Cerium modified supported type nickel-based catalyst as well as preparation method and application thereof

A nickel-based catalyst, supported technology, applied in the preparation of amino compounds, chemical instruments and methods, preparation of organic compounds, etc., can solve the problems of increasing the difficulty of recycling precious metal catalysts, complicated preparation process of modified catalysts, etc. and low cost of use, good product quality, and the effect of overcoming side reactions

Active Publication Date: 2017-06-30
ZHEJIANG LINJIANG CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the preparation process of the modified catalyst is more complicated, and the addition of auxiliary elements increases the difficulty of recycling the precious metal catalyst.

Method used

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  • Cerium modified supported type nickel-based catalyst as well as preparation method and application thereof
  • Cerium modified supported type nickel-based catalyst as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Weigh 20 grams of titanium dioxide carrier, impregnate it in an equal volume of mixed aqueous solution of nickel nitrate and cerium nitrate (dissolve 5 grams of nickel nitrate and 0.5 grams of cerium nitrate in 20 mL of aqueous solution), immerse for 4 hours, and dry at 110 ° C for 3 hours Afterwards, calcining at 500°C for 4 hours, and then reducing in hydrogen flow at 400°C for 2 hours to obtain a cerium-modified supported nickel-based catalyst.

Embodiment 2

[0031] Weigh 20 grams of titanium dioxide carrier, impregnate it in an equal volume of mixed aqueous solution of nickel nitrate and cerium nitrate (dissolve 10 grams of nickel nitrate and 0.5 grams of cerium nitrate in 20 mL of aqueous solution), immerse for 6 hours, and dry at 120 ° C for 2 hours Afterwards, it was calcined at 600°C for 3 hours, and then reduced in a hydrogen flow at 450°C for 2 hours to obtain a cerium-modified supported nickel-based catalyst.

Embodiment 3

[0033] Weigh 20 grams of titanium dioxide carrier, impregnate it in an equal volume of mixed aqueous solution of nickel nitrate and cerium nitrate (dissolve 2 grams of nickel nitrate and 0.2 grams of cerium nitrate in 20 mL of aqueous solution), immerse for 3 hours, and dry at 90 ° C for 4 hours Afterwards, it was calcined at 400°C for 6 hours, and then reduced in a hydrogen flow at 550°C for 1 hour to obtain a cerium-modified supported nickel-based catalyst.

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Abstract

The invention discloses a cerium modified supported type nickel-based catalyst as well as a preparation method and an application thereof. In the catalyst, metallic nickel particles and metallic cerium particles are uniformly dispersed in surfaces and pore channels of titanium dioxide supporters. The preparation method of the catalyst comprises steps as follows: the titanium dioxide supporters are impregnated with a nickel nitrate and cerium nitrate mixed aqueous solution with an incipient-wetness impregnation method, dried, roasted and reduced in hydrogen stream, and the catalyst is prepared. The catalyst has lower preparation and use cost; compared with a traditional skeletal nickel catalyst, the catalyst overcomes side reactions of hydrogenated dehalogenation, addition of a dehalogenation inhibitor is not needed, selectivity of a product is high, quality of the product is good, and the catalyst can be applied to a reaction for preparing halogenated aromatic amine from haloaromatic nitrocompounds through catalytic hydrogenation.

Description

technical field [0001] The invention relates to a cerium-modified supported nickel-based catalyst, a preparation method and application thereof. Background technique [0002] Halogenated aromatic amines are an important class of organic chemical intermediates, widely used in the synthesis of fine chemicals such as medicine, dyes and pigments. [0003] Halogenated aromatic amines are generally prepared from halogenated aromatic nitro compounds through reduction reactions, mainly including chemical reduction and catalytic hydrogenation reduction. Chemical reduction methods include iron powder reduction method, alkali sulfide reduction method and hydrazine hydrate reduction method, etc., but these reduction methods have disadvantages such as large environmental pollution, low product yield, and poor product quality, and have been gradually eliminated. The catalytic hydrogenation reduction method has the advantages of high yield, good product quality, mild reaction environment,...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/83C07C209/36C07C211/52
CPCB01J23/83B01J35/0093C07C209/365C07C211/52
Inventor 易苗尹新
Owner ZHEJIANG LINJIANG CHEM
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