Combined catalyst for improving denitration performance and application thereof

A technology for combining catalyst and performance, applied in the field of catalyst segment combination, can solve the problems of difficulty in meeting diesel vehicles, catalyst poisoning and high operating temperature, and achieve the effects of high selectivity, low cost and simple raw materials

Inactive Publication Date: 2012-07-25
BEIJING UNIV OF CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For example, the denitrification methods disclosed in patent CN101428215 and patent CN101396655 are based on V 2 o 5 -WO 3 / TiO 2 The advantage of this type of catalytic system is that it has a high catalytic activity for the standard SCR reaction shown in equation (1), but it also has certain problems: the use temperature range of the catalyst is limited to 250-430 °C , has the characteristics of high operating temperature and narrow temperature window, and the catalyst has poor activity below 250 °C, so there is a lot of gas preheating energy consumption in industrial applications, although increasing the V in the catalyst 2 o 5 The specific gravity can also improve the low-temperature activity, but at the same time it will promote the SO in the diesel engine exhaust 2 Catalyst poisoning by oxidation
It can be seen that a single high temperature effect is significant for V 2 o 5 -WO 3 / TiO 2 Catalyst or MnO with outstanding low temperature effect x -CeO 2 / TiO 2 Both are difficult to meet the requirements of diesel vehicle SCR, and the combined result of the catalytic performance of the two is what is needed by today's research.

Method used

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  • Combined catalyst for improving denitration performance and application thereof
  • Combined catalyst for improving denitration performance and application thereof
  • Combined catalyst for improving denitration performance and application thereof

Examples

Experimental program
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preparation example Construction

[0034] Staged Catalyst Preparation

[0035] Weigh the mass of the precursor according to the result calculated in step (1), and divide it into two beakers to prepare V 2 o 5 -WO 3 / TiO 2 with MnO x -CeO 2 / TiO 2 . Slowly add the weighed ammonium metavanadate, ammonium paratungstate, manganese nitrate, and cerium nitrate into two 1000ml beakers that have taken 500ml of deionized water, and stir in a water bath at 40°C to promote the complete dissolution of the precursor. liquid, and then a certain amount of industrial anatase TiO 2 Add them to the impregnating liquid respectively, keep stirring in a water bath for 12-24 hours, then use a rotary evaporator to remove the water in the impregnating liquid, dry them in an oven, take them out and calcinate them in a muffle furnace. The obtained two calcined products are cooled, ground, pressed into tablets, and 40-60 mesh particles are screened out to obtain the corresponding V2 o 5 -WO 3 / TiO 2 with MnO x -CeO 2 / TiO 2...

Embodiment 1

[0053] Weigh 0.651gMn(NO 3 ) 2 (chemically pure, 50%), 0.252g Ce(NO 3 ) 3 ·6H 2 O (analytical pure), and dissolve it in water to make an impregnation solution, then weigh 1g of anatase TiO 2 Add it into the impregnating solution, stir in a water bath at 40°C for 24 hours, then use a rotary evaporator to remove the moisture in the impregnating solution, place it in an oven to dry for 6 hours, and finally place the above-mentioned loaded catalyst in an air atmosphere at 2°C / min The temperature was raised to 500°C for 6 hours, and the obtained calcined product was cooled, ground, pressed into tablets, and 40-60 mesh particles were screened out to obtain a loading capacity of 10wt% Mn, 10wt% CeO 2 Loaded MnO x -CeO 2 / TiO 2 catalyst.

[0054] Weigh 0.0514g NH 4 VO 3 (analytically pure), 0.113g 5(NH 4 ) 2 O·12WO 3 ·5H 2 O (analytical pure), and dissolve it in water to make an impregnation solution, then weigh 1g of anatase TiO 2 Add it into the impregnating solution,...

Embodiment 2

[0057] Weigh 0.651g Mn(NO 3 ) 2 (chemically pure, 50%), 0.202g Ce(NO 3 ) 3 ·6H 2 O (analytically pure), all the other preparation methods are the same as in Example 1, and the loading capacity obtained is 10wt% Mn, 8wt% CeO 2 MnO x -CeO 2 / TiO 2 catalyst.

[0058] Weigh 0.0514g NH 4 VO 3 (analytically pure), 0.09g 5(NH 4 ) 2 O·12WO 3 ·5H 2 O (analytically pure), all the other preparation methods are the same as in Example 1, and the loading capacity that can be obtained is 4wt%V 2 o 5 , 8wt% WO 3 V 2 o 5 -WO 3 / TiO 2 catalyst.

[0059] Catalyst segmented combination mode and activity evaluation means are the same as embodiment 1, NO x See Table 1, 2, 3, 4 for details of conversion rate and each reaction product yield.

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Abstract

The invention discloses a combined catalyst for improving denitration performance and an application thereof, which belongs to the field of catalysts. In the catalyst, industrial anatase crystal form TiO2 is taken as a carrier; V2O5-WO3/TiO2 is put at the front section of MnOx-CeO2/TiO2, and is called front section; MnOx-CeO2/TiO2 is called back section; the front section refers to a section where an air current main body is contacted firstly; the back section refers to a section where the air current main body is contacted secondly; the mass ratio of the front section to the back section is 1:1-1:3; V2O5 accounts for 2-4 percent of the mass of the carrier TiO2; WO3 accounts for 8-10 percent of the mass of the carrier TiO2; Mn accounts for 10-20 percent of the mass of the carrier TiO2; CeO2 accounts for 8-10 percent of the mass of the carrier TiO2; and MnOx is taken as the general name of MnO2 and Mn2O3. The combined catalyst can be applied to an integral catalyst for industrial application. The combined catalyst has a wider active temperature window; particularly, the removing efficiency of NOx by NH3-SCR is greatly increased under the exhaust low-temperature wording condition of a diesel engine; and moreover, the same NOx removing efficiency as the conventional catalyst can be obtained at a medium-high temperature section.

Description

technical field [0001] The invention belongs to a catalyst segmented combination method for improving the performance of ammonia selective catalytic reduction of nitrogen oxides in diesel engine exhaust purification, in particular to a segmented combination method for improving the load-type composite oxide catalyst and the load The catalytic performance of the type monolithic catalyst can pass NH 3 A method for selective catalytic reduction of nitrogen oxides. Background technique [0002] Since the 1970s, with the aggravation of the shortage of global oil resources, the intensification of the greenhouse effect and the CO 2 The increase in emission reduction pressure and the continuous improvement of diesel engine technology make modern diesel engines not only efficient, economical (fuel consumption is about 30% lower than gasoline engines), environmentally friendly (CO 2 Its emissions are about 30% lower than that of gasoline engines), and it is completely comparable to ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/34B01J23/30B01D53/94B01D53/56
Inventor 张润铎罗臻陈标华
Owner BEIJING UNIV OF CHEM TECH
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