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Kenone selective hydrogenation catalyst, and preparation method and application thereof

A hydrogenation catalyst and selective technology, applied in catalyst activation/preparation, carbon-based compound preparation, chemical instruments and methods, etc. problems, to achieve high hydrogenation conversion rate and corresponding saturated ketone selectivity, improve the target product selectivity, reduce the effect of catalyst cost

Active Publication Date: 2021-12-14
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] CN101518734A discloses a catalyst for catalytic combustion of low calorific value gas, the catalyst contains 60-80% γ-Al 2 o 3 , 19.9-39.5% oxides of La or Mn or their combination, and the remaining components are Pd, which improves the high-temperature activity of the catalyst, but the catalyst has a high metal content, and the metal promoter in the oxidation state cannot improve the hydrogenation selectivity of the catalyst. It is tested that the catalyst is used in the hydrogenation of ketene, the substrate conversion rate is low, and the ketone group is also reduced during the reaction, the ketene polymer exceeds 5%, and the product selectivity is low
The catalyst components are complex, the preparation process is cumbersome, and it is difficult to achieve large-scale production
[0006] CN110075887B discloses a palladium-supported catalyst for catalytic combustion of methanol, which mainly solves the problems of high noble metal content and easy deactivation of catalysts prepared in the prior art
Prepared by impregnation and precipitation method, including active component Pd, additives such as manganese nitrate, sodium dihydrogen phosphate and activated alumina carrier, the catalyst has high activity and selectivity in the catalytic combustion of methanol, and the precious metal is not easy to agglomerate and lose active, but the catalyst has a low conversion rate and poor selectivity of the hydrogenation substrate in the enone hydrogenation reaction, and the ketone group is also reduced during the reaction

Method used

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  • Kenone selective hydrogenation catalyst, and preparation method and application thereof
  • Kenone selective hydrogenation catalyst, and preparation method and application thereof
  • Kenone selective hydrogenation catalyst, and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0071] Preparation of enone selective hydrogenation catalyst:

[0072] (1) Take 10g nanometer terbium oxide and hydrogen for hydrogenation reaction, the mass space velocity is 10h -1 , the reaction temperature is 600°C, the reaction pressure is 3MPa, and the reaction time is 2h. The product obtained by the hydrogenation reaction is placed in a metal ball mill and ground for 3h under a hydrogen atmosphere to obtain TbH with a particle size of 0.01mm to 1mm. 3 particles.

[0073] (2) Get 10g of nano manganese dioxide and ammonia to carry out nitriding reaction, the mass space velocity is 5h -1 , the reaction temperature is 700°C, the reaction pressure is 2MPa, and the reaction time is 120h. The obtained product is placed in a metal ball mill and ground for 3h under an ammonia atmosphere to obtain MnN particles with a particle size of 0.01mm-1mm.

[0074] (3) Take 26.32g of pseudo-boehmite (dry basis alumina content 76wt%, 0.196mol), add 20ml of deionized water, stir for 1 hour...

Embodiment 2

[0080] Preparation of enone selective hydrogenation catalyst:

[0081] (1) Take 10g nanometer terbium oxide and hydrogen for hydrogenation reaction, the mass space velocity is 5h -1 , the reaction temperature is 700°C, the reaction pressure is 2MPa, and the reaction time is 1h. The obtained product is placed in a metal ball mill and ground for 10h under a hydrogen atmosphere to obtain TbH with a particle size of 0.02-0.08mm. 3 particles.

[0082] (2) Take 10g of nano-manganese dioxide and ammonia for nitriding reaction to prepare MnN, and the mass space velocity is 2h -1 , the reaction temperature is 800°C, the reaction pressure is 1MPa, and the reaction time is 150h. The obtained product is placed in a metal ball mill, and ground for 10h under an ammonia atmosphere to obtain MnN particles with a particle size of 0.02-0.08mm.

[0083] (3) Take 26.32g of pseudo-boehmite (produced by German Sasol company, brand SB, alumina content 76wt%), add 20ml of deionized water, stir for 1h...

Embodiment 3

[0089] Preparation of enone selective hydrogenation catalyst:

[0090] (1) Take 10g nanometer terbium oxide and hydrogen for hydrogenation reaction, the mass space velocity is 2h -1 , the reaction temperature is 500°C, the reaction pressure is 1MPa, and the reaction time is 3h. The obtained product is placed in a metal ball mill and ground for 5h under a hydrogen atmosphere to obtain TbH with a particle size of 0.02-0.1mm. 3 particles.

[0091] (2) Take 10g of nano-manganese dioxide and ammonia for nitriding reaction to prepare MnN, and the mass space velocity is 10h -1 , the reaction temperature is 500°C, the reaction pressure is 3MPa, and the reaction time is 90h. The obtained product is placed in a metal ball mill, and ground for 5h under an ammonia atmosphere to obtain MnN particles with a particle size of 0.02-0.1mm.

[0092] (3) Take 26.32g of pseudo-boehmite (dry basis alumina content 76wt%, 0.196mol), add 20ml of deionized water, stir for 1 hour to make it slurry, an...

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Abstract

The present invention provides a ketene selective hydrogenation catalyst, and a preparation method and application thereof. The catalyst comprises an alumina carrier and active components, and the active components comprise 0.2-1 wt% of palladium, 0.5-2 wt% of manganese nitride (in terms of manganese element), and 0.5-6 wt% of hydride of at least one of terbium, cerium, yttrium and lutetium (in terms of metal element) based on the mass of the carrier. The catalyst is low in palladium content, is used for preparing corresponding saturated ketones through selective hydrogenation of ketene, has higher activity, and can inhibit ketene polymerization and reduce side reaction selectivity.

Description

technical field [0001] The invention belongs to the technical field of enone catalytic hydrogenation, and relates to a catalyst for the selective hydrogenation of enone and its preparation method and application, specifically, a catalyst for the selective hydrogenation of enone to the corresponding saturated ketone and its preparation method and apply. Background technique [0002] At present, palladium-based catalysts are commonly used in industry to promote the selective hydrogenation of enones. This is because the transition metal palladium has a good activation performance for hydrogen, and the surface of the transition metal Pd can be passivated to inhibit the reduction of the ketone group. Thereby improving the reaction selectivity. The Lindlar catalyst mainly used in the selective hydrogenation reaction of enone in industrial production is the strategy of surface passivation, and the Pd / C catalyst is modified with additives such as lead and bismuth, but the Lindlar c...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J31/12B01J27/24B01J23/44B01J35/10B01J21/04C07C45/62C07C49/04
CPCB01J31/121B01J27/24B01J23/44B01J21/04B01J37/0201B01J37/0036B01J37/08C07C45/62B01J35/635B01J35/615C07C49/04
Inventor 刘泽超谢硕张永振黄文学沈稳鲍元野
Owner WANHUA CHEM GRP CO LTD
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