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Regeneration method of metal catalyst

A metal catalyst and catalyst technology, applied in the direction of catalyst regeneration/reactivation, metal/metal oxide/metal hydroxide catalyst, chemical instruments and methods, etc., can solve the problem of sintering, extraction and pickling without changing catalyst particles Unsatisfactory effects and other problems, to achieve the effect of improving surface utilization, easy industrial production, and simple operation

Active Publication Date: 2016-03-23
CHANGCHUN INST OF APPLIED CHEMISTRY - CHINESE ACAD OF SCI
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The regeneration method adopted in the early stage is to use solvent (such as acetone, cyclohexane and other organic solvents) extraction method (such as Ind.Eng.Chem.Res.1998,37,882-886, etc.), and use the method of oxidizing acid to wash the catalyst to remove the catalyst Surface deposits (such as Environ.Sci.Technol.2006, 40, 2030-2036, etc.), due to the unsatisfactory effect of extraction and pickling methods, researchers use reducing gas high-temperature reduction method and oxidizing gas high-temperature oxidation method (such as Appl.Catal.B, Environ.1997, 13, 265-274; CN201180047091, etc.)
However, these treatment methods can only change the catalyst surface deposits, and do not change the problems such as sintering of catalyst particles.

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0026] Weigh 100 mg of sintered deactivated carbon-supported iron catalyst, 500 mg of urea, grind them evenly with a mortar, put the evenly ground mixture in a quartz boat, place it in a tube furnace, use nitrogen as a protective gas, and calcinate at 900 ° C for 1 hours, the regenerated catalyst is obtained. Scanning electron microscope test such as figure 2 . figure 1 It is a scanning electron microscope test picture of a carbon-supported iron catalyst deactivated by sintering. It can be seen that the particle size of its iron particles is mainly distributed at about 0.6 microns; figure 2 It can be seen that the particle size of the regenerated iron particles is mainly distributed at about 25 nanometers. After the regeneration treatment, the particles are redispersed, and the particle size is one-twentieth of the original particle size.

Embodiment 2

[0028] Weigh 100 mg of sintered deactivated carbon-supported palladium catalyst and 500 mg of urea, grind them evenly with a mortar, put the evenly ground mixture in a quartz boat, place it in a tube furnace, use nitrogen as a protective gas, and calcinate at 350 ° C for 5 hours, the regenerated catalyst is obtained. The obtained regenerated catalysts were subjected to electrochemical tests, such as image 3 Shown by the dotted line.

[0029] Sintering deactivated palladium carbon catalysts for electrochemical tests, such as image 3 shown by the solid line.

[0030] image 3 Among them, the solid line is the cyclic voltammetry curve of the deactivated palladium-carbon catalyst, and the dotted line is the cyclic voltammetry curve of the regenerated palladium-carbon catalyst, from image 3 It can be seen that the dotted line of the oxidation peak current of formic acid is significantly larger than the solid line, indicating that the regeneration method of the present invent...

Embodiment 3

[0032] Weigh 100mg of sintered deactivated carbon-supported platinum catalyst, 1000mg of urea, grind them evenly with a mortar, put the evenly ground mixture in a quartz boat, place it in a tube furnace, use nitrogen as a protective gas, and calcinate at 300°C for 2 hours, the regenerated catalyst is obtained. The metal particles of the regenerated catalyst are less dispersed, and the activity can be greatly improved.

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Abstract

The invention relates to a regeneration method of a metal catalyst, and belongs to the technical field of regeneration of deactivated catalyst. The regeneration method comprises the following steps: evenly mixing a deactivated catalyst with a nitrogen-containing compound, which can be degraded into nitrogen-containing gas at a high temperature; then placing the obtained mixture into a tubular furnace, and burning the mixture at a high temperature under the protection of inert gas so as to obtain the regenerated metal catalyst. The used nitrogen-containing compound can be degraded into nitrogen-containing gas at a high temperature, the nitrogen-containing gas can interact with metal particles so as to disperse metal particles and reduce the particle size of metal particles, thus the surface utilization rate of metal is improved; the used nitrogen-containing compound is degraded into gas at a high temperature, no other impurity is introduced; furthermore, the operation is simple, the method can be easily applied to the industrial production; and the method can effectively regenerate deactivated catalyst to obtain regenerated catalyst with recovered activity.

Description

technical field [0001] The invention relates to the technical field of deactivated catalyst regeneration, in particular to a metal catalyst regeneration method. Background technique [0002] The activity and selectivity of the catalyst will gradually decrease during the use process, and even the use value of the catalyst will be lost. This is the deactivation process of the catalyst. Catalyst deactivation is a complex physical and chemical process, and deactivation is usually divided into three types: catalyst deactivation such as carbon deposition, catalyst poisoning deactivation, catalyst thermal deactivation and sintering deactivation. Catalyst regeneration refers to an operation means and method in which the activity and selectivity of the catalyst drop to a certain extent after use, and the activity and selectivity of the catalyst can be recovered through appropriate treatment. It is to prolong the service life of the catalyst and reduce the production cost. an importa...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/90B01J23/94B01J23/96B01J38/02B01J38/04
CPCB01J23/90B01J23/94B01J23/96B01J38/02B01J38/04B01J2523/17B01J2523/18B01J2523/19B01J2523/821B01J2523/824B01J2523/828B01J2523/842B01J2523/845B01J2523/847
Inventor 徐维林阮明波刘京宋平李二岭
Owner CHANGCHUN INST OF APPLIED CHEMISTRY - CHINESE ACAD OF SCI
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