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Denitration catalyst for CO-SCR flue gas denitrification and preparation method thereof

A denitrification catalyst and catalyst technology, applied in the field of CO-SCR flue gas denitrification denitrification catalyst and its preparation, can solve the problems of lower production cost and easy cracking, and achieve lower production cost, high airflow resistance and high mechanical strength Effect

Pending Publication Date: 2022-01-11
SHIHEZI UNIVERSITY
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] The purpose of the present invention is to provide a method for preparing a denitrification catalyst for CO-SCR flue gas denitrification, by mixing the powder catalyst with active components and adhesive additives and coating it on the mullite carrier , while improving the adhesion, it solves the problem that mullite as a carrier is easy to crack during the low-temperature calcination process, thereby reducing the production cost

Method used

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  • Denitration catalyst for CO-SCR flue gas denitrification and preparation method thereof
  • Denitration catalyst for CO-SCR flue gas denitrification and preparation method thereof
  • Denitration catalyst for CO-SCR flue gas denitrification and preparation method thereof

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preparation example Construction

[0041] A preparation method for a denitration catalyst for CO-SCR flue gas denitration, comprising the following steps:

[0042] (1) prepare catalyst powder;

[0043] (2) Add additive and described catalyst powder to water, mix uniformly, obtain slurry; Described additive is inorganic binder, organic polymer solution, surfactant;

[0044] (3) impregnating the pretreated, honeycomb-shaped mullite carrier in the slurry, drying and calcining to obtain the denitration catalyst for CO-SCR flue gas denitration.

[0045] Preferably, in the step (1), the catalyst powder is prepared by co-precipitation method;

[0046] The mass percent of each component in the slurry in the step (2) is: water 50-70%, additive 10-20%, catalyst powder 20-40%;

[0047] The pretreatment in the step (3) is as follows: soak the cleaned mullite carrier in the mixed solution containing urea and aluminum salt for 24 hours, dry at 80° C., and then calcinate.

[0048] Further preferably, in the described step ...

Embodiment 1

[0063] The specific operation steps are as follows:

[0064] (1) Dissolving Cu salt and Ce salt in water to form metal salt solution, preparing catalyst powder by co-precipitation method, crushing to 100 mesh or more through a pulverizer, and then sieving for use.

[0065] The copper salt is at least one of copper sulfate, copper chloride and copper nitrate; the cerium salt is at least one of cerium nitrate, cerium chloride and cerium sulfate, and the molar ratio of Ce:Cu is 6.67:1.

[0066] In the preparation of catalyst powder by co-precipitation method: stir the metal salt solution, then add a precipitating agent dropwise (precipitating agent adopts a kind of sodium hydroxide and ammonia water) until its pH is 9-11, stir, let stand for precipitation, The powder catalyst is obtained after suction filtration, drying and calcination.

[0067] Preferably, the catalyst prepared by using cerium nitrate and copper nitrate has the best catalytic performance and is the best choice....

Embodiment 2

[0083] The specific operation steps are as follows:

[0084] (1) Using Al(NO 3 ) 3 9H 2 O Prepare 1 L, 2 mol / L aluminum salt solution, and then prepare 1 L, 6.67 mol / L urea solution, add these two parts of the solution into a jacketed stirring pot and stir for 4 hours at room temperature. Then pour the evenly stirred mixed solution into an iron mold box of 20cm*20cm*20cm, soak the mullite honeycomb carrier for 24 hours, dry and calcinate at 80°C to obtain the pretreated mullite carrier (The weight gain of the mullite carrier after pretreatment is not less than 5% of the mass of the carrier without pretreatment).

[0085] (2) 241.6g of Cu(NO 3 ) 2 ·3H 2 O and 2896.25g of Ce(NO 3 ) 3 ·6H 2 O was added into 2000g of purified water, and stirred until dissolved to obtain a metal salt solution. Then add 1mol / L sodium hydroxide solution to adjust the pH to 10-11, stir for 4 hours and let it stand for 24 hours, then use pure water to filter to neutral, then use ethanol to fi...

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Abstract

The invention relates to a denitration catalyst for CO-SCR flue gas denitration and a preparation method of the denitration catalyst. The preparation method comprises the following steps: (1) preparing catalyst powder; (2) adding an additive and the catalyst powder into water, and uniformly mixing to obtain slurry, wherein the additive comprises an inorganic binder, an organic polymer solution and a surfactant; and (3) dipping a pretreated honeycomb mullite carrier in the slurry, drying, and calcining to obtain the denitration catalyst for CO-SCR flue gas denitration. According to the denitration catalyst for CO-SCR flue gas denitration and the preparation method of the denitration catalyst, the powder catalyst is mixed with the additive with adhesion, so that the adhesion of a catalyst coating on a mullite carrier is enhanced, and the coating catalyst with low cost and high adhesion is obtained.

Description

technical field [0001] The invention belongs to the technical field of CO-SCR flue gas denitrification, and in particular relates to a denitrification catalyst for CO-SCR flue gas denitrification and a preparation method thereof. Background technique [0002] Fossil energy such as coal, oil and natural gas will produce a lot of nitrogen oxides that are harmful to the environment and human body when they are used, such as common nitrous oxide, nitrogen monoxide (NO), nitrogen dioxide (NO 2 )Wait. The presence of these nitrogen oxides in large quantities in the environment will not only affect animals and plants, but also reduce the visibility of the air, seriously affecting people's travel safety, and at the same time destroy the ozone layer and form acid rain to pollute the environment. When the content in the air is too high, it will endanger the human body. The immune system, respiratory system and cardiovascular and cerebrovascular systems, etc., may lead to death in sev...

Claims

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Application Information

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IPC IPC(8): B01J23/83B01J35/04B01J37/03B01J37/02B01D53/86B01D53/56
CPCB01J23/83B01J23/002B01J37/038B01J37/0213B01D53/8628B01D2251/204B01J35/56
Inventor 于锋李文健但建明代斌
Owner SHIHEZI UNIVERSITY