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Hydrogen sulfide selective oxidation catalyst as well as preparation method and application thereof

An oxidation catalyst and selective technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc., can solve the problem of poor catalyst activity, low specific surface area, poor stability, etc. problem, to achieve the effect of high selectivity, enhanced activity, and good stability

Pending Publication Date: 2022-05-31
FUZHOU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The object of the present invention is to aim at MnO 2 The material also has the problems of low specific surface area and poor activity. A preparation method and application of a cerium-modified manganese dioxide catalyst are provided to solve the problem of H in the prior art. 2 S selective oxidation transition metal oxide catalysts have problems such as poor activity and poor stability, aiming to prepare cerium-manganese composite metal oxide catalysts with better activity and excellent stability

Method used

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  • Hydrogen sulfide selective oxidation catalyst as well as preparation method and application thereof
  • Hydrogen sulfide selective oxidation catalyst as well as preparation method and application thereof
  • Hydrogen sulfide selective oxidation catalyst as well as preparation method and application thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0035]Weigh 0.01 mol of potassium permanganate and 0.5 mmol of cerium nitrate hexahydrate, add them into 60 mL of deionized water, and stir at room temperature for 10 min. Then add 0.001 mol of ascorbic acid weighed into 10 mL of deionized water, and stir at room temperature for 10 min. Then add the aqueous solution of reducing precipitant to the mixed solution of potassium permanganate and cerium nitrate hexahydrate, and continue to stir at room temperature for 10 minutes. Then the solution was transferred to a 100mL autoclave for 100°C hydrothermal treatment for 24 hours. After the reaction was completed, the autoclave was naturally cooled to room temperature, the precipitate was washed and filtered with deionized water, and dried at 100°C for 12 hours. Then the cerium-modified manganese dioxide catalyst was obtained after calcination at a rate of 3°C / min to 300°C for 3 hours, named 5Ce-MnO 2 .

Embodiment 2

[0037] Weigh 0.01mol of potassium permanganate and 0.001mol of cerium nitrate hexahydrate, add them into 60mL of deionized water, and stir at room temperature for 10min. Then add 0.001 mol of ascorbic acid weighed into 10 mL of deionized water, and stir at room temperature for 10 min. Then add the aqueous solution of reducing precipitant to the mixed solution of potassium permanganate and cerium nitrate hexahydrate, and continue to stir at room temperature for 10 minutes. Then the solution was transferred to a 100mL autoclave for 100°C hydrothermal treatment for 24 hours. After the reaction was completed, the autoclave was naturally cooled to room temperature, the precipitate was washed and filtered with deionized water, and dried at 100°C for 12 hours. Then the cerium-modified manganese dioxide catalyst was obtained after roasting at 300°C at a heating rate of 3°C / min, named 10Ce-MnO 2 .

Embodiment 3

[0039] Weigh 0.01 mol of potassium permanganate and 0.005 mol of cerium nitrate hexahydrate, add them into 60 mL of deionized water, and stir at room temperature for 10 min. Then add 0.001 mol of ascorbic acid weighed into 10 mL of deionized water, and stir at room temperature for 10 min. Then add the aqueous solution of reducing precipitant to the mixed solution of potassium permanganate and cerium nitrate hexahydrate, and continue to stir at room temperature for 10 minutes. Then the solution was transferred to a 100mL autoclave for 100°C hydrothermal treatment for 24 hours. After the reaction was completed, the autoclave was naturally cooled to room temperature, the precipitate was washed and filtered with deionized water, and dried at 100°C for 12 hours. Then the cerium-modified manganese dioxide catalyst was obtained after calcination at a rate of 3°C / min to 300°C for 3 hours, named 50Ce-MnO 2 .

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Abstract

The invention belongs to the technical field of material preparation and environmental catalysis, and particularly relates to a hydrogen sulfide selective oxidation catalyst and a preparation method and application thereof. The catalyst cerium-manganese composite metal oxide (Ce-MnO2) is prepared by adding cerium salt and a reduction precipitator into KMnO4 and reacting. The method comprises the following steps: slowly adding a reduction precipitator into an aqueous solution in which potassium permanganate and cerium salt are uniformly mixed, stirring, carrying out hydrothermal treatment, separating, drying and roasting to obtain the cerium modified manganese dioxide catalyst. The cerium modified manganese dioxide catalyst prepared by the method provided by the invention is large in specific surface area, shows high H2S conversion rate and sulfur selectivity when being applied to selective catalytic oxidation reaction of H2S, and has relatively good stability.

Description

technical field [0001] The present invention relates to the preparation technology of a kind of environmental catalyst and its application field, be specifically related to the preparation method of hydrogen sulfide selective oxidation catalyst and its in H 2 Applications in the selective catalytic oxidation of S. Background technique [0002] The desulfurization process of gasoline or diesel in the petroleum industry, containing a large amount of hydrogen sulfide (H 2 S) natural gas and biogas refining process, metal melting in steel production and other processes are often accompanied by a considerable amount of H 2 S produced. With the continuous development and progress of society, people pay more and more attention to the problems of environmental pollution and resource recycling. The Claus process is used to remove H 2 S and recovery of sulfur are currently the most widely used and largest desulfurization process. However, limited by the thermodynamic equilibrium,...

Claims

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Application Information

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IPC IPC(8): B01J23/34B01J35/10B01D53/86B01D53/52
CPCB01J23/002B01J23/34B01D53/8612B01J35/638B01J35/633B01J35/635B01J35/643B01J35/647B01J35/615Y02P20/584Y02A50/20
Inventor 肖益鸿郑程程杨勤丰郑勇曹彦宁刘福建江莉龙
Owner FUZHOU UNIV