Honeycomb type low-temperature flue gas denitrification catalyst and preparing method

A denitration catalyst and low-temperature flue gas technology, applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems that denitration catalysts cannot be used normally, cannot be applied in large-scale industrialization, and have a narrow application temperature range, etc. Achieve the effect of improving anti-poisoning performance, improving denitration efficiency, and improving mechanical strength and hardness

Inactive Publication Date: 2016-06-01
东营信拓汽车消声器有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The reaction temperature of SNCR technology is 850°C-1100°C, the highest efficiency of this technology is about 50%, and it will cause a large amount of NH3 to escape
The SCR technology uses NH3 as the reducing agent, and the efficiency can usually reach more than 80%. Its characteristic is that the catalyst V2O5-TiO2 has good catalytic activity in the temperature range of 300°C-420°C, but it is not suitable for industrial applications other than power plant boilers. Conditions, due to the low flue gas temperature, usually below 300°C, ordinary denitrification catalysts cannot be used normally
[0004] At present, the existing honeycomb low-temperature denitrification catalyst technology in China cannot be applied on a large scale. The main disadvantages are narrow application temperature range, low product strength, low removal efficiency, short practical application life, and no wear resistance.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0016] The preparation steps of above-mentioned catalyst are as follows:

[0017] First configure the active component solution: the precursor of vanadium oxide ammonium metavanadate, the precursor of molybdenum oxide ammonium paramolybdate, the precursor of tungsten oxide ammonium paratungstate and manganese nitrate in proportion (ammonium metavanadate 3.87-6.45 parts by mass, ammonium paramolybdate 3.83-6.30 parts by mass, ammonium paratungstate 0.11-1.13 parts by mass, manganese nitrate 2.89-8.67 parts by mass) dissolved in deionized water, then add 0.3-0.8 parts by mass of copper nitrate, 0.02-0.1 parts by mass boric acid and 0.03-0.3 parts by mass of triammonium phosphate, the solution is heated to 50°C-60°C, and then the pH value of the solution is adjusted to 2.0-3.0 with oxalic acid or citric acid.

[0018] Secondly, the impregnation method is used to support the catalyst: take 76.25-88.95 parts by mass of nano-anatase titanium dioxide, slowly add the active component ...

Embodiment 1

[0021] (1) Configure the active solution, the percentage of each component: ammonium metavanadate 3% ammonium paramolybdate 4% ammonium paratungstate 1% manganese nitrate 4% copper nitrate 0.1% boric acid 0.1% triammonium phosphate 0.3%, titanium dioxide 87.5%. The ratio between the final composition of the catalyst and the precursor is as follows: the ratio of vanadium oxide to ammonium metavanadate is 0.775, the ratio of molybdenum oxide to ammonium paramolybdate is 0.885, the ratio of tungsten oxide to ammonium paratungstate is 0.81, and the ratio of manganese oxide to manganese nitrate The proportional relationship is 0.346.

[0022] (2) Prepare deionized water of the same quality as titanium dioxide, first add ammonium metavanadate, ammonium paramolybdate, ammonium paratungstate, then add copper nitrate, boric acid, triammonium phosphate, heat the solution to 60°C and add oxalic acid, adjust the pH value to 2.0.

[0023] (3) Impregnate the supported catalyst, add the cor...

Embodiment 2

[0026] (1) Configure the active solution, the percentage of each component: ammonium metavanadate 3.2% ammonium paramolybdate 5% ammonium paratungstate 0.8% manganese nitrate 5% copper nitrate 0.1% boric acid 0.1% triammonium phosphate 0.3%, titanium dioxide 85.5%. The ratio between the final composition of the catalyst and the precursor is as follows: the ratio of vanadium oxide to ammonium metavanadate is 0.775, the ratio of molybdenum oxide to ammonium paramolybdate is 0.885, the ratio of tungsten oxide to ammonium paratungstate is 0.81, and the ratio of manganese oxide to manganese nitrate The proportional relationship is 0.346.

[0027] (2) Prepare deionized water equal in quality to titanium dioxide, first add ammonium metavanadate, ammonium paramolybdate, ammonium paratungstate, then add copper nitrate, boric acid, triammonium phosphate, heat the solution to 60°C and add citric acid to adjust the pH value to 2.0.

[0028](3) Impregnate the supported catalyst, add the c...

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Abstract

The invention discloses a honeycomb type low-temperature flue gas denitrification catalystpowder and a preparing method thereof.The honeycomb type low-temperature flue gas denitrification catalyst powder is prepared from, by mass, 3.0-5.0 parts of vanadium oxide, 3.5-5.1 parts of molybdenum oxide, 0.1-1.0 part of tungsten oxide, 0.1-3.0 parts of manganese oxide, 0.01-0.1 part of phosphorus oxide, 0.01-0.05 part of boric oxide, 0.1-1.0 part of copper oxide and 84.75-92.68 parts of titanium dioxide.The preparing method comprises the steps that firstly, an active component solution is prepared; secondly, a catalyst is loaded with an impregnation method; thirdly, the consistent honeycomb type catalyst is prepared through extruding forming.According to the honeycomb type low-temperature flue gas denitrification catalyst powder and the preparing method thereof, the activity and catalytic capability of the low-temperature flue gas denitrification catalyst are effectively improved, the denitrification efficiency can reach 38% at 120 DEG C and reaches 95.1% at 210 DEG C, high industrial application value is achieved, and the honeycomb type low-temperature flue gas denitrification catalyst can be widely applied to NH3 selective catalytic reaction of nitric oxide in flue gas.

Description

a technical field [0001] The present invention relates to a catalyst, especially a kind of NH 3 Selective Catalytic Reduction (SCR) Removal of NO X Honeycomb catalyst and preparation method thereof. Two technical background [0002] Nitrogen oxides (NO X ) mainly comes from the combustion of fossil fuels, which can not only produce acid rain, but also react with hydrocarbons to form photochemical smog, which is one of the main sources of pm2.5 pollutants at present. Air quality has huge implications. [0003] NO X It mainly adopts the methods of combustion process and post-combustion treatment. At present, low nitrogen combustion (LNB), selective non-catalytic reduction (SNCR) and selective catalytic reduction (SCR) technologies are mainly used in industry. LNB technology is to change the combustion method of fuel, and the efficiency is usually only 30-40%. The reaction temperature of SNCR technology is 850°C-1100°C, the highest efficiency of this technology is about 5...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/199B01J35/04B01D53/86B01D53/56
CPCB01J27/199B01D53/8628B01J35/04
Inventor 延晓峰杜德亮周少坤
Owner 东营信拓汽车消声器有限公司
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