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Silver catalyst for producing ethylene oxide by ethylene epoxidation and its preparation method and application

An ethylene epoxidation, silver catalyst technology, applied in metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, bulk chemical production, etc., can solve the problem of uneven particle size distribution of active components, etc. problems, to achieve high catalytic activity and selectivity, improved stability, and uniform distribution.

Active Publication Date: 2022-05-24
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The purpose of the present invention is to provide a silver catalyst for the production of ethylene oxide by ethylene epoxidation and a preparation method thereof to further improve the activity, selectivity and sex and stability

Method used

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  • Silver catalyst for producing ethylene oxide by ethylene epoxidation and its preparation method and application
  • Silver catalyst for producing ethylene oxide by ethylene epoxidation and its preparation method and application
  • Silver catalyst for producing ethylene oxide by ethylene epoxidation and its preparation method and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0057] Dissolve 200g of pyridine and 1000g of 1,4-butanediamine in 1500g of deionized water, slowly add silver oxalate to the mixture under stirring, and keep the temperature below 30°C. Contains 24% silver by weight. After the silver amine solution is prepared, keep the existing temperature, add 15.0g of cesium sulfate, 2.8g of calcium nitrate, 1.4g of ammonium perrhenate and 0.5g of cerium sulfate, then add 200g of citric acid, and finally add deionized Water makes the total mass of the solution reach 5000g, and is prepared into an impregnating solution for use.

[0058] Take 2500g of carrier sample and put it into a container, vacuumize to a degree of vacuum lower than 10mmHg, put the above impregnating liquid into it, immerse the carrier, keep it for 30 minutes, and then remove the excess impregnating liquid by leaching. The above-mentioned solid was dried at 100°C for 8 hours, heated in an air flow at 400°C for 20 minutes, and cooled to prepare a silver catalyst for ethy...

Embodiment 2

[0060] Dissolve 500g of ethylenediamine and 800g of 1,3-propanediamine in 1500g of deionized water, slowly add silver nitrate to the mixture under stirring, and keep the temperature below 30°C. The immersion solution contains 20% silver by weight. After the silver amine solution is prepared, keep the existing temperature, add 5.0g of cesium sulfate, 12.8g of barium acetate, 5.4g of perrhenic acid and 2.0g of cerium sulfate, then add 50g of acetic acid, and finally add deionized water to make the solution. The total mass of the solution reaches 5000g, which is prepared into an impregnating liquid and is ready for use.

[0061] Take 2500g of the carrier sample and put it into the container, vacuumize until the vacuum degree is lower than 10mmHg, put the above dipping solution into it, immerse the carrier, keep it for 60 minutes, and then remove the excess dipping solution by leaching. The above-mentioned solid was dried at 150°C for 3 hours, heated in an air flow of 500°C for 1...

Embodiment 3

[0063] Dissolve 500g of ethylenediamine and 800g of 1,3-propanediamine in 1500g of deionized water, slowly add silver nitrate to the mixture under stirring, and keep the temperature below 30°C. The immersion solution contains 20% silver by weight. After the silver amine solution is prepared, keep the existing temperature, add 5.0g of cesium sulfate, 12.8g of barium acetate, 5.4g of perrhenic acid and 2.0g of cerium sulfate, then add 600g of malic acid, and finally add deionized water. Make the total mass of the solution reach 5000g, prepare the dipping solution, and stand by.

[0064] Take 2500g of carrier sample and put it into the container, vacuum to the degree of vacuum lower than 10mmHg, put the above impregnating liquid into it, immerse the carrier, keep it for 90 minutes and then remove the excess impregnating liquid by leaching. The above-mentioned solid was dried at 60°C for 24 hours, heated in an air flow at 200°C for 60 minutes, and cooled to prepare a silver catal...

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Abstract

The invention belongs to the field of catalysts, and relates to a silver catalyst for ethylene oxide production of ethylene oxide, a preparation method and application thereof. The silver catalyst comprises a carrier and silver loaded thereon and optional additives, the average particle diameter of the silver particles in the silver catalyst is 80-120nm, and the silver particles within the average particle diameter ± 20% range account for all silver particles. More than 80% of the particles, and the silver particles whose particle size is within the range of the average particle size ± 10% account for more than 50% of all silver particles. Compared with the prior art, the silver catalyst provided by the invention has higher catalytic activity and selectivity and significantly improved stability for the reaction of ethylene oxidation to produce ethylene oxide.

Description

technical field [0001] The invention belongs to the field of catalysts, and more particularly, relates to a silver catalyst for producing ethylene oxide by epoxidizing ethylene and a preparation method and application thereof. Background technique [0002] The epoxidation of ethylene under the action of silver catalyst mainly produces ethylene oxide (EO), and at the same time a side reaction occurs to generate carbon dioxide and water. Among them, activity, selectivity and stability are the main performance indicators of silver catalyst. Activity refers to the reaction temperature required when the ethylene oxide production process reaches a certain reaction load. The lower the reaction temperature, the higher the activity of the catalyst; the selectivity refers to the number of moles of ethylene converted into ethylene oxide and the amount of ethylene in the reaction. The ratio of the total reaction moles; the stability is expressed as the decline rate of activity and selec...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/50B01J23/68B01J35/02C07D301/10C07D303/04B01J35/00
CPCB01J23/50B01J23/688C07D301/10C07D303/04B01J35/40Y02P20/52
Inventor 韩红苓孙欣欣任冬梅李金兵林强王淑娟代武军汤之强魏会娟
Owner CHINA PETROLEUM & CHEM CORP