular sieve for dipping, filter, wash, and dry the filter cake at 60 °C for 6 hours , to obtain CuPt / SSZ-39.

[0033] (2) Preparation of molecular sieve-encapsulated core-shell catalyst: Measure 8 mL of tetrapropylammon...

Embodiment 2

[0036] (1) Preparation of CuPt / SSZ-39: 5g Beta zeolite, 25.8g 2,6-dimethyl-N,N-dimethylpiperidine, 17.5g sodium silicate, 4.8g γ-aminopropyltrimethoxy Silane and 30 g of deionized water were mixed, and stirred thoroughly; the above mixed solution was transferred to a high-pressure reactor, and crystallized at 165 ° C for 2 d; Dry at 60°C for 6h, and then calcinate in air at 550°C for 7h to obtain modified SSZ-39 molecular sieve. Weigh 0.1g of platinum nitrate and 0.3g of copper nitrate, dissolve them in deionized water to make platinum nitrate solution and copper nitrate solution, add 2g of modified SSZ-39 molecular sieve to impregnate, filter, wash, and dry the filter cake at 60 °C for 6h, CuPt / SSZ-39 was obtained.

[0037] (2) Preparation of molecular sieve-encapsulated core-shell catalyst: Measure 8 mL of tetrapropylammonium bromide solution, 6 mL of methyl orthosilicate and 20 mL of deionized water, weigh 2 g of CuPt / SSZ-39, stir well and transfer to the reaction In the ...

Embodiment 3

[0039] (1) Preparation of CuPt / SSZ-39: 5g MOR zeolite, 30.3g N-ethyl-N-propyl-2,6-dimethylpiperidine, 25.7g sodium silicate, 5.2g γ-aminopropyl Mix trimethoxysilane with 50 g of deionized water, and stir thoroughly; transfer the above mixed solution into a high-pressure reaction kettle, and hydrothermally crystallize at 160 °C for 2 d; after the reaction, filter and separate, and wash the filter cake with deionized water until Neutral, dried at 80°C for 7.5h, and then calcined in air at 750°C for 7h to obtain modified SSZ-39 molecular sieve. Weigh 0.15g of ammonium chloroplatinate and 0.4g of copper acetate, dissolve them in deionized water to make ammonium chloroplatinate solution and copper acetate solution, add 2g of modified SSZ-39 molecular sieve for dipping, filter, wash, and filter cake at 80℃ After drying for 7.5 h, CuPt / SSZ-39 was obtained.

[0040] (2) Preparation of molecular sieve-encapsulated core-shell catalyst: weigh 8 mL of hexadecyl trimethyl ammonium bromide...

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PUM

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Abstract

The invention discloses a molecular sieve packaged core-shell catalyst (Figure 1) and a preparation method thereof, and relates to the field of catalyst preparation. According to the core-shell catalyst, an inner core is CuPt/SSZ-39, a shell is hierarchical pore Silicalite-1, the catalyst is prepared from CuPt/SSZ-39, a silicon source and a quaternary ammonium salt structure-directing agent through a hydrothermal synthesis method, and the inner core is prepared by dipping an SSZ-39 molecular sieve in a CuPt bimetallic precursor solution; the modified SSZ-39 molecular sieve is prepared by modifying an SSZ-39 molecular sieve with a silane coupling agent. The CuPt bimetallic nanoparticles in the catalyst prepared by the invention are anchored on the surface of the modified SSZ-39 molecular sieve and encapsulated in the shell of the hierarchical pore Silicalite-1 molecular sieve, so that the activity and sintering resistance of the catalyst are remarkably improved, and the catalyst can be applied to the fields of petrochemical engineering, fine chemical engineering and the like.

Description

technical field [0001] The invention relates to the technical field of catalysts, in particular to a core-shell catalyst encapsulated by a molecular sieve and a preparation method thereof. Background technique [0002] Bimetallic nanoparticles exhibit desired activities in various catalytic reactions. The size and dispersion of bimetallic nanoparticles have an important influence on the catalytic performance of bimetallic nanocatalytic materials. The smaller the size of bimetallic nanoparticles, the higher the dispersion. , the better the catalytic activity. However, the aggregation and sintering of metal nanoparticles often lead to the loss of catalytic performance during the actual reaction process. At the same time, due to the lack of effective regulation of the reaction site, it is difficult to effectively control the catalytic reaction pathway, which inevitably leads to the occurrence of side reactions such as carbon deposition, which leads to the decrease of the selec...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/76B01J35/00B01J35/10B01J37/02B01J37/10
CPCB01J29/76B01J35/0086B01J35/10B01J37/0201B01J37/10B01J2229/18
Inventor 周钰明王佳佳王彦云鲍杰华左长江李蕊盛晓莉张一卫
Owner SOUTHEAST UNIV
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