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Low-mercury catalyst for hydrochlorination of acetylene

A low-mercury catalyst, acetylene hydrochlorination technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problem of poor stability and anti-poisoning performance, catalyst poisoning deactivation, catalyst deactivation mercury flow and other problems, to achieve the effect of enhancing anti-poisoning performance, reducing reaction and high selectivity

Active Publication Date: 2013-07-17
XINJIANG TIANYE GRP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

These several patents have adopted a relatively low content of mercuric chloride as the main active component of the catalyst, and other metal chlorides as the auxiliary active component, with activated carbon or molecular sieve as the carrier, but due to the fact that the raw material gas contains H 2 S.PH 3 impurity, causing poisoning and deactivation of the catalyst, and because acetylene has a high reducibility, it is easy to make the main active component in the catalysis Hg 2+ converted to Hg 0 , resulting in catalyst deactivation and loss of mercury flow
Thereby lead to the deactivation of catalyst, so although the catalytic activity of above-mentioned low-mercury catalyst can meet the production requirements, its stability and anti-poisoning performance are relatively poor, the life-span is shorter, fail to obtain industrial application in acetylene hydrochlorination

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] Weigh 8.65g of manganese nitrate tetrahydrate and dissolve it in 40ml of deionized water, weigh 20g of activated carbon carrier and put it into the manganese nitrate solution, soak it at 60°C for 4h; filter out the residual liquid, dry it at 105°C, and roast it under nitrogen protection atmosphere at 180°C For 3 hours, cool to room temperature under nitrogen protection; weigh 0.92g of mercuric chloride, dissolve it in 40ml of deionized water, put the carrier loaded with manganese into the mercuric chloride solution, and soak at 70°C for 4h; filter the residual liquid, 105°C Dry to obtain a low-mercury catalyst for acetylene hydrochlorination.

Embodiment 2

[0022] Weigh 7.51g of cobalt sulfate heptahydrate and dissolve it in 40ml of deionized water, weigh 20g of zeolite carrier and put it into the cobalt sulfate solution, soak it at 60°C for 4h; filter off the residual liquid, dry it at 105°C, and roast it under nitrogen protection atmosphere at 900°C After 3 hours, cool down to room temperature under the protection of nitrogen; repeat the above steps to prepare cobalt sulfate solution, soak the once-loaded carrier at 60°C for 4h, filter off the residual liquid, dry at 105°C, and roast at 900°C for 3 hours under nitrogen protection atmosphere. Cool to room temperature under protection; weigh 0.77g of mercuric chloride, dissolve it in 40ml of deionized water, put the carrier loaded with cobalt into the mercuric chloride solution, soak at 70°C for 4h; filter the residual liquid, dry at 105°C to obtain acetylene Hydrochlorination with low mercury catalysts.

Embodiment 3

[0024] Weigh 7.29g of copper nitrate trihydrate and dissolve it in 40ml of deionized water, weigh 20g of activated carbon carrier and put it into the copper nitrate solution, soak it at 60°C for 4h; filter off the residual liquid, dry it at 105°C, and roast it under nitrogen protection atmosphere at 200°C 3 hours, cooled to room temperature under the protection of nitrogen; Weigh 0.67g of mercuric chloride, dissolve it in 40ml of deionized water, put the carrier loaded with copper into the mercuric chloride solution, soak at 70°C for 4h; filter the residual liquid, 108°C Dry to obtain a low-mercury catalyst for acetylene hydrochlorination.

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PUM

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Abstract

The invention discloses a low-mercury catalyst and particularly relates to the low-mercury catalyst which is suitable for synthesizing vinyl chloride by hydrochlorination reaction of acetylene. The catalyst comprises a main active component, namely mercury chloride, auxiliary active components, namely at least one of oxides of cobalt, manganese, silver and copper and a carrier, namely activated carbon, wherein the mercury chloride accounts for 2-4% of the weight of the carrier of the catalyst, and the auxiliary active components account for 5-30% of the weight of the carrier of the catalyst in total. According to the prepared low-mercury complex catalyst disclosed by the invention, the auxiliary components are added, so that the anti-poisoning performance of the low-mercury catalyst is enhanced, the reduction of the mercury chloride during the using process is reduced, the loss of mercury is retarded, the service life of the low-mercury catalyst is significantly prolonged, and the low-mercury catalyst is the novel low-mercury catalyst with good activity, strong stability and high selectivity. The low-mercury catalyst has the advantages of simple production process, short production period and low mercury consumption.

Description

technical field [0001] The invention relates to a catalyst, in particular to a low-mercury catalyst used for acetylene hydrochlorination to synthesize vinyl chloride. Background technique [0002] Polyvinyl chloride is one of the five major synthetic resins in the world, widely used in important areas of the national economy such as industry, agriculture, and building materials. Vinyl chloride monomer is an important raw material for organic chemical synthesis. Its main purpose is to produce polyvinyl chloride resin and other vinyl chloride copolymers. With the development of social economy, its demand is increasing day by day. The sources of vinyl chloride mainly include calcium carbide acetylene method, petroleum ethylene method and dichloroethane cracking method. my country's energy structure of "short of oil, poor in gas, and rich in coal" determines that the production of polyvinyl chloride by calcium carbide acetylene has become the mainstream. Although calcium carbi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/138B01J29/00
Inventor 王小艳王小昌陈万银王伟夏锐李静张传彩庞晓东郑伟玲谢东阳谢金重周佳赵忠峰李春华李国栋
Owner XINJIANG TIANYE GRP
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