Regeneration method of hydrogenation catalyst

A hydrogenation catalyst and catalyst technology, applied in the direction of catalyst regeneration/reactivation, chemical instruments and methods, catalyst activation/preparation, etc., can solve the problems that the physical and chemical properties and structure of hydrogenation catalysts cannot meet the requirements of industrial production, and achieve Wide range of applications and the effect of reducing the amount of use

Active Publication Date: 2022-03-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] To sum up, the conventional methods of burning sulfur and carbon are adopted in the prior art, and the physical and chemical properties and structure of the regenerated hydrogenation catalyst cannot meet the requirements of industrial production.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041](1) After sampling the deactivated sulfided residue hydrogenation catalyst from the reaction device, seal it with ethanol liquid. Using a fat extractor, the above-mentioned catalyst is immersed in toluene solution, heated to a boiling state of toluene and refluxed to condense for 24 hours, after the extraction is completed, vacuum-dried to obtain deactivated catalyst A1 (in the form of deactivated hydrogenation catalyst A1 Based on the weight of the source fresh catalyst, the content of active metal molybdenum in terms of oxides is 16%; based on the weight of the source fresh catalyst of this deactivated hydrogenation catalyst, the contained deposition metal iron and vanadium, the total amount in terms of metal element content is 1.33%).

[0042] (2) After sampling and taking out the deactivated sulfurized bulk hydrofining catalyst from the reaction device, seal it with ethanol liquid. Using a fat extractor, immerse the above catalyst in toluene solution, heat to the bo...

Embodiment 2

[0048] (1) After sampling the deactivated sulfided residue hydrogenation catalyst from the reaction device, seal it with ethanol liquid. Using a fat extractor, immerse the above catalyst in toluene solution, heat to the boiling state of toluene and reflux condensation, maintain for 24 hours, after the extraction is completed, vacuum dry to obtain deactivated hydrogenation catalyst A1 (in the form of deactivated hydrogenation catalyst The source of A1 is based on the weight of the fresh catalyst, and the content of the active metal molybdenum as an oxide is 16%; based on the weight of the source of the deactivated hydrogenation catalyst, the contained deposited metal iron and vanadium are calculated as metal elements The total content is 1.33%).

[0049] (2) After sampling and taking out the deactivated sulfurized bulk hydrofining catalyst from the reaction device, seal it with ethanol liquid. Using a fat extractor, the above-mentioned catalyst is immersed in toluene solution,...

Embodiment 3

[0055] (1) After sampling the deactivated sulfided residue hydrogenation catalyst from the reaction device, seal it with ethanol liquid. Using a fat extractor, immerse the above catalyst in toluene solution, heat to the boiling state of toluene and reflux condensation, maintain for 24 hours, after the extraction is completed, vacuum dry to obtain deactivated hydrogenation catalyst A1 (in the form of deactivated hydrogenation catalyst The source of A1 is based on the weight of the fresh catalyst, and the content of the active metal molybdenum as an oxide is 16%; based on the weight of the source of the deactivated hydrogenation catalyst, the contained deposited metal iron and vanadium are calculated as metal elements The total content is 1.33%).

[0056] (2) After sampling and taking out the deactivated sulfurized bulk hydrofining catalyst from the reaction device, seal it with ethanol liquid. Using a fat extractor, the above-mentioned catalyst is immersed in toluene solution,...

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Abstract

The invention provides a regeneration method of a hydrogenation catalyst. The method comprises the following steps: (1) mixing inactivated hydrogenation catalysts A1 and A2, soaking the mixture in a solvent, and carrying out ultrasonic treatment to obtain a catalyst B and a mixed material mixed with black powder; (2) recovering the catalyst B, and filtering the mixed material mixed with the black powder to obtain powder C; (3) grinding the catalyst B into powder, screening to obtain catalyst powder D, and forming, drying and roasting to obtain a regenerated carrier; and (4) dissolving the powder C in diesel oil, dipping on a regenerated carrier, and drying to obtain the regenerated hydrogenation catalyst. According to the method, active metal components do not need to be additionally supplemented, the desulfurization performance of the regenerated catalyst is good, the dosage of a vulcanizing agent can be reduced, the vulcanizing time can be shortened, and the obtained regenerated hydrogenation catalyst has good physicochemical properties and activity.

Description

technical field [0001] The invention relates to a catalyst regeneration method, more specifically, to a method for preparing a hydrodesulfurization catalyst by regeneration of a spent catalyst. Background technique [0002] Residual oil hydrogenation technology has the characteristics of strong feedstock adaptability, simple production and operation process, etc., and can provide high-quality feedstock for downstream catalytic cracking processes. It has become one of the most important heavy oil processing technologies in modern oil refining and petrochemical industries. In particular, in recent years, the amount of residual oil hydrotreating in China has been increasing, and the demand for residual oil hydrogenation catalysts has also increased significantly. In addition, the residual oil contains high content of metals, colloids, and asphaltenes, resulting in a generally 1 to 2-year operating cycle of the residual oil hydrogenation unit, and the catalyst will not be regene...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/051B01J23/888B01J27/30B01J38/50B01J38/52B01J38/00B01J38/02B01J35/10B01J37/08B01J37/02C10G45/08
CPCB01J27/051B01J23/8885B01J23/002B01J27/30B01J38/50B01J38/52B01J38/00B01J38/02B01J35/1038B01J35/1019B01J37/0018B01J37/0207C10G45/08B01J2523/00B01J2523/31B01J2523/68B01J2523/69B01J2523/847
Inventor 关月明袁胜华王永林张成
Owner CHINA PETROLEUM & CHEM CORP
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