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Selective reduction catalyst for nitrogen oxide in smoking gas, its preparation method and application

A nitrogen oxides, selective technology, applied in physical/chemical process catalysts, chemical instruments and methods, separation methods, etc., can solve the problems of small specific surface area of ​​active components, poor heat transfer performance, low mechanical strength, etc. The effect of long durability, quick start performance and high mechanical strength

Inactive Publication Date: 2003-09-24
SOUTH CHINA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The catalyzer that is applied to this method is called SCR catalyst, and many patents have been reported various formulations of this catalyzer; For example, patents such as US5,198,403, US4,085,193 disclose SCR catalyst and preparation method thereof; In these patents The structure, composition and preparation methods of catalysts have been widely used. They load active components such as vanadium, molybdenum, tungsten, etc. on inorganic oxides through homogeneous solution method, co-precipitation method, solution precipitation method, precipitation mixing method and other methods. Carriers such as titanium dioxide, alumina, silica and zirconia, etc., add binders for extrusion molding, and finally heat treatment; because the aforementioned technologies use extrusion molding, these catalysts have low mechanical strength, poor heat transfer performance, and start-up. Disadvantages such as slowness, small specific surface area of ​​active components, high cost due to the need for a large amount of active components

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033]31.0 g of cordierite honeycomb ceramics with a diameter of 30 mm and a height of 50 mm were fired at 450 ° C and cooled; the fired cordierite honeycomb ceramics were heated in Al(OH) 3 Immerse in the sol for 30 minutes, take it out and dry it in a drying oven for 2 hours, set the temperature at 120°C; impregnate the dried carrier in the sol again, repeat the steps of impregnation and drying until the increase after drying The weight is slightly greater than 4.0g, and the carrier is calcined at 450°C to obtain 4.0g Al loaded 2 o 3 cordierite honeycomb ceramic substrate.

[0034] With the same method and steps the above-mentioned obtained load Al 2 o 3 The cordierite honeycomb ceramic support on Ti(OH) 4 Immersion-drying in the sol, and finally got the loaded 0.9gTiO 2 and 4.0gAl 2 o 3 composite catalyst support.

[0035] With 0.1046g ammonium metavanadate, 0.8652g ammonium molybdate and 0.0989g ammonium tungstate in 50mlH 2 Miscible in O; soak the prepared compos...

Embodiment 2

[0038] The preparation method is the same as in Example 1. 31.3g of cordierite honeycomb ceramics with a diameter of 30mm and a height of 50mm are prepared as 4.2gAl 2 o 3 and 0.9g TiO 2 composite catalyst support. The active ingredient content is 0.09gV 2 o 5 , 0.09gMoO 3 , 0.72gWO 3 . at various temperatures, space velocities and NH 3 The NO removal experiment was carried out on the sample under the / NO ratio, and the NO removal rate results are shown in Table 2.

[0039] Table 2 Note: volumetric space velocity 10000h -1 , O 2 Content 5%

Embodiment 3

[0041] The preparation method is the same as in Example 1. 31.0 g of cordierite honeycomb ceramics with a diameter of 30 mm and a height of 50 mm are prepared as a load of 4.6 g Al 2 o 3 and 1.2gTiO 2 composite catalyst support. The active ingredient content is 0.10gV 2 o 5 , 0.10gMoO 3 , 0.80gWO 3 . The NO removal experiment was carried out on this sample, and the NO removal rate results are shown in Table 3:

[0042] table 3 Note: volumetric space velocity 10000h -1 , O 2 Content 5%

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Abstract

The present invention provides a selective reduction catalyst of nitrogen oxide in flue gas. It uses iolite cellular ceramics, Al2O3 and TiO2 as carrier, and uses the following metal oxides as activecomponents: (A), V2O5; (B) MoO3; and (C) WO3. The preparation method of said catalyst includes the following steps: preparing compouind catalyst carrier on which Al2O3 and TiO2 are loaded; repeatedlyimpregnating said compound catalyst carrier with ammonium metavanadate, ammonium molybdate and ammonium tungstate mixed aqueous solution, drying until the set load quantity of V2O5, WO3 and MoO3 is reached; finally roasting for 1-5 hr. so as to obtain the invented catalyst. Said catalyst can be used in ammonia reduction method for removing nitrogen oxide from flue gas.

Description

technical field [0001] The invention relates to a catalyst technology, in particular to a catalyst for the selective reduction of nitrogen oxides in flue gas, its preparation method and application. Background technique [0002] The pollution of the atmosphere by nitrogen oxides (NOx) is a worldwide environmental problem. Its main impact on the atmosphere is the formation of acid rain and high ground ozone concentration, which poses a huge threat to human health and the ecological environment. Post-combustion flue gas treatment is essential, although various combustion modification techniques are applied to reduce NO x Emissions, but in order to meet increasingly stringent emission standards, the development of new and efficient catalysts to deal with various gaseous pollutants is also becoming more and more important. In recent years, the use of catalysts to convert nitrogen oxides in flue gas emitted from power stations and other pollution sourc...

Claims

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Application Information

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IPC IPC(8): B01D53/56B01D53/86B01D53/94B01J21/06
Inventor 田柳青叶代启
Owner SOUTH CHINA UNIV OF TECH
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