Denitration catalyst and preparation method thereof

A technology of denitration catalyst and composite catalyst, which is applied in the field of denitration catalyst and its preparation, can solve the problems of high ash content, high ash content of flue gas, catalyst wear, etc., achieve high hardness and wear resistance, huge pore structure, and improve the effect of SO2 resistance

Pending Publication Date: 2017-05-31
SHENWU TECH GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The ash content of flue gas from coal-fired power plants in my country is high, which can easily cause a series of problems such as catalyst wear, blockage, poisoning, etc. Catalyst blockage and poisoning can be restored by regeneration, but catalyst wear is the damage of the physical structure of the catalyst, which cannot be regenerated. Wear is the catalyst consumption important factor
In addition, during the production, the denitrification catalyst is in contact with the acidic strong corrosive medium, which leads to serious corrosion of the catalyst, and at the same time as the acid corrosion, there is also the phenomenon of movement and impact of solid particles on the catalyst. Under long-term continuous use conditions, the catalyst is easily damaged
[0005] The existing anti-wear technology of denitration catalyst generally adopts end face hardening, which improves the wear resistance of the catalyst to a certain extent, but the ash content in coal in my country is very high, and the hardening of the end face alone cannot completely solve the problem of catalyst wear, especially in flow In the case of uneven field distribution, the catalyst will undergo non-renewable physical damage such as cracking and collapse due to insufficient wear resistance under the erosion of high ash flue gas
[0006] Therefore, the current denitrification catalysts still need to be improved

Method used

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  • Denitration catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0065] 1. Preparation of carrier

[0066] Take 43.96g of titanyl sulfate and 36.64g of aluminum chloride, dissolve them in an appropriate amount of deionized water, and stir them evenly to prepare a titanium source solution and an aluminum source solution respectively, and the concentration ratio of the two is 1:1. The obtained titanium source solution, aluminum source solution, and ammonia water are dripped into a reaction kettle at a certain flow rate in a co-current manner, and a stirring device is installed in the reaction kettle. The dripping speed of the titanium source solution and the aluminum source solution is the same, the dripping speed of ammonia water is controlled, the pH value of the reaction solution is controlled at 10, and a precipitation mixture of titanium hydroxide and aluminum hydroxide is obtained by co-precipitation. Suction filtration and washing of the precipitate were repeated several times until the pH value of the filtrate reached about 7. After ...

Embodiment 2

[0077] 1. Preparation of carrier

[0078] Take 72.77g of titanyl sulfate and 30.33g of aluminum chloride, dissolve them in an appropriate amount of deionized water, and stir them evenly to prepare a titanium source solution and an aluminum source solution respectively, and the concentration ratio of the two is 1:0.5. The obtained titanium source solution, aluminum source solution, and ammonia water are dripped into a reaction kettle at a certain flow rate in a co-current manner, and a stirring device is installed in the reaction kettle. The dripping speed of the titanium source solution and the aluminum source solution is the same, the dripping speed of ammonia water is controlled, the pH value of the reaction solution is controlled at 10, and a precipitation mixture of titanium hydroxide and aluminum hydroxide is obtained by co-precipitation. Suction filtration and washing of the precipitate were repeated several times until the pH value of the filtrate reached about 7. Afte...

Embodiment 3

[0089] 1. Preparation of carrier

[0090]Take 37.79g of titanyl sulfate and 63.01g of aluminum chloride, dissolve them in an appropriate amount of deionized water, and stir them evenly to prepare titanium source solution and aluminum source solution respectively, and the concentration ratio of the two is 1:2. The obtained titanium source solution, aluminum source solution, and ammonia water are dripped into a reaction kettle at a certain flow rate in a co-current manner, and a stirring device is installed in the reaction kettle. The dropping speed of the titanium source solution and the aluminum source solution is the same, the dropping speed of ammonia water is controlled, the pH value of the reaction solution is controlled at 10, and a precipitation mixture of titanium hydroxide and aluminum hydroxide is obtained by co-precipitation. Suction filtration and washing of the precipitate were repeated several times until the pH value of the filtrate reached about 7. After drying...

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Abstract

The invention discloses a denitration catalyst and a preparation method thereof. The preparation method comprises the following steps: preparing a precipitate mixture of titanium hydroxide and aluminium hydroxide; drying and roasting the precipitate mixture to obtain TiO2-Al2O3 compound oxide carrier powder; extruding, forming, sizing and drying the TiO2-Al2O3 compound oxide carrier powder, activated carbon powder, enamelled powder and an adhesive to obtain an activated carbon/TiO2-Al2O3 compound catalyst; dissolving ammonium metatungstate and ammonium metavanadate in oxalic acid to obtain first impregnation liquid; impregnating the activated carbon/TiO2-Al2O3 compound catalyst in the first impregnation liquid to obtain a V2O5-WO3/activated carbon/TiO2-Al2O3 compound catalyst; preparing second impregnation liquid; and impregnating the V2O5-WO3/activated carbon/TiO2-Al2O3 compound catalyst in second impregnation liquid to obtain the denitration catalyst. The denitration catalyst prepared by the method disclosed by the invention has relatively high denitration catalytic activity, is high in wear resistance and acid resistance and wide in active temperature region, and can recover waste heat while performs denitration treatment on to-be-treated flue gas.

Description

technical field [0001] The invention relates to the technical field of chemical engineering, in particular, the invention relates to a denitration catalyst and a preparation method thereof. Background technique [0002] NO emissions from human activities x More than 90% comes from the fuel combustion process. When fuels in various industrial furnaces, civil stoves, motor vehicles and other internal combustion engines are burned at high temperature, the nitrogen-containing substances in the fuel are oxidized to produce NO x , the N in the air involved in the combustion 2 and O 2 also generates NO x . From the perspective of energy structure, coal occupies an absolute dominant position in the composition of primary energy and power generation energy in China. And more than 80% of coal in our country is directly burned, especially for power plants, industrial boilers and civil boilers. Therefore, for a long period of time, the NO in flue gas X Emissions are the cause of...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/888B01D53/86B01D53/56
CPCB01J23/888B01D53/8628B01D2258/0283B01J23/002B01J2523/00B01J2523/55B01J2523/69B01J2523/47B01J2523/31
Inventor 吴道洪宋敏洁陈珊王东方王志军
Owner SHENWU TECH GRP CO LTD
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