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A kind of mixed silicon source method synthetic oxalate hydrogenation catalyst and preparation method thereof

A hydrogenation catalyst and mixed silicon source method technology, applied in the chemical industry, can solve problems such as environmental pollution in catalyst production, and achieve the effects of enhancing sintering resistance, improving the environment, and increasing hydrogenation activity and selectivity.

Active Publication Date: 2017-01-11
河南能源集团研究总院有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0009] The technical problem to be solved by the present invention is that the ammonia water and urea used in the preparation process of the dimethyl oxalate hydrogenation catalyst will generate a large amount of ammonia gas, which brings certain pollution to the production environment of the catalyst, and provides a kind of catalyst with high activity and high Catalyst for selective and long-life oxalate hydrogenation to ethylene glycol, preparation method and application thereof

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  • A kind of mixed silicon source method synthetic oxalate hydrogenation catalyst and preparation method thereof

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Effect test

Embodiment 1

[0028] The preparation method of the oxalate hydrogenation catalyst synthesized by the mixed silicon source method of the present embodiment is as follows:

[0029] Based on 100g of catalyst, according to 32%CuO, 1%B 2 o 3 , 67%SiO2 2Weigh 96.64g of copper nitrate trihydrate and 1.78g of boric acid into 1200mL of water, heat and stir until the solids are completely dissolved, add 134g of 25% silica sol (pH 1) acidified by nitric acid into the prepared solution drop by drop, and forcefully Stir for 7h, then drop an aqueous solution containing 68.12g of sodium silicate into the mixing system, wherein the ratio of silica sol and sodium silicate is 1:1 (based on SiO 2 After stirring for 2 hours, it was crystallized in a 130°C hydrothermal kettle for 12 hours. The obtained solid-liquid mixture was washed by centrifugation, washing with alcohol, and then dried at 120°C. After calcination at 450°C for 6 hours, the catalyst was prepared. use.

[0030] Catalyst evaluation: The prep...

Embodiment 2

[0032] The preparation method of the oxalate hydrogenation catalyst synthesized by the mixed silicon source method of the present embodiment is as follows:

[0033] Based on 100g catalyst, according to 20%CuO, 0.5%ZnO, 79.5%SiO 2 Take 60.4g of copper nitrate trihydrate and 1.83g of zinc nitrate hexahydrate into 2500mL of water, the concentration of copper salt is 0.1mol / L, stir until all the solids are dissolved, and acidify 212g of silica sol with a content of 25% in nitric acid (pH 2 ) was added dropwise to the prepared solution, and stirred vigorously for 1h, then the aqueous solution containing 53.89g of sodium silicate was dropped into the mixing system, wherein the ratio of silica sol and sodium silicate was 2:1 (based on SiO 2 After stirring for 2 hours, it was crystallized in a 110°C hydrothermal kettle for 20 hours, and the obtained solid-liquid mixture was washed with centrifugal water and alcohol in turn, and then dried at 100°C. After calcination at 450°C for 6 hou...

Embodiment 3

[0036] The preparation method of the oxalate hydrogenation catalyst synthesized by the mixed silicon source method of the present embodiment is as follows:

[0037] Based on 100g of catalyst, according to 20%CuO, 0.1%Al 2 o 3 , 79.9% SiO 2 Take 60.4g of copper nitrate trihydrate and 0.37g of aluminum nitrate nonahydrate into 167mL of water, the concentration of copper salt is 1.5mol / L, stir until all the solids are dissolved, and acidify 106.53g of silica sol with a content of 25% in nitric acid (pH is 2) Add dropwise to the prepared solution and stir vigorously for 6 hours, then drop the aqueous solution containing 108.3g of sodium silicate into the mixing system, wherein the ratio of silica sol and sodium silicate is 1:2 (based on SiO 2 After stirring for 4 hours, it was crystallized in a 120°C hydrothermal kettle for 15 hours. The obtained solid-liquid mixture was washed with centrifugal water and alcohol in turn, and then dried at 90°C. After calcination at 450°C for 6 h...

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Abstract

An oxalate hydrogenation catalyst synthesized by a mixed silicon source method and a preparation method thereof are provided. The invention discloses the catalyst for oxalate hydrogenation preparation of ethylene glycol and the preparation method thereof, wherein the catalyst is a CuO-MxOy-SiO2 system and is prepared by the mixed silicon source method; silicon dioxide is added in forms of silica sol and sodium silicate in order, sodium silicate is used not only as a silicon source but also simultaneously as a precipitator, a stable chemical structure is formed among hydroxyl generated from hydrolysis of silica sol and sodium silicate, copper and an auxiliary agent, at the same time, the hydrogenation activity and selectivity of the catalyst are enhanced by utilizing a synergistic effect between the two silicon sources, and besides, the anti-sintering ability of the copper catalyst is also enhanced. The catalyst has relatively high activity and selectivity for the reaction of oxalate hydrogenation preparation of ethylene glycol, the conversion rate of oxalate is more than 99%, and the selectivity of ethylene glycol is more than 95%.

Description

technical field [0001] The invention belongs to the technical field of chemical industry, and in particular relates to a catalyst used in the hydrogenation of oxalate ester to prepare ethylene glycol and a preparation method thereof. Background technique [0002] Ethylene glycol is an important chemical raw material. It reacts with terephthalic acid to produce polyethylene terephthalate, which can be used as a raw material for polyester fibers and polyester plastics. It is also widely used in the production of lubricants, Plasticizers, paints, adhesives, surfactants, explosives and other industrial fields, but also can be used to configure antifreeze or directly as an organic solvent. In addition, it can also be used in industries such as paint, photographic developer, brake fluid and ink. [0003] At present, the industrial production of ethylene glycol mainly adopts the route of producing ethylene oxide through gas-phase oxidation of petroleum ethylene, and then through l...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/72B01J23/80B01J23/889B01J23/83B01J23/825B01J23/745C07C29/149C07C31/20
CPCY02P20/52
Inventor 闫捷赵立红李丰穆仕芳张鲁湘尚如静蒋元力魏灵朝
Owner 河南能源集团研究总院有限公司