Low-temperature denitration catalyst capable of resisting halogen element Cl poisoning and preparation method and application of low-temperature denitration catalyst

A low-temperature denitrification and catalyst technology, applied in the direction of catalyst activation/preparation, chemical instruments and methods, heterogeneous catalyst chemical elements, etc., can solve the problems of long preparation cycle, abnormal discharge of target pollutants, limited application range, etc., and achieve good results Effects of anti-halogen Cl poisoning performance, good NOx elimination ability, and high NOx elimination ability

Pending Publication Date: 2021-10-01
SHANGHAI INST OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, two major problems emerged during the use of this technology in the industrial field: (1) The high activity temperature (300-400°C) of traditional SCR catalysts always requires auxiliary equipment and extra energy to heat the bag (2) The SCR catalyst has poor resistance to the inevitable deactivation caused by complex flue gas components, which greatly increases the cost of catalyst replacement and even leads to the target Abnormal discharge of pollutants
The catalyst prepared by ordinary impregnation method will limit its dispersibility due to the high content of active components, thereby reducing the activity; although the sol-gel method can solve the problem of low dispersibility, it has the disadvantages of long preparation period, complicated operation, Disadvantages such as limited scope

Method used

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  • Low-temperature denitration catalyst capable of resisting halogen element Cl poisoning and preparation method and application of low-temperature denitration catalyst
  • Low-temperature denitration catalyst capable of resisting halogen element Cl poisoning and preparation method and application of low-temperature denitration catalyst
  • Low-temperature denitration catalyst capable of resisting halogen element Cl poisoning and preparation method and application of low-temperature denitration catalyst

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Preparation of Mn-Ce-O by Surface Impregnation Combustion Method x / TiO 2 catalyst

[0038] (1) Weigh 2.87g of manganese nitrate (50% aqueous solution), 1.09g of cerium nitrate and 3.80g of glycine and dissolve them in 7mL of deionized water, stir and mix evenly;

[0039] (2) Weigh 2g of anatase titanium dioxide with a particle size of 100nm and add it to the mixed solution, and stir it with a magnetic force for 1h;

[0040] (3) Place the product obtained in step (2) in a muffle furnace preheated to 300°C and burn rapidly for 1-2 minutes, then continue to heat up from 300°C to 450°C, roast at 450°C for 4 hours, and finally grind Prepared Mn-Ce-O x / TiO 2 Catalyst, denoted as MCT-G.

Embodiment 2

[0057] MCT, MCT-G, Cl-MCT, Cl-MCT-G catalysts for NH 3 -Evaluation of catalytic activity of SCR low temperature denitrification reaction

[0058] The reaction conditions and process of activity test are as follows:

[0059] 500ppm NO, 500ppm NH 3 , 5vol%O 2 , N 2 As carrier gas, all gases are provided by cylinder gas, the total gas flow rate is 200mL / min, and the space velocity (GHSV) is 80000mL / (g·h). During the reaction, ensure that the quartz reaction tube of the catalyst is located in the constant temperature area of ​​the reactor. The activity test temperature is 50-250°C, and the activity test is carried out at every interval of 25°C as a temperature point. The test results are as follows: figure 1 shown.

[0060] from figure 1 It can be seen that the prepared Mn-Ce-O x / TiO 2 Catalyst NO x The order of conversion rate is as follows: MCT-G>MCT>Cl-MCT-G>Cl-MCT. At low temperature ( figure 2 As shown, after MCT-G catalyst was poisoned by Cl, NO x The conversion ...

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Abstract

The invention relates to a low-temperature denitration catalyst capable of resisting halogen element Cl poisoning and a preparation method and application thereof. The catalyst is prepared through a surface impregnation combustion method, and the preparation method comprises the following steps: (1) dissolving manganous nitrate, cerous nitrate and fuel in deionized water to obtain a mixed solution; (2) adding titanium dioxide into the mixed solution, and uniformly stirring to obtain a precursor product; and (3) burning the precursor product in a combustion chamber, continuously roasting, and grinding the obtained solid reaction product to obtain the target product. The catalyst is used for NH3-SCR reaction. Compared with a catalyst prepared by a traditional impregnation method, the Mn-Ce-Ox / TiO2 low-temperature denitration catalyst prepared by the preparation method disclosed by the invention has relatively good low-temperature denitration activity and halogen element Cl poisoning resistance, and the reduction amplitude of the NOx conversion rate of the catalyst is relatively small in a temperature range of 100-200 DEG C; equipment required in the preparation process is simple, the cost of raw materials is low, the combustion reaction is mild, and the method is a simple, safe and reliable new method.

Description

technical field [0001] The invention relates to the technical field of chemical catalysts, in particular to a Mn-Ce-O compound resistant to halogen element Cl poisoning x / TiO 2 Low-temperature denitrification catalyst and its preparation method and application. Background technique [0002] With the rapid development of the economy, the combustion of a large amount of fossil fuels and the emission of automobile exhaust have produced a lot of dust, sulfur dioxide (SO 2 ), nitrogen oxides (NO x ) and other air pollutants. NO x It is one of the main air pollutants and an important cause of air pollution phenomena such as acid rain, photochemical smog, and haze, and has become the focus of air pollution control. use NH 3 Performing selective catalytic reduction (SCR) has proven to be an effective after-combustion treatment technology to control NO emissions from stationary sources. However, two major problems emerged during the use of this technology in the industrial fi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/34B01J27/10B01J37/02B01J37/08B01D53/86B01D53/56
CPCB01J23/34B01J23/002B01J27/10B01J35/0013B01J37/0201B01J37/088B01D53/8628B01J2523/00B01J2523/3712B01J2523/47B01J2523/72
Inventor 毛东森叶琳倩郭晓明俞俊吴贵升
Owner SHANGHAI INST OF TECH
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