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A kind of copper-based catalyst for hydrogenation of oxalate to ethylene glycol and preparation method thereof

A technology of copper-based catalyst and oxalate ester, which is applied in the field of catalysis, can solve the problems of poor catalyst stability and achieve the effects of improving low-temperature activity, large-scale industrial application prospects, and high operation reproducibility

Active Publication Date: 2021-12-14
FUJIAN INST OF RES ON THE STRUCTURE OF MATTER CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The purpose of the present invention is to provide a copper-based catalyst for hydrogenation of oxalate to ethylene glycol and a preparation method thereof to solve the problems of poor catalyst stability in the prior art

Method used

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  • A kind of copper-based catalyst for hydrogenation of oxalate to ethylene glycol and preparation method thereof
  • A kind of copper-based catalyst for hydrogenation of oxalate to ethylene glycol and preparation method thereof
  • A kind of copper-based catalyst for hydrogenation of oxalate to ethylene glycol and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0026] A. The silica gel carrier used is the B-type silica carrier of Qingdao Ocean Chemical Co., Ltd., which is commercially available, and its specific surface area is 300m 2 / g, with an average pore size of 12nm and a particle size of 1.5-2.5cm, soak in 1mol / L ammonia water for one week, filter and dry at 120°C for 24h in a drying oven to obtain a pretreated silica carrier;

[0027] B. Dissolve 6g of copper acetate in 30mL of deionized water, stir at 60°C until the copper acetate is completely dissolved, then add 30mL of 28% concentrated ammonia water, and continue stirring for 0.5h to obtain a copper ammonia solution; put 4g of pretreated silica carrier in After drying at 160°C for 2 hours, immerse in cuproammonia solution, and after immersing at 60°C for 24 hours, filter and wash for 3-4 times to obtain the catalyst precursor;

[0028]C. Adding 7.2g of silica sol with a mass fraction of 20% in 120mL deionized water is made into a silica sol solution with a concentration o...

Embodiment 2

[0032] A. With embodiment 1.

[0033] B. Dissolve 9g of copper acetate in 30mL of deionized water, stir at 30°C until the copper acetate is completely dissolved, then add 40mL of 28% concentrated ammonia water, and continue stirring for 0.5h to obtain a copper ammonia solution; put 4g of pretreated silica carrier in After drying at 180°C for 1 hour, immerse in cuproammonia solution, and after immersing at 80°C for 12 hours, filter and wash for 3-4 times to obtain the catalyst precursor;

[0034] C. Adding 7.2g of silica sol with a mass fraction of 20% in 120mL deionized water is made into a silica sol solution with a concentration of 0.2mol / L, and stirring makes the two evenly mixed; the catalyst precursor obtained in step B is immersed in the silica sol In the solution, after stirring at 60°C for 24h, the temperature was raised to 90°C for ammonia distillation for 1h; the mixture was transferred to a hydrothermal kettle, and the temperature was raised to 200°C for hydrotherma...

Embodiment 3

[0038] A. The silica gel carrier used is the B-type silica carrier of Qingdao Ocean Chemical Co., Ltd., which is commercially available, and its specific surface area is 350m 2 / g, with an average pore diameter of 14nm and a particle size of 2-3cm, soaked in 2mol / L ammonia water for one week, filtered and dried in a drying oven at 150°C for 12h to obtain a pretreated silica carrier;

[0039] B. Dissolve 12g of copper acetate in 30mL of deionized water, stir at 40°C until the copper acetate is completely dissolved, then add 40mL of 28% concentrated ammonia water, and continue stirring for 0.5h to obtain a copper ammonia solution; put 4g of pretreated silica carrier in After drying at 150°C for 3 hours, immerse in cuproammonia solution, after immersing at 40°C for 36h, filter and wash 3-4 times to obtain the catalyst precursor;

[0040] C. Adding 14.4g of silica sol with a mass fraction of 20% in 120mL deionized water is made into a silica sol solution with a concentration of 0....

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Abstract

The invention provides a copper-based catalyst for hydrogenating oxalate to ethylene glycol and a preparation method thereof. The chemical representation of the catalyst is: Cu‑SiO 2 @SiO 2 , where Cu‑SiO 2 As the active component of the catalyst, SiO 2 It is a carrier; copper accounts for 5-20 wt% of the mass percentage of the catalyst, and the rest is silicon dioxide. The catalyst adopts the copper in the catalyst precursor obtained by the ion exchange method to be Si-O-Cu(NH 3 ) 2 , [Cu(NH 3 ) 2 ] 2+ , [Cu(NH 3 ) 4 ] 2+ Adding a small amount of silica sol forms a protective layer on the surface of the catalyst precursor, which can effectively enhance the interaction between the active component copper and the carrier, prevent the agglomeration of copper particles during calcination and reaction, and improve the activity and stability of the catalyst. . The copper-based catalyst is applied in the reaction of oxalate hydrogenation to prepare ethylene glycol. At a lower reaction temperature, the selectivity of ethylene glycol can reach 97%, and the catalyst activity remains unchanged for 500 hours of continuous reaction.

Description

technical field [0001] The invention belongs to the technical field of catalysis, and in particular relates to a high-temperature-resistant copper-based catalyst obtained by ion exchange-silica sol coating-ammonia steaming hydrothermal method and a preparation method thereof, in particular to a catalyst used in the hydrogenation of oxalate ester to ethylene glycol and its preparation method. Background technique [0002] Ethylene glycol is an important basic raw material and chemical intermediate, mainly used in the synthesis of polyester resin and fiber, and also commonly used as solvent, antifreeze, lubricant, plasticizer, surfactant, etc. At present, the annual demand for ethylene glycol exceeds 20 million tons, and about half of the market demand is in China. Due to its unique properties and wide application value, people have been devoting themselves to the development of efficient methods for the synthesis of ethylene glycol in recent years. Among them, coal-to-ethyl...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/72B01J35/10B01J37/30B01J37/10B01J37/02C07C29/149C07C31/20
CPCB01J23/72B01J37/30B01J37/10B01J37/0215B01J37/0201C07C29/149B01J35/23B01J35/647B01J35/615C07C31/202Y02P20/52
Inventor 姚元根杨锦霞林凌孙明玲李斐陈冲冲黄隆朱凌斌
Owner FUJIAN INST OF RES ON THE STRUCTURE OF MATTER CHINESE ACAD OF SCI