Method for preparing flue gas SCR (Selective Catalytic Reduction) denitration catalyst

A denitrification catalyst and flue gas technology, applied in the direction of catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of low-temperature denitrification efficiency of commercial catalysts, high cost of SCR denitrification, and high energy consumption of catalyst preparation , to achieve the effect of solving low-temperature denitrification efficiency, improving low-temperature SCR denitrification activity, and improving performance

Inactive Publication Date: 2012-07-11
SHANDONG UNIV
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] The purpose of the present invention is to combine microwave radiation technology with the advantages of rapid heating and no temperature gradient, and apply microwave radiation technology to the preparation of power plant SCR denitrification catalyst, and provide a preparation method of flue gas SCR denitration catalyst, which solves the problem of catalyst High energy consumption for preparation, high cost of SCR denitrification, low denitrification efficiency of commercial catalysts at low temperature and narrow denitrification temperature window, etc.

Method used

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  • Method for preparing flue gas SCR (Selective Catalytic Reduction) denitration catalyst
  • Method for preparing flue gas SCR (Selective Catalytic Reduction) denitration catalyst
  • Method for preparing flue gas SCR (Selective Catalytic Reduction) denitration catalyst

Examples

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Embodiment 1

[0026] A flue gas SCR denitrification catalyst (2%V5%Mn / TiO 2 ) preparation method, the steps are as follows:

[0027] 215mg oxalic acid (C 2 h 2 o 4 ) into 30ml of distilled water, stirred to make an oxalic acid solution, and then 133mg of ammonium metavanadate (NH 4 VO 3 ) was dissolved in the oxalic acid solution, and constantly stirred to make ammonium metavanadate-oxalic acid solution; 1028mg manganese nitrate Mn(NO 3 ) 2 Dissolved in the solution prepared above, then 5gTiO 2 The powder was immersed in this mixed solution, and stirred for 3 hours under the condition of heating in a water bath at 50° C. to obtain a mixed sol (active component V 2 o 5 with TiO 2 The mass ratio is 2%, MnO 2 with TiO 2 The mass ratio of the sol is 5%); the prepared mixed sol was left to stand in the air for 8h, and then put into a microwave oven and heated for 20min at a power of 210W to obtain a solid; , the obtained solid is ground after cooling, and sieved to get the particles ...

Embodiment 2

[0029] A flue gas SCR denitrification catalyst (3%V5%Mn / TiO 2 ) preparation method, the steps are as follows: 322.5mg oxalic acid (C 2 h 2 o 4 ) into 35ml of distilled water, stirred to make an oxalic acid solution, and then 199.5mg of ammonium metavanadate (NH 4 VO 3 ) was dissolved in oxalic acid solution, and stirred continuously to make ammonium metavanadate-oxalic acid solution; 1028mg manganese nitrate (Mn(NO 3 ) 2 ) was dissolved in the solution prepared above, and then 5gTiO 2 The powder was immersed in this mixed solution, and stirred for 2 hours under the condition of heating in a water bath at 60° C. to obtain a mixed sol (active component V 2 o 5 with TiO 2 The mass ratio is 3%, MnO 2 with TiO 2 The mass ratio is 5%); the prepared mixed sol was left to stand in the air for 10h, then put into a microwave oven and heated for 20min at a power of 210W to obtain a solid; put the obtained solid into a muffle furnace and calcined for 5h under an air atmosphere o...

Embodiment 3

[0031] A flue gas SCR denitrification catalyst (4%V5%Mn / TiO 2 ) preparation method, the steps are as follows: 430mg oxalic acid C 2 h 2 o 4 Add 40ml of distilled water, stir to make oxalic acid solution, then add 266mg of ammonium metavanadate NH 4 VO 3 Dissolve in oxalic acid solution, stir constantly to make ammonium metavanadate-oxalic acid solution; mix 1028mg manganese nitrate Mn(NO 3 ) 2 Dissolved in the solution prepared above, then 5gTiO 2 The powder is immersed in this mixed solution, and stirred for 1 h under the condition of heating in a water bath at 70° C. to obtain a mixed sol (active component V 2 o 5 with TiO 2 The mass ratio is 4%, MnO 2 with TiO 2 The mass ratio of the sol is 5%); the prepared mixed sol was left to stand in the air for 12h, and then placed in a microwave oven at a power of 300W and heated for 10min to obtain a solid; the obtained solid was calcined in a muffle furnace at 400°C for 6h , the obtained solid is ground after cooling, an...

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Abstract

The invention relates to a method for preparing a flue gas SCR (Selective Catalytic Reduction) denitration catalyst. The method comprises the following steps of: mixing ammonium metavanadate, oxalic acid, manganese salt and water for preparing a mixture solution, adding titanium dioxide powder into the mixture solution, heating in water bath and stirring, and obtaining mixed sol by standing at room temperature; putting the mixed sol into a microwave oven, heating and drying by utilizing microwave radiation; and putting dried solid into a muffle furnace for burning. According to the method disclosed by the invention, a temperature window of the SCR catalyst can be broadened to a low-temperature direction, the problems of low denitration efficiency at low temperature and narrow temperature window of a commercial catalyst are solved; compared with the traditional drying method, the microwave radiation heating and drying method has the advantages that low-temperature SCR denitration activity of the composite catalyst can be increased to a large extend, when the activity temperature is up to 250 DEG C, the denitration efficiency of the catalyst prepared by the traditional drying method is up to 51.9%, and the denitration efficiency of the catalyst can be increased by 31.7 percentage points and can be up to 83.6% by the microwave radiation heating and drying method.

Description

technical field [0001] The invention relates to a preparation method of a denitrification catalyst, belonging to the fields of flue gas denitrification technology and microwave technology. Background technique [0002] Nitrogen oxides are one of the main air pollutants, which can cause pollution such as acid rain and photochemical smog, and cause great harm to the environment and human body. Nitrogen oxide emissions from coal-fired power plants account for about half of my country's total emissions. Therefore, controlling NOx from coal-fired power plants x Emissions are imminent. At present, technologies to control NOx emissions from coal-fired power plants mainly include low NO x Burners, reburning, Selective Non-Catalytic Reduction (SNCR) and Selective Catalytic Reduction (SCR). Compared with denitration technologies such as reburning denitration and SNCR denitration, SCR has higher denitration efficiency and is easy to meet the increasingly stringent NO x national emi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/34B01J37/34B01D53/90B01D53/56
Inventor 韩奎华熊志波李英杰路春美牛胜利邹鹏
Owner SHANDONG UNIV
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