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Anthraquinone hydrogenation heterogeneous channel monolithic catalyst and preparation method thereof

An integral catalyst, catalyst technology, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc., can solve the problem of difficult to achieve higher conversion depth, insufficient conversion depth, Problems such as decreased activity and selectivity

Active Publication Date: 2019-04-12
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The hydrogen efficiency of the catalyst has been significantly improved, but there are still shortcomings such as many preparation steps, large amount of noble metals and low catalyst selectivity.
[0010] In the prior art, generally used monolithic catalysts have a uniform pore size structure, that is, during the reaction, the flow rate of the reactant in the pore is constant, but as the reaction progresses, the content of the reactant in the reaction system continues to decrease, and the same Under the condition of flow rate, it is difficult to achieve a higher conversion depth, which leads to side reactions at the beginning due to the high initial activity of the catalyst, and in the later stage, the conversion depth is not enough due to too fast flow rate, that is, the activity and selectivity of the reaction are uniform. lower result

Method used

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  • Anthraquinone hydrogenation heterogeneous channel monolithic catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] a) Fully mix 5000 grams of aluminum hydroxide dry rubber powder (dry basis 73.6w%), 100 grams of methyl cellulose, 4300 grams of water and 500 grams of 30w% nitric acid solution to form a plastic paste, put the paste Put it into a die with a hole density of 300 / square inch, a height of 10 cm, and an area ratio of opening I and opening II of 1:5, extrude into a multi-channel overall structure, dry at 150°C for 12 hours, and bake at 650°C for 4 hours. Hour, obtain catalyst carrier;

[0028] b) Take a honeycomb-shaped γ-alumina block with a pore size of 300, an area ratio of opening I and opening II of 1:5, and a height of 10 cm, and immerse it in an aqueous solution of 0.5Mol / L palladium chloride at room temperature. Immerse for 5 minutes, blow out the remaining solution in the channel after taking it out, dry at 120°C for 6 hours, bake at 450°C for 2 hours, repeat twice to obtain the catalyst in the oxidation state;

[0029] c) put the oxidized catalyst obtained in step...

Embodiment 2

[0032] The catalyst preparation method is the same as in Example 1, except that the metal type, content, mesh number of the carrier, the area ratio of the upper and lower openings of the carrier channel, and the reduction conditions are different. The reducing agent used is hydrogen, and the reduction conditions are: hydrogen The pressure was 2MPa, the temperature was 300°C, and the catalysts obtained were numbered E-2 for 4 hours. See Table 1 for the specific conditions and reaction results.

Embodiment 3~7

[0034] The catalyst preparation method is the same as that in Example 1, except that the metal species used, the content, the mesh number of the support, the area ratio of the support pore opening I and the opening II, the shape of the support opening, and the reduction conditions are different. The obtained catalyst The numbers are E-3~E-7 respectively, and the specific conditions and reaction results are shown in Table 1.

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Abstract

The invention discloses an anthraquinone hydrogenation non-uniform pore overall catalyst and a preparation method thereof. The area ratio of the opening I and the opening II at both ends of the pore channel of the catalyst is 1:1.1~1:100, preferably 1:2~1 : 10. The cross-sectional area of ​​the channel between opening I and opening II increases continuously or stepwise, or a combination of both. The preparation method is as follows: (1) Dip a carrier with an overall catalyst shape into a solution containing active components, take it out after a certain period of immersion, and obtain an oxidized catalyst after drying and roasting; (2) Dip the obtained oxidized catalyst After reduction and then drying under an inert atmosphere, an anthraquinone hydrogenation heterogeneous channel monolithic catalyst is obtained. The monolithic catalyst of the present invention has non-uniform pores and is used in the hydrogenation process of preparing hydrogen peroxide by the anthraquinone method, thereby ensuring the reaction activity of the catalyst while improving the selectivity of the reaction.

Description

technical field [0001] The invention belongs to the field of catalyst preparation, and in particular relates to a reduced noble metal integral catalyst with a non-uniform pore structure, which is mainly used for the anthraquinone hydrogenation reaction in the process of preparing hydrogen peroxide by an anthraquinone method. Background technique [0002] Hydrogen peroxide, also known as hydrogen peroxide, is an important chemical raw material, which has been produced in industry as early as the middle of the 19th century, and is one of the main basic chemical products in the world. With the growth of social demands, especially the increasing importance of ecological environment protection, hydrogen peroxide has become an important chemical. As an oxidizing agent, bleaching agent, disinfectant, polymer initiator and crosslinking agent, it is widely used in papermaking, textile, chemical synthesis, military industry, electronics, food processing, medicine, cosmetics, environme...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J35/10B01J23/44B01J23/42C01B15/023
CPCC01B15/023B01J23/42B01J23/44B01J35/60
Inventor 刘全杰方向晨徐会青贾立明王伟尹泽群
Owner CHINA PETROLEUM & CHEM CORP
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