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Application of a supported catalyst for improving the selective hydrogenation of citronellal

A supported catalyst and selective technology, applied in catalytic reaction, molecular sieve catalyst, organic compound/hydride/coordination complex catalyst, etc., can solve problems such as difficulty, catalyst selectivity decrease, conversion rate decrease, etc. Improve selectivity and the effect of the method is simple and easy to implement

Active Publication Date: 2021-05-18
NANJING TECH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are many common methods for loading metal particles on porous carriers, such as equal-volume impregnation method, vapor deposition method, dual-solvent method, etc., but their common drawback is that the loaded metal nanoparticles cannot completely enter the inside of the pores. The outer surface is also loaded, resulting in a decrease in the selectivity of the catalyst and the generation of by-products, which will increase the difficulty of subsequent product separation and purification
With the deepening of the research, metal nanoparticles are encapsulated inside the organometallic framework, which improves the catalytic selectivity, but the reduction of active sites and the confinement effect of the channels will significantly reduce the conversion rate.
The problem that selectivity and conversion cannot be achieved at the same time still exists, and it is still difficult to apply it to industry in large-scale preparation

Method used

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  • Application of a supported catalyst for improving the selective hydrogenation of citronellal
  • Application of a supported catalyst for improving the selective hydrogenation of citronellal
  • Application of a supported catalyst for improving the selective hydrogenation of citronellal

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Nitride Metallic Platinum Nanoparticles / Molecular Sieve Catalysts

[0028] Select a type A molecular sieve with a pore size of 3 angstroms, adopt the traditional method: equal volume impregnation method, impregnate the chloroplatinate solution on the molecular sieve, dry at 80°C for 10h, and reduce it at 300°C for 2h in a hydrogen atmosphere to prepare A Pt / molecular sieve supported catalyst was obtained.

[0029] Weigh 40 mg of the above-prepared Pt / 3A catalyst, and place it in a vacuum oven at 120°C for 12 hours to dry before performing the reaction to remove the gas and water that may be adsorbed in the pores of the molecular sieve. Weigh 40 mg of the dried catalyst and place it in the inner liner of a 40 mL autoclave, add 3 mL of ethyl acetate and 300 mg of 2-phenylquinoline, ultrasonicate the mixture for 2 minutes, add the rotor, fully stir for 4 h, and The poisoned mixture was centrifuged to obtain a poisoned Pt / 3A catalyst.

Embodiment 2

[0031] Nitride Metallic Platinum Nanoparticles / Molecular Sieve Catalysts

[0032] Select a type A molecular sieve with a pore size of 3 angstroms, adopt the traditional method: equal volume impregnation method, impregnate the chloroplatinate solution on the molecular sieve, dry at 80°C for 10h, and reduce it at 300°C for 2h in a hydrogen atmosphere to prepare A Pt / molecular sieve supported catalyst was obtained.

[0033] Weigh 40 mg of the above-prepared Pt / 3A catalyst, and place it in a vacuum oven at 120°C for 12 hours to dry before performing the reaction to remove the gas and water that may be adsorbed in the pores of the molecular sieve. Weigh 40 mg of the dried catalyst and place it in the lining of a 40 mL autoclave, add 3 mL of ethyl acetate and 300 μL of pyridine, ultrasonicate the mixture for 2 minutes, add the rotor, stir thoroughly for 4 hours, and centrifuge the poisoned mixture Separated to obtain a poisoned Pt / 3A catalyst.

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Abstract

The invention discloses the application of a supported catalyst for improving the selective hydrogenation of citronellal. The catalyst is applied to the selective hydrogenation of citronellal. The preparation method of the catalyst is as follows: when the catalyst carrier is porous For the carrier, use a poisoning agent with a kinetic diameter larger than the pore size of the carrier to fully stir the reaction with the pre-prepared supported catalyst to obtain a poisoned supported catalyst; when the catalyst carrier is a non-porous carrier, use a kinetic diameter larger than the target selectivity The poisoning agent of the reactant is fully stirred and reacted with the pre-prepared supported catalyst to obtain the poisoned supported catalyst; wherein, the poisoning agent is all nitrides that can strongly interact with the active components. The method precisely regulates the chemical selectivity of the catalyst by using a nitrogen poisoning agent, and can significantly improve the selectivity of citronellol by utilizing the molecular size selectivity and the selectivity of the exposed chemical reaction site under the premise of maintaining a conversion rate of 98%. selective.

Description

technical field [0001] The invention relates to the technical field of selective catalysts, in particular to the application of a supported catalyst for improving the selective hydrogenation of citronellal. Background technique [0002] As an important compound, unsaturated alcohols have important applications in the fields of pharmaceuticals, perfumes, and spices. Such compounds have limited natural sources and are usually prepared from unsaturated aldehydes by hydrogenation of C=O bonds. However, selective C=O bond hydrogenation is difficult to achieve due to the thermodynamic advantage of C=C bond hydrogenation on conventional heterogeneous catalysts, such as metal oxide-supported metal nanoparticles. Therefore, it is very meaningful to design a catalyst that can selectively hydrogenate C=O bonds. Selective catalysis is a method to maximize the use of resources to obtain target products, which greatly reduces the separation work in the later stage, and is being explored...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/74B01J31/02B01J31/26C07C29/141C07C33/025
CPCB01J29/7407B01J31/0244B01J31/26B01J2229/18B01J2229/34B01J2231/643C07C29/141C07C33/025
Inventor 张伟娜霍峰蔚房传真张所瀛孟凡辰张文磊
Owner NANJING TECH UNIV