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A kind of α, β-unsaturated aldehyde selective hydrogenation conversion catalyst and its preparation method and application

A technology for aldehyde selectivity and hydrogenation conversion, which is applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, chemical instruments and methods, etc. Solve problems such as leaching and catalyst deactivation, and achieve the effects of adjustable pore size, easy synthesis, improved reaction selectivity, and high specific surface area

Active Publication Date: 2022-06-28
SOUTHEAST UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] Purpose of the invention: To solve the problems of conventional supported selective catalytic hydrogenation catalysts such as competitive adsorption of reaction substrates, poor selectivity to target products, easy leaching of active components under working conditions and deactivation of the catalyst, the present invention provides an α,β- A catalyst for the selective hydrogenation conversion of unsaturated aldehydes, and a preparation method of the catalyst is provided; in addition, the invention also provides an application of the catalyst for the selective catalytic hydrogenation of α, β-unsaturated aldehydes to prepare unsaturated alcohols

Method used

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  • A kind of α, β-unsaturated aldehyde selective hydrogenation conversion catalyst and its preparation method and application

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Embodiment 1

[0029] A preparation method of α,β-unsaturated aldehyde selective hydroconversion catalyst, comprising the following steps:

[0030] (1) Disperse 0.08g CuO in 100mL absolute ethanol, slowly add 1.50g polyvinylpyrrolidone;

[0031] (2) After the above-mentioned mixture was stirred at room temperature for 12 hours and mixed uniformly, it was added to a mixed solution containing 50 mL of deionized water, 50 mL of absolute ethanol, and 4 mL of ammonia water (28 wt %), and 1.5 g of hexadecyl triacetate was added during the stirring process. Methyl ammonium bromide and 3.0 g of ethyl orthosilicate were stirred at room temperature for 12 hours and mixed well, then transferred to a hydrothermal reactor, reacted at 120 °C for 15 hours, and after natural cooling, the reaction solution was centrifuged and washed, Dry at 80 °C for 15 h to obtain CuO@SiO 2 ;

[0032] (3) CuO@SiO obtained in step (2) 2 Disperse in 30 mL of an aqueous solution containing 0.20 g of cerium nitrate hexahydra...

Embodiment 2

[0036] A preparation method of α,β-unsaturated aldehyde selective hydroconversion catalyst, comprising the following steps:

[0037] (1) Take 0.06g PtO 2 Disperse in 90mL absolute ethanol, slowly add 1.30g polyvinylpyrrolidone;

[0038] (2) After the above mixture was stirred at room temperature for 10 hours and mixed well, it was added to a mixed solution containing 45 mL of deionized water, 45 mL of absolute ethanol, and 3.7 mL of ammonia water (28 wt %), and 1.2 g of hexadecyl was added during the stirring process. Trimethylammonium bromide and 2.8g of ethyl orthosilicate were stirred at room temperature for 10h and mixed uniformly, then transferred to a hydrothermal reactor, reacted at 180°C for 10h, and after natural cooling, the reaction solution was centrifuged and washed , and dried at 120 °C for 10 h to obtain PtO 2 @SiO 2 ;

[0039] (3) PtO obtained in step (2) 2 @SiO 2 Disperse in 20 mL of an aqueous solution containing 0.30 g of indium nitrate, stir at room t...

Embodiment 3

[0043] A preparation method of α,β-unsaturated aldehyde selective hydroconversion catalyst, comprising the following steps:

[0044] (1) get 0.15g NiO and disperse in 110mL absolute ethanol, slowly add 1.70g polyvinylpyrrolidone;

[0045] (2) After the above mixture was stirred at room temperature for 15 hours and mixed well, it was added to a mixed solution containing 55 mL of deionized water, 55 mL of absolute ethanol, and 4.2 mL of ammonia water (28 wt %), and 1.8 g of hexadecyl was added during the stirring process. Trimethylammonium bromide and 3.2g of ethyl orthosilicate were stirred at room temperature for 15h and mixed uniformly, then transferred to a hydrothermal reactor, reacted at 140°C for 14h, and after natural cooling, the reaction solution was centrifuged and washed , and dried at 90 °C for 14 h to obtain NiO@SiO 2 ;

[0046] (3) NiO@SiO obtained in step (2) 2 Disperse in 55mL aqueous solution containing 0.35g ammonium metavanadate, stir at room temperature f...

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Abstract

The invention discloses an α, β-unsaturated aldehyde selective hydrogenation conversion catalyst and its preparation method and application. The catalyst uses metal M as the core and porous silica as the shell to form M@SiO 2 After the core-shell structure, the SiO 2 Other metal oxides M'O are loaded on the surface of the shell, and M'O is prepared by reduction x / M@SiO 2 catalyst. The M'O x / M@SiO 2 The catalyst has M in the core and M'O outside the core x Two active faces with different catalytic properties; due to SiO 2 Porous structure, H 2 The dynamic diameter of α,β-unsaturated aldehydes is quite different, affected by mass transfer resistance, H 2 Molecules enter the core M surface for activation and dissociation to form H, H overflows to the surface and M’O x Adsorption activation of α,β‑unsaturated aldehydes. The catalyst of the invention can not only reduce the competitive adsorption of reaction substrates, improve the selectivity, but also reduce M sintering in the nucleus and improve the stability of the catalyst. The α, β-unsaturated aldehyde selective hydrogenation conversion catalyst of the present invention is used for the catalytic hydrogenation of α, β-unsaturated aldehydes to prepare unsaturated alcohols, effectively improving the catalytic conversion rate of α, β-unsaturated aldehydes and unsaturated alcohols selective.

Description

technical field [0001] The invention belongs to the industrial catalyst technology, and particularly relates to an α,β-unsaturated aldehyde selective hydrogenation conversion catalyst and a preparation method and application thereof. Background technique [0002] α,β-Unsaturated aldehydes can be selectively hydrogenated to obtain unsaturated alcohols, saturated aldehydes and saturated alcohols. Among them, unsaturated alcohol is an important raw material in the production process of pesticide, fragrance, medicine, resin and other fine chemical products. However, the selective hydrogenation of α,β-unsaturated aldehydes is thermodynamically and kinetically favorable for the hydrogenation of C=C bonds rather than C=O bonds due to the larger bond energy of C=O bonds than C=C bonds of hydrogenation. Therefore, improving the hydrogenation selectivity of C=O bonds to obtain unsaturated alcohols has always been a great challenge in basic research and industrial applications. [0...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/83B01J23/62B01J23/847B01J23/44C07D307/44C07D307/42C07C29/141C07C33/32C07C33/02
CPCB01J23/83B01J23/62B01J23/8472B01J23/44C07D307/44C07D307/42C07C29/141B01J35/397C07C33/32C07C33/02
Inventor 吴东方张金鑫
Owner SOUTHEAST UNIV