Preparation method of high-specific-surface CuMn2O4 catalyst for CO low-temperature oxidation removal

A technology of high specific surface area and catalyst, applied in the direction of metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, chemical instrument and method, etc. Chemical industry production, problems affecting catalyst activity and stability, etc., to achieve the effect of low cost, short time consumption and convenient operation

Inactive Publication Date: 2016-10-19
HENAN NORMAL UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The main problem at present is that the copper-manganese composite oxides prepared by traditional impregnation and co-precipitation methods are difficult to ensure the full mixing of multiple components, except for spinel CuMn 2 o 4 In addition, it is easy to generate CuO or MnO x The crystal phase seriously affects the activity and stability of the catalyst; a single spinel CuMn can be obtained by using sol-gel technology 2 o 4 phase, but the prepared CuMn 2 o 4 The specific area of ​​the catalyst is relatively low (≤50m 2 / g), it is difficult to meet the demand for high catalytic activity in practical applications
However, the disadvantage of this method is that the manufacturing equipment and operation are relatively complicated, and it is difficult to realize large-scale industrial production.

Method used

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  • Preparation method of high-specific-surface CuMn2O4 catalyst for CO low-temperature oxidation removal

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] Weigh 10mmol of copper acetate and 20mmol of manganese acetate and dissolve them in 100mL of deionized water to prepare a mixed solution with a total molar concentration of about 0.3mol / L, and quickly add 100mL of the solution with a molar concentration of 0.3mol / L under the conditions of ultrasonic assistance and strong stirring. L ammonium oxalate solution, gradually a light blue precipitate formed. Wherein the ultrasonic power is 50W, and the rotational speed of the stirrer is 800r / min. After continuing to stir for 40 min, the precipitate was filtered and washed three times with absolute ethanol, and then dried at 60° C. for 24 h to obtain a copper manganese oxalate precursor. Then the CuMn oxalate precursor was ground and then heated to 300 °C in the air for 2 h (heating rate 1 °C / min), and finally the spinel CuMn 2 o 4 Catalyst (if attached figure 1 shown), its specific surface area is 109m 2 / g.

[0016] The catalyst needs to be made into 40-60 mesh particles...

Embodiment 2

[0020] Weigh 10mmol of copper nitrate and 20mmol of manganese nitrate and dissolve them in 100mL of deionized water to prepare a mixed salt solution with a total molar concentration of about 0.3mol / L. Under the conditions of ultrasonic assistance and strong stirring, quickly add 60mL of / L of ammonium oxalate solution, a light blue precipitate gradually formed. Wherein the ultrasonic power is 80W, and the rotational speed of the stirrer is 1200r / min. After continuing to stir for 60 min, the precipitate was filtered and washed three times with absolute ethanol, and then dried at 80° C. for 12 h to obtain a copper manganese oxalate precursor. Then the CuMn oxalate precursor was ground and then heated to 400 °C in air for 1 h (heating rate was 2 °C / min), and finally the spinel CuMn 2 o 4 Catalyst with a specific surface area of ​​100m 2 / g.

[0021]Catalyst treatment and activity evaluation methods are the same as in Example 1, but the CO content in the feed gas is 2000ppm, a...

Embodiment 3

[0023] Weigh 14mmol of copper acetate and 28mmol of manganese acetate and dissolve them in 100mL of deionized water to prepare a mixed solution with a total molar concentration of about 0.42mol / L. Under the conditions of ultrasonic assistance and strong stirring, 140mL of L ammonium oxalate solution, gradually a light blue precipitate formed. Wherein the ultrasonic power is 70W, and the rotational speed of the stirrer is 900r / min. After continuing to stir for 45 min, the precipitate was filtered and washed three times with absolute ethanol, and then dried at 70° C. for 20 h to obtain a copper manganese oxalate precursor. Then the copper manganese oxalate precursor was ground and then heated to 350 °C in air and roasted for 3 h (heating rate was 0.5 °C / min) to obtain spinel CuMn 2 o 4 Catalyst with a specific surface area of ​​104m 2 / g.

[0024] Catalyst treatment and activity evaluation methods are the same as in Example 1, but the content of CO in the feed gas is 500ppm,...

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Abstract

The invention discloses a preparation method of a high-specific-surface CuMn2O4 catalyst for CO low-temperature oxidation removal. The method comprises the steps that soluble copper salt and soluble manganese salt with the mole ratio being 1:2 are prepared into a solution with the total mole concentration of 0.21-0.45 mol/L, then, an ammonium oxalate solution with the mole concentration of 0.3-0.5 mol/L is added, the mixture continues to be stirred and is dried at the temperature of 60-90 DEG C after being precipitated and washed to obtain a copper manganese oxalate precursor, and the copper manganese oxalate precursor is heated at the heating speed of 0.5-2 DEG C/min to 300-400 DEG C to be roasted for 0.5-3 h to obtain the spinel type CuMn2O4 catalyst. The prepared CuMn2O4 catalyst has the advantages of being large in specific surface, simple in preparation process, convenient to operate, good in repeatability and the like, can achieve oxidization removal of CO in air within the wide temperature range, and has the quite good stability.

Description

technical field [0001] The invention belongs to the technical field of heterogeneous catalysis, and in particular relates to a high specific surface CuMn used for low-temperature oxidation and elimination of CO 2 o 4 Catalyst preparation method. Background technique [0002] Carbon monoxide (CO) oxidative elimination is a widely used reaction in practice, involving many aspects such as industry, environmental protection, military affairs and human life, such as: gas purification in CO lasers, CO gas detector materials, gas purification for breathing Devices, tobacco harm reduction, closed systems (such as aircraft, submarines, spacecraft, etc.) and the elimination of trace CO in automobile exhaust, etc. Among them, the low-temperature catalytic oxidation method is the simplest, cheapest, most direct and most effective method to eliminate CO. At present, the industry mainly uses noble metal catalysts (such as Pd, Pt, Au, etc.) with high catalytic activity, good heat resist...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/889B01J35/10
CPCB01J23/005B01J23/8892B01J35/1019
Inventor 汤清虎谢小培赵培正
Owner HENAN NORMAL UNIV
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