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Preparation method of mesoporous silica supported copper catalyst with central radial pore channels

A technology of mesoporous silica and copper catalysts is applied in the preparation of organic compounds, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc. High power consumption, increased by-products, etc., to achieve the effect of being suitable for large-scale industrial production, realizing automatic operation, and reducing environmental pollution

Active Publication Date: 2019-03-08
CHINA CATALYST HLDG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The reaction temperature and pressure of the above-mentioned catalysts are high, and the selectivity of ethylene glycol is low, which leads to high heat and power consumption and increased by-products. In addition, the copper-based catalysts are prone to grain agglomeration and deactivation, which makes the life of the catalyst difficult to meet the requirements of industrialization.

Method used

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  • Preparation method of mesoporous silica supported copper catalyst with central radial pore channels
  • Preparation method of mesoporous silica supported copper catalyst with central radial pore channels
  • Preparation method of mesoporous silica supported copper catalyst with central radial pore channels

Examples

Experimental program
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Effect test

Embodiment 1

[0030] A kind of center radial mesoporous silicon oxide nanosphere supported copper catalyst is prepared by the following method:

[0031] (1) 142.3g ether, 75.2g ethanol, 4.78g concentration are 28% ammoniacal liquor and 438.8g distilled water are mixed to become homogeneous solution, then add 4.20g cetyltrimethylammonium bromide (CTAB) at room temperature at rotating speed After stirring at 1000rpm for 1 hour, 20g of ethyl silicate (TEOS) was quickly added dropwise to the above mixture, stirred at 800rpm for 2 hours, and then heated to 50°C for 12 hours; a white precipitate was obtained;

[0032] (2) The white precipitate obtained in step (1) is filtered, washed and dried at 105°C for 24 hours, then raised to 500°C at a heating rate of 2°C / min and roasted for 6 hours to remove organic components, and obtain a radial channel with a center Mesoporous silica nanospheres (DMSNs), such as figure 1 shown;

[0033] (3) In 200ml of Cu(NO 3 ) 2 Add 5.0mol / L nitric acid solution t...

Embodiment 2

[0035] A kind of center radial mesoporous silicon oxide nanosphere supported copper catalyst is prepared by the following method:

[0036] (1) Mix 175.3g of ether, 96.8g of ethanol, 9.57g of 26% ammonia and 721.3g of distilled water to form a homogeneous solution, then add 4.04g of cetylpyridinium bromide and stir for 1 hour at room temperature at 1500rpm Finally, 20g of methyl silicate was quickly added dropwise to the above mixture, stirred at a rotation speed of 1500rpm for 2 hours, and then heated to 60°C for 6 hours to obtain a white precipitate;

[0037] (2) The white precipitate obtained in step (1) is filtered, washed and dried at 120°C for 12 hours, then raised to 550°C at a heating rate of 5°C / min and roasted for 4 hours to remove organic components, and obtain a radial channel with a center Mesoporous silica nanospheres (DMSNs);

[0038] (3) In 200ml of Cu(CH 3 COO) 2 Add 2.5 mol / L hydrochloric acid solution to the solution to adjust the pH value to 1.0, and add ...

Embodiment 3

[0040] A kind of center radial mesoporous silicon oxide nanosphere supported copper catalyst is prepared by the following method:

[0041] (1) 158.6g of ether, 91.3g of ethanol, 6.89g of 25% ammonia and 449.3g of distilled water are mixed to form a homogeneous solution, and then 3.63g of hexadecyltrimethylammonium chloride is added at room temperature at 1200rpm After stirring for 1 hour, 20 g of propyl silicate was quickly added dropwise to the above mixture, stirred at 1200 rpm for 2 hours, then heated to 60°C for 10 hours to obtain a white precipitate;

[0042] (2) The white precipitate obtained in step (1) is filtered, washed and dried at 120°C for 12 hours, then raised to 550°C at a heating rate of 2°C / min and roasted for 4 hours to remove organic components, and obtain a radial channel with a center Mesoporous silica nanospheres (DMSNs);

[0043] (3) In 200ml of Cu(NO 3 ) 2 Add 50wt% nitric acid solution to the solution to adjust the pH value to 1.0, add in step (2) t...

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Abstract

The invention discloses a preparation method of a mesoporous silica supported copper catalyst with central radial pore channels. Diethyl ether, ethanol, ammonia water and water are mixed, a long-chainstructure directing agent and an organosilicon compound are added, a reaction is performed, and silica nanospheres are obtained after filtration, washing, drying and roasting; pH of a soluble coppersalt solution is adjusted to 1-2 by an acid solution, then the silica nanospheres are added, an ammonium carbonate solution is added to adjust pH to 6-8 after stirring, a solid product is filtered, washed, dried and roasted, and a catalyst product is obtained. The content of copper in the prepared catalyst is 10%-45% of the total weight of the catalyst, and the content of monovalent copper is 20 mol%-60 mol% of the total number of active copper moles; the catalyst has specific surface area of being larger than 500 m<2> / g, pore volume being larger than 1.0 ml / g and average mesoporous size being2.8-10 nm. The catalyst is used for reaction of synthesis of ethylene glycol from dimethyl oxalate by hydrogenation, the conversion rate of dimethyl oxalate is higher than 99%, and selectivity of ethylene glycol is higher than 96%.

Description

technical field [0001] The invention relates to a method for preparing a hydrogenation catalyst, in particular to a method for preparing a silica-supported copper catalyst used for hydrogenation of dimethyl oxalate. Background technique [0002] The hydrogenation reaction of dimethyl oxalate (DMO) is the most critical step in the process of CO coupling synthesis of ethylene glycol. At the same time, in addition to the production of ethylene glycol, the hydrogenation reaction of dimethyl oxalate can also be used to produce methyl glycolate (MG) and ethanol, which are important components of the coal chemical industry chain. In 1985, UCC Corporation of the United States applied for two patents on the hydrogenation of dimethyl oxalate. The US4677234 technology mainly uses copper carbonate and ammonium carbonate as raw materials to prepare Cu-Si catalysts; US4628128 introduces a Cu-Si catalyst prepared by impregnation. catalyst. US4112245 mainly adopts co-precipitation method ...

Claims

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Application Information

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IPC IPC(8): B01J23/72C07C29/149C07C31/20
CPCB01J23/72C07C29/149C07C31/202Y02P20/52
Inventor 王志光王建青王炳春李进
Owner CHINA CATALYST HLDG CO LTD