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Preparation method and application of hydrotalcite-like derived magnesium aluminate spinel loaded noble metal palladium catalyst

A magnesium-aluminum spinel, palladium catalyst technology, applied in metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problem of low temperature activity, high temperature stability and water resistance Problems such as poor steam capacity and uneven distribution of additives can achieve the effects of excellent low temperature activity, abundant pore channels and narrow pore size distribution.

Active Publication Date: 2021-07-09
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The catalyst involved in the present invention innovatively uses the special two-dimensional ion layer structure of magnesium-aluminum hydrotalcite, and brings its large specific surface area and uniform metal distribution into the design of the catalyst carrier, making up for the traditional impregnation. Catalyst defects (loss of specific surface, uneven distribution of additives, etc.) The interaction with the carrier solves the problems of poor low-temperature activity, high-temperature stability and water vapor resistance of traditional palladium-aluminum catalysts

Method used

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  • Preparation method and application of hydrotalcite-like derived magnesium aluminate spinel loaded noble metal palladium catalyst
  • Preparation method and application of hydrotalcite-like derived magnesium aluminate spinel loaded noble metal palladium catalyst
  • Preparation method and application of hydrotalcite-like derived magnesium aluminate spinel loaded noble metal palladium catalyst

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Experimental program
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Embodiment 1

[0038] Dissolve 39.39 g of aluminum nitrate nonahydrate (0.105 mol) in 100 ml of deionized water, stir at room temperature for 30 minutes, and record it as solution A. In a 500ml four-necked flask, 3.71g of anhydrous sodium carbonate (ie 0.035 moles) was dissolved in 100ml of deionized water, and placed in a constant temperature water bath at 35°C and stirred evenly, which was designated as solution B. Dissolve 12g of sodium hydroxide (that is, 0.3 mole) in 150ml of deionized water, and record it as solution C. Add solution A dropwise to solution B, use mechanical stirring, control the rotation speed to 800 rpm, monitor the pH value of the mixed solution in real time, and use solution C to control the pH value to be stable at 10±0.5, when the dropwise addition of solution A is completed, Stirring was stopped, and the temperature of the constant temperature water bath was raised to 70° C. and maintained, and left to age for 12 hours.

[0039] The obtained white suspension was ...

Embodiment 2

[0043] Dissolve 31.51 g of aluminum nitrate nonahydrate (ie 0.084 mol) and 5.39 g of magnesium nitrate hexahydrate (ie 0.021 mol) in 100 ml of deionized water, stir at room temperature for 30 minutes, and record it as solution A. In a 500ml four-necked flask, 3.71g of anhydrous sodium carbonate (ie 0.035 moles) was dissolved in 100ml of deionized water, and placed in a constant temperature water bath at 35°C and stirred evenly, which was designated as solution B. Dissolve 12g of sodium hydroxide (that is, 0.3 mole) in 150ml of deionized water, and record it as solution C. Add solution A dropwise to solution B, use mechanical stirring, control the rotation speed to 300 rpm, monitor the pH value of the mixed solution in real time, and use solution C to control the pH value to be stable at 10±0.5, when the dropwise addition of solution A is completed, Stirring was stopped, and the temperature of the constant temperature water bath was raised to 70° C. and maintained, and left to ...

Embodiment 3

[0048] Dissolve 29.54 g of aluminum nitrate nonahydrate (ie 0.079 mol) and 6.73 g of magnesium nitrate hexahydrate (ie 0.026 mol) in 100 ml of deionized water, stir at room temperature for 30 minutes, and record it as solution A. In a 500ml four-necked flask, 3.71g of anhydrous sodium carbonate (ie 0.035 moles) was dissolved in 100ml of deionized water, and placed in a constant temperature water bath at 35°C and stirred evenly, which was designated as solution B. Dissolve 12g of sodium hydroxide (that is, 0.3 mole) in 150ml of deionized water, and record it as solution C. Add solution A dropwise to solution B, use mechanical stirring, control the rotation speed to 60 rpm, monitor the pH value of the mixed solution in real time, and use solution C to control the pH value to be stable at 10±0.5, when the dropwise addition of solution A is completed, Stirring was stopped, and the temperature of the constant temperature water bath was raised to 70° C. and maintained, and left to a...

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Abstract

The invention relates to a preparation method and application of a hydrotalcite-like derived magnesium aluminate spinel loaded noble metal palladium catalyst. According to the method, magnesium-aluminum hydrotalcite is used as a carrier precursor, magnesium aluminate spinel with a good crystal form and a large specific surface area is obtained through thermal decomposition of the hydrotalcite, and the magnesium aluminate spinel is used as a carrier to load palladium oxide to obtain the catalyst. The special two-dimensional ionic layer structure of the magnesium-aluminum hydrotalcite is utilized, the characteristics of large specific surface area and uniform metal distribution of the magnesium-aluminum hydrotalcite are introduced into the design of the catalyst carrier, and the problems that a traditional palladium-aluminum catalyst is poor in low-temperature activity, high-temperature stability and water vapor resistance are solved.

Description

technical field [0001] The invention relates to a high-performance noble metal palladium-based catalyst for catalytic combustion of methane, a preparation method thereof, and a method for using the catalyst to catalyze the combustion reaction of methane. Background technique [0002] As an economical and clean new energy source, methane is widely used in power plants, natural gas vehicles and various chemical synthesis processes. However, the incomplete combustion of methane in the exhaust gas will cause a huge greenhouse effect. Compared with another kind of carbon dioxide gas that can also cause the greenhouse effect, its harmfulness is more than 20 times that of carbon dioxide. In order to use methane more rationally and further reduce methane emissions in the atmosphere, it is of great significance to realize the complete combustion of methane under low temperature conditions. Compared with the traditional open flame combustion method, catalytic oxidation of methane can...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/44B01J35/10B82Y30/00B82Y40/00F23G7/07
CPCB01J23/58B01J23/005F23G7/07F23G2209/14B01J35/394B01J35/23B01J35/61B01J35/64
Inventor 赵玉军宋嘉钰王胜平徐艳
Owner TIANJIN UNIV