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Magnetic functional zeolite molecular sieve catalyst and preparation method thereof

A zeolite molecular sieve and catalyst technology, applied in the field of magnetic functional zeolite molecular sieve catalyst and its preparation, can solve the problems of difficulty in wide application, poor mechanical strength, no report on the synthesis of single-crystal zeolite-coated magnetic nanoparticle materials, etc., and the method is simple and rapid. , The effect of large micropore specific surface area and high yield

Active Publication Date: 2021-10-01
FUDAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although a composite structure with inorganic magnetic nanoparticles as the core and microporous zeolite as the shell has been obtained, the shell zeolite is a polycrystalline aggregate with poor mechanical strength, which makes it difficult to be widely used in industry
So far, there is no report on the synthesis of single crystal zeolite-encapsulated magnetic nanoparticles

Method used

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  • Magnetic functional zeolite molecular sieve catalyst and preparation method thereof
  • Magnetic functional zeolite molecular sieve catalyst and preparation method thereof
  • Magnetic functional zeolite molecular sieve catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] (1) Add 0.02 g Fe 3 o 4 Nanoparticles were dispersed in 10 ml of ethanol and 90 ml of deionized water, followed by the addition of 4 ml of concentrated ammonia. Under mechanical stirring, 1 ml of tetraethyl orthosilicate (TEOS) was slowly added dropwise and hydrolyzed for 1 h at room temperature. Add 0.01 g of resorcinol and 0.02 ml of formaldehyde to the above system, and continue to react with mechanical stirring at room temperature for 1 day. Finally, the product is separated with a magnet, and the product obtained is washed with water and ethanol;

[0033] (2) Fe will be obtained 3 o 4 @SiO 2 @RF (phenolic resin) is roasted and carbonized under nitrogen, and the carbonized Fe 3 o 4 @SiO 2 @C and then etched SiO with 1 mole per liter of sodium hydroxide solution in an 80-degree oil bath 2 get Fe 3 o 4 @hollow@C;

[0034] (3) will get 0.01 g Fe 3 o 4 @hollow@C dispersed in 5 ml of (0.1 Tetraethyl orthosilicate: 0.2 Tetrapropylammonium hydroxide: 0 Alumin...

Embodiment 2

[0036] (1) Add 0.1 g CoFe 2 o 4 Nanoparticles were dispersed in 50 ml of ethanol and 50 ml of deionized water, followed by the addition of 1 ml of concentrated ammonia. Under mechanical stirring, 2 ml of tetramethyl orthosilicate (TMOS) was slowly added dropwise and hydrolyzed for 1 h at room temperature. Then, 0.05 g of phenol and 0.1 ml of formaldehyde were added to the above system, and mechanical stirring was continued for 1 day at room temperature. Finally, the product is separated with a magnet, and the product obtained is washed with water and ethanol;

[0037] (2) CoFe will be obtained 2 o 4 @SiO 2 @RF (phenolic resin) is roasted and carbonized under nitrogen, and the carbonized CoFe 2 o 4 @SiO 2 @C and then etched SiO with 1 mole per liter of ammonia water in an 80-degree oil bath 2 Get CoFe 2 o 4 @hollow@C;

[0038] (3) will get 0.1 g CoFe 2 o 4 @hollow@C dispersed in 10 ml of (2 sodium silicate: 0.5 tetraethylammonium hydroxide: 0.02 aluminum sulfate: ...

Embodiment 3

[0040] (1) Add 0.05 g Fe 3 o 4 Nanoparticles were dispersed in 30 ml of ethanol and 60 ml of deionized water, followed by the addition of 3 ml of concentrated ammonia. Under mechanical stirring, 1 ml of tetrabutyl orthosilicate (TBOS) was slowly added dropwise and hydrolyzed for 1 h at room temperature. Add 0.03 g of hydroquinone and 0.06 ml of formaldehyde to the above system, and continue to react with mechanical stirring at room temperature for 1 day. Finally, the product is separated with a magnet, and the product obtained is washed with water and ethanol;

[0041] (2) Fe will be obtained 3 o 4 @SiO 2 @RF (phenolic resin) is roasted and carbonized under nitrogen, and the carbonized Fe 3 o 4 @SiO 2 @C and then etched SiO with 1 mole per liter of sodium hydroxide solution in an 80-degree oil bath 2 get Fe 3 o 4 @hollow@C;

[0042] (3) will get 0.05 g Fe 3 o 4 @hollow@C is dispersed in 5 ml of (1 silica: 0.1 tetrabutylammonium hydroxide: 0.02 sodium metaaluminat...

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Abstract

The invention belongs to the technical field of chemical catalysts, and particularly relates to a magnetic functional zeolite molecular sieve catalyst and a preparation method thereof. The magnetic functional zeolite molecular sieve catalyst disclosed by the invention is prepared by coating a zeolite molecular sieve shell layer with an ordered microporous structure on the surface of magnetic nanoparticles by utilizing a gradient crystallization confinement growth technology. The method comprises the following steps: adopting a sol-gel chemical synthesis method, sequentially wrapping inorganic magnetic nanoparticles with amorphous silicon dioxide and a phenolic resin shell layer, and then performing carbonization-etching to obtain a carbon-wrapped magnetic nanoparticle compound with a hollow structure; and putting the magnetic nanoparticles with the hollow structure into a molecular sieve mother solution, carrying out hydrothermal crystallization for three times, and roasting to obtain the catalyst with the zeolite molecular sieve coated outside the magnetic nanoparticles. The magnetic functional zeolite material has relatively strong magnetic responsiveness, and has a wide application prospect in a zeolite catalytic reaction in a magnetically stabilized bed reactor.

Description

technical field [0001] The invention belongs to the technical field of chemical catalysts, and in particular relates to a magnetic functional zeolite molecular sieve catalyst and a preparation method thereof. Background technique [0002] Microporous zeolite molecular sieves are widely used in industrial heterogeneous catalytic reactions due to their uniform and well-developed micropore channels, adjustable acidity and good hydrothermal stability. The heterogeneous catalytic reaction is usually carried out with the solid zeolite catalyst and the reaction medium under the condition of mechanical stirring or air blowing stirring. With the end of the reaction, the catalyst and the product are taken out of the reactor. In order to realize the recycling of the catalyst, the catalyst and the reaction medium need to be separated into solid and liquid. The commonly used separation methods are filtration and pressure filtration. However, due to the low separation efficiency of the ...

Claims

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Application Information

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IPC IPC(8): B01J29/03B01J29/14B01J29/46B01J29/76B01J37/03B01J37/06B01J37/08B01J35/10C07C1/20C07C11/04C10G50/00
CPCB01J29/0333B01J29/146B01J29/46B01J29/7615B01J29/7607B01J37/036B01J37/06B01J37/082B01J37/0018C07C1/20C10G50/00B01J2229/186C10G2400/30C10G2300/70C10G2300/1092B01J35/397B01J35/33B01J35/23B01J35/61C07C11/04Y02P20/52Y02P30/40Y02P30/20Y02P20/584
Inventor 李伟马冰段林林卜凡兴王金秀赵东元
Owner FUDAN UNIV