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A kind of preparation method of high active middle and low temperature SCR denitrification catalyst

A denitration catalyst and a high-activity technology, applied in the field of environmental engineering, can solve the problems of insufficient number of crystal faces and the decline of the macroscopic catalytic performance of the catalyst, and achieve the effect of improving the catalytic performance.

Active Publication Date: 2017-10-10
河南东大高温节能材料有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This is for NO and NO 2 Insufficient number of crystal faces with high adsorption and activation capacity, resulting in a decline in the macroscopic catalytic performance of the catalyst

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] The preparation method of the high-activity medium-low temperature SCR denitration catalyst of this embodiment, the steps are as follows:

[0026] (1) Impregnation: 100 grams of ZSM-5 molecular sieve with a silicon-aluminum ratio of 25, 15.15 grams of Cu (NO 3 ) 2 ·3H 2 Dissolve O in 200mL of water; mix the molecular sieve and copper nitrate aqueous solution evenly, and dry at 80°C for 10 hours to complete the impregnation;

[0027] (2) Calcination: The obtained product was dried at 100°C for 6 hours, and then calcined at 550°C for 6 hours. The obtained catalyst number is Cat-1, and the copper oxide loading is 5%;

[0028] (3) Modification: The prepared Cat-1 was placed in a pressure vessel, and the NO content was 10%. 2 The content is 5%, and the mixed atmosphere of helium as the balance gas is modified. The modification temperature is 600 ° C, and the modification time is 4 hours. The catalyst obtained is Cat-2.

Embodiment 2

[0030] The preparation method of the high-activity medium-low temperature SCR denitration catalyst of this embodiment, the steps are as follows:

[0031] (1) Impregnation: 100 grams of ZSM-5 molecular sieve with a silicon-aluminum ratio of 80, 38.88 grams of Ni (NO 3 )2·6H 2 O was dissolved in 200 mL of water. Mix the molecular sieve and nickel nitrate aqueous solution evenly, and dry at 80°C for 10 hours to complete the impregnation;

[0032] (2) Calcination: The product obtained in step (1) was dried at 100°C for 6 hours, and then calcined at 500°C for 7 hours to obtain a catalyst numbered Cat-3 with a nickel oxide loading of 10%;

[0033] (3) Modification: The prepared Cat-3 was placed in a pressure vessel, and the NO content was 10%. 2 The content is 5%, and the mixed atmosphere of helium as the balance gas is modified. The modification temperature is 700 ° C, and the modification time is 6 hours. The catalyst obtained is Cat-4.

Embodiment 3

[0035] The preparation method of the high-activity medium-low temperature SCR denitration catalyst of this embodiment, the steps are as follows:

[0036] (1) Impregnation: 100 grams of ZSM-5 molecular sieve with a silicon-aluminum ratio of 120, 29.16 grams of Ni (NO 3 ) 2 ·6H 2 O and 22.73 g Cu (NO 3 ) 2 ·3H 2 Dissolve O in 200mL water; mix molecular sieve with copper nitrate and nickel nitrate aqueous solution evenly, and dry at 80°C for 10 hours to complete impregnation;

[0037] (2) Calcination: The product obtained in step (1) was dried at 100°C for 6 hours, and then calcined at 600°C for 5 hours to obtain a catalyst numbered Cat-5, with nickel oxide and copper oxide loadings of 15%;

[0038] (3) Modification: place the prepared Cat-3 in a pressure vessel, use a mixed atmosphere with NO content of 20%, NO2 content of 10%, and helium as the balance gas for modification treatment, and the modification temperature is 700 °C, the modification time is 6 hours, and the pre...

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Abstract

The invention discloses a method for preparing a high-activity catalyst for medium and low temperature SCR denitration. The present invention uses a ZSM-5 type microporous zeolite as a carrier, which is loaded with one or more of copper and nickel oxides. The loading employs an equivalent-volume impregnation method, uses the nitrate of the above metal as load raw materials; and high temperature calcination is used for the production of an oxide catalyst. The oxide catalyst is treated at a high temperature by using a mixed gas of NO and NO2 at a certain concentration as an oxide crystal form selective modifier, so that the crystal form of the oxide transforms into one with high adsorption activation performance of nitrogen oxide, thereby enhancing the low-temperature catalytic activity.

Description

technical field [0001] The invention belongs to the field of environmental engineering, and in particular relates to a preparation method of a catalyst for removing nitrogen oxides from industrial tail gas by catalyzing ammonia reduction reaction. Background technique [0002] Nitrogen oxides (NOx) mainly include NO and NO2. A variety of industrial exhaust gases contain nitrogen oxides, which are discharged into the atmosphere, which is an important cause of acid rain and photochemical smog, and is also the main cause of severe smog in northern my country. my country's coal-based energy structure results in the flue gas of coal-fired power plants containing a large amount of nitrogen oxides, which is the main source of nitrogen oxide emissions. Other industries such as iron and steel, chemical industry, medicine, cement, waste incineration power generation and other industries all emit nitrogen oxides, and the exhaust of internal combustion engines in vehicles is also the m...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/46B01D53/90B01D53/56
CPCB01D53/8628B01D53/90B01D2255/2073B01D2255/20738B01D2255/20753B01D2255/20761B01D2255/504B01D2257/404B01J29/46B01J2229/12B01J2229/18
Inventor 张傑
Owner 河南东大高温节能材料有限公司