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Aluminum oxide loaded manganese-nickel catalyst with no exhaust gas nitric oxide and preparation application

An alumina supported, nitrogen oxide technology, applied in metal/metal oxide/metal hydroxide catalysts, catalyst activation/preparation, physical/chemical process catalysts, etc., can solve the problem of poor resistance to water and sulfur dioxide poisoning, low temperature problems such as low activity, to achieve good industrial application potential, reduce reaction gas resistance, and improve the effect of application scope

Inactive Publication Date: 2019-09-27
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The technical problem to be solved by the present invention is: how to solve the common problems of low low temperature activity and poor resistance to water and sulfur dioxide poisoning in current low temperature denitrification catalysts

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0012] Dissolve 0.1 mol aluminum isopropoxide in 100 mL of absolute ethanol, then add 16 mL of 68% wt.% nitric acid, stir vigorously at 25°C for 5 h to obtain solution A; take 10 g of P123 and dissolve in 100 mL of Water and ethanol, stirred vigorously at 25°C for 5 h to obtain solution B; slowly added solution B to solution A, continued vigorously stirring at 25°C for 4 h, transferred the mixed solution to a blast drying oven at 60°C for crystallization After aging for 48 h, the bright yellow solid was transferred to a muffle furnace for calcination in the air atmosphere, and the temperature was raised to 400 °C at a slow heating rate of 1 °C / min and kept at a constant temperature for 6 h to obtain ordered mesoporous alumina; take 5 g The prepared OMA carrier was dispersed in 100mL Mn(NO 3 ) 2 and Ni(NO 3 ) 2 In the mixed solution (wherein Mn(NO 3 ) 2 The amount of the substance is 3.08 mmol, and the Ni / Mn molar ratio is 0.4), then a 70°C water bath and slow stirring unt...

Embodiment 2

[0014] Dissolve 0.1 mol aluminum isopropoxide in 100 mL of absolute ethanol, then add 14 mL of 68% wt.% nitric acid, stir vigorously at 25°C for 5 h to obtain solution A; dissolve 8 g of P123 in 100 mL With absolute ethanol, stir vigorously at 25°C for 5 h to obtain solution B; slowly add solution B to solution A, continue vigorously stirring at 25°C for 4 h, and transfer the mixed solution to a blast drying oven at 60°C After crystallization and aging for 48 h, the bright yellow solid obtained was transferred to a muffle furnace for calcination in an air atmosphere, and the temperature was raised to 400 °C at a slow heating rate of 1 °C / min, and then raised to 600 °C at a rate of 5 °C / min and kept at a constant temperature for 6 h, to obtain ordered mesoporous alumina; take 5g of the prepared OMA carrier, and use initial wet impregnation to disperse it in 100mL Mn(NO 3 ) 2 and Ni(NO 3 ) 2 In the mixed solution (wherein Mn(NO 3 ) 2 The amount of the substance is 5.16 mmol...

Embodiment 3

[0016] Dissolve 0.1 mol aluminum isopropoxide in 100 mL of absolute ethanol, then add 15 mL of 68% wt.% nitric acid, stir vigorously at 25°C for 5 h to obtain solution A; dissolve 9 g of P123 in 100 mL With absolute ethanol, stir vigorously at 25°C for 5 h to obtain solution B; slowly add solution B to solution A, continue vigorously stirring at 25°C for 4 h, and transfer the mixed solution to a blast drying oven at 60°C After crystallization and aging for 48 h, the bright yellow solid was transferred to a muffle furnace for calcination in an air atmosphere. The temperature was raised to 400 °C at a slow heating rate of 1 °C / min, and then raised to 800 °C at a rate of 5 °C / min and kept at a constant temperature for 4 h, to obtain ordered mesoporous alumina; take 5g of the prepared OMA carrier, and use initial wet impregnation to disperse it in 100mL Mn(NO 3 ) 2 and Ni(NO 3 ) 2 In the mixed solution (wherein Mn(NO 3 ) 2 The amount of the substance is 6.64 mmol, and the Ni / ...

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PUM

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Abstract

The invention belongs to the technical field of exhaust gas treatment, and particularly relates to an aluminum oxide loaded manganese-nickel catalyst with no exhaust gas nitric oxide. Ordered mesoporous alumina is adopted as a carrier loaded active component, the active components are manganese dioxide and nickel oxide, the molar ratio of the nickel element to the manganese element is 0.4, the mass percentage of the ordered mesoporous alumina carrier is 78,8-92.0%, and the mass percentage of MnO2 is 5-13%. The invention further relates to a preparation method and application of the catalyst. The ordered mesoporous alumina is adopted as the carrier for the first time to be applied to the field of novel environment catalytic materials, the preparation method has the advantages of being easy to implement, small in gas resistance and good in low temperature activity, and the industrial application potential is achieved.

Description

technical field [0001] The invention belongs to the technical field of waste gas treatment, and relates to a preparation method and application of a novel low-temperature denitrification catalyst with ordered mesoporous alumina as a carrier. Background technique [0002] Regarding the pollution control of the iron and steel industry, the government work report last year clearly stated that my country will start the ultra-low emission transformation of the iron and steel industry in 2018. The hourly average emission concentration of nitrogen oxides in flue gas from machine head and pellet roasting flue gas is ≤50mg / m 3 . The improvement of air pollution control standards in the iron and steel industry is imminent. Under this background, it is imperative to develop new high-efficiency steel sintering flue gas denitrification catalysts. [0003] Currently widely used V 2 o 5 -WO 3 (MoO 3 ) / TiO 2 The working temperature of the catalyst is high (300 ~ 400°C), so that the SC...

Claims

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Application Information

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IPC IPC(8): B01J23/889B01J37/02B01J37/08B01D53/86B01D53/56
CPCB01D53/8628B01D2258/0283B01J23/8892B01J37/0201B01J37/082
Inventor 黄张根刘勇进侯亚芹李昱琳
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI