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Regeneration method of fluorination catalyst

A fluorination catalyst and catalyst technology, applied in the direction of catalyst regeneration/reactivation, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of fast decay of catalyst catalytic activity, low specific surface area of ​​fluorination catalyst, and target product selectivity Low-level problems, to achieve the effect of maintaining mechanical properties, preventing sintering, increasing specific surface area and pore volume

Active Publication Date: 2015-09-30
太仓中化环保化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This regeneration method has a better regeneration effect for most metal catalysts, but for the fluorination catalyst with the above structure, the regeneration effect is not ideal, and the activity of the regenerated catalyst can only reach 50% to 60% of the fresh catalyst
In addition, there are also problems such as the low specific surface area of ​​the fluorination catalyst, which leads to rapid decay of the catalytic activity of the catalyst and low selectivity of the target product.

Method used

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  • Regeneration method of fluorination catalyst

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Experimental program
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Effect test

Embodiment 1

[0026] Put the quantitative old fluorination catalyst into the fixed-bed reactor, and then follow the steps below to regenerate the catalyst:

[0027] (1) High-temperature purge process: heat the fluorination catalyst to 300°C, and continuously blow nitrogen gas with a pressure of 0.5MPa and a temperature of 300°C to purge the fluorination catalyst, and control the contact time between the nitrogen gas and the catalyst for 0.5 hours , the ventilation time is 30 hours;

[0028] (2) High-temperature regeneration process: After completing the high-temperature purging process, the first regeneration gas with a temperature of 300°C is continuously introduced under normal pressure. The first regeneration gas is a mixture of nitrogen and air at a mass ratio of 1:1, controlled The contact time between the first regeneration gas and the fluorination catalyst is 1 hour, and the ventilation time is 40 hours;

[0029] (3) Variable ratio regeneration process: control the temperature of th...

Embodiment 2

[0032] Put the quantitative old fluorination catalyst into the fixed-bed reactor, and then follow the steps below to regenerate the catalyst:

[0033] (1) High-temperature purge process: heat the fluorination catalyst to 300°C, and continuously blow nitrogen gas with a pressure of 0.1MPa and a temperature of 300°C to purge the fluorination catalyst, and control the contact time between the nitrogen gas and the catalyst for 0.5 hours , the ventilation time is 30 hours;

[0034] (2) High-temperature regeneration process: After completing the high-temperature purging process, the first regeneration gas with a temperature of 300°C is continuously introduced under normal pressure. The first regeneration gas is a mixture of nitrogen and air at a mass ratio of 1:1, controlled The contact time between the first regeneration gas and the fluorination catalyst is 0.5 hours, and the ventilation time is 20 hours;

[0035](3) Variable ratio regeneration process: control the temperature of ...

Embodiment 3

[0038] Put the quantitative old fluorination catalyst into the fixed-bed reactor, and then follow the steps below to regenerate the catalyst:

[0039] (1) High-temperature purge process: heat the fluorination catalyst to 200°C, and continuously blow in nitrogen gas with a pressure of 0.1MPa and a temperature of 200°C to purge the fluorination catalyst, and control the contact time between the nitrogen gas and the catalyst for 15 minutes , the ventilation time is 30 hours;

[0040] (2) High-temperature regeneration process: After completing the high-temperature purge process, the first regeneration gas with a temperature of 200°C is continuously introduced under normal pressure. The first regeneration gas is composed of nitrogen and air at a mass ratio of 1:1, and the The contact time of the first regeneration gas and the fluorination catalyst is 15 minutes, and the ventilation time is 10 hours;

[0041] (3) Variable ratio regeneration process: control the temperature of the f...

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Abstract

The invention relates to a fluorination catalyst regeneration method which comprises a high-temperature purging process, a high-temperature regenerating process, a ratio of transformation generating process and a high-pressure generating process, wherein the high-temperature purging process is that a high-temperature catalyst is purged through high-temperature nitrogen; the high-temperature regenerating process is that the catalyst is regenerated through a mixed gas containing less gas capable of reacting with carbon; the ratio of transformation generating process is that the content of reaction gas in the mixed gas is constantly increased to regenerate the catalyst; the high-pressure generating process is that the mixed gas regenerates the catalyst under the condition that the environment stress of a regeneration system is constantly increased. The method can enable the activity of the catalyst to recover to initial activity.

Description

technical field [0001] The invention relates to a regeneration method of a fluorination catalyst used in the preparation process of fluoroalkane. Background technique [0002] 1,1,1,2-tetrafluoroethane (HFC-134a) and pentafluoroethane (HFC-125) are ODS (ozone-depleting substances) substitutes and are new green refrigerants. 1,1,1,2-Tetrafluoroethane (HFC-134a) and pentafluoroethane (HFC-125) can be catalyzed by HF and halogenated olefins under the catalysis of a solid catalyst at a certain temperature, pressure and contact time prepared by reacting under conditions. Chinese invention patent ZL01141970.9 discloses a fluorination catalyst that can be used for the preparation of 1,1,1,2-tetrafluoroethane. The structure formula of the fluorination catalyst is CrX 0.005-0.5 Y 0.005-0.3 o 0.1-1.0 f 1.0-3.0 , where X is Mn, Co or Zn, and Y is Mg or Ni. The catalyst has the advantages of high activity, good stability and long service life. However, due to high-temperature car...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/32B01J27/138B01J38/04B01J38/12C07C19/08C07C17/20
CPCY02P20/584
Inventor 鲜毅张广青李雪莲杨明波李顺黄健康肖立盛
Owner 太仓中化环保化工有限公司