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Method for preparing low-temperature SCR (selective catalytic reduction) denitration catalyst

A denitration catalyst and low temperature technology, applied in the field of catalysis, can solve the problems of no flue gas denitration catalyst suitable for industrial kilns, low flue gas temperature, increase catalyst service life, etc., and achieve good nitrogen oxide removal rate and water resistance. Sulfur resistance, good low temperature activity

Inactive Publication Date: 2012-10-10
JIANGSU LONGYUAN CATALYST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At this time, most of the dust, heavy metals and substances contained in the flue gas that are likely to poison the catalyst are removed by the dust collector, which reduces the risk of catalyst wear, blockage and poisoning deactivation, increases the service life of the catalyst, and reduces the replacement of the catalyst. cycle, reducing the operating cost of the denitrification system, but in the low-dust arrangement, the flue gas temperature drops a lot, between 150-200 ° C, which poses a challenge to the low-temperature activity of the catalyst
[0004] In addition, the nitrogen oxides emitted by my country's industrial kilns (glass kilns, cement kilns, etc.) also account for a large part of the total domestic nitrogen oxide emissions, which is the second source of emissions after thermal power plants. The flue gas temperature of industrial kilns is relatively low, mostly between 150-250 °C, and there is no flue gas denitrification catalyst suitable for industrial kilns at present

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Embodiment 1 The preparation method of low-temperature SCR denitration catalyst comprises the following process steps:

[0019] (1) Preparation of ammonium metavanadate solution: weigh 6.4 g of ammonium metavanadate, stir and dissolve the weighed ammonium metavanadate in 10 g of ethanolamine aqueous solution at 90°C, the concentration of ethanolamine aqueous solution is 5 g / mL;

[0020] (2) Weigh 90g of titanium-tungsten powder, add the metal salt solution obtained in step (2) into it, heat to 70-90°C, keep stirring at a constant temperature until the water is evaporated to dryness, and then add the step ( 1) The obtained ammonium metavanadate solution was heated to 70-90°C, kept at a constant temperature while stirring evenly until the water was evaporated to dryness, and a solid was obtained;

[0021] (3) Drying: drying the solid finally obtained in step (3) at 50-70°C for 5 hours, and then at 100-120°C for 4 hours;

[0022] (4) Calcination: The material obtained aft...

Embodiment 2

[0024] Embodiment 2 The preparation method of low-temperature SCR denitration catalyst comprises the following process steps:

[0025] (1) Preparation of ammonium metavanadate solution: weigh 12.9g of ammonium metavanadate, stir and dissolve the weighed ammonium metavanadate in 8g of ethanolamine aqueous solution at 70-90°C, the concentration of the aqueous solution of ethanolamine is 3g / mL ;

[0026] (2) Preparation of metal salt solution: Dissolve 12.6g of cerium nitrate in 120g of water;

[0027] (3) Mixing: Weigh 85g of titanium-tungsten powder, add the metal salt solution obtained in step (2) to it, heat to 70-90°C, keep stirring at a constant temperature until the water evaporates to dryness, and then add The ammonium metavanadate solution obtained in step (1) was heated to 70-90°C, kept at a constant temperature while stirring evenly until the water was evaporated to dryness, and a solid was obtained;

[0028] (4) Drying: drying the solid finally obtained in step (3) ...

Embodiment 3

[0031] Embodiment 3 The preparation method of low-temperature SCR denitration catalyst comprises the following process steps:

[0032] (1) Preparation of ammonium metavanadate solution: weigh 9.0 g of ammonium metavanadate, stir and dissolve the weighed ammonium metavanadate in 4 g of ethanolamine aqueous solution at 70-90 °C, the concentration of ethanolamine aqueous solution is 5 g / mL ;

[0033] (2) Mixing: Weigh 93g of titanium-tungsten powder, add the metal salt solution obtained in step (2) into it, heat to 70-90°C, keep stirring at a constant temperature until the water is evaporated to dryness, and then add The ammonium metavanadate solution obtained in step (1) was heated to 70-90°C, kept at a constant temperature while stirring evenly until the water was evaporated to dryness, and a solid was obtained;

[0034] (4) Drying: drying the solid finally obtained in step (3) at 50-70°C for 6 hours, and then at 100-120°C for 5 hours;

[0035] (5) Calcination: The material o...

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PUM

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Abstract

The invention relates to a method for preparing a low-temperature SCR (selective catalytic reduction) denitration catalyst, and belongs to the technical field of catalysis. The denitration catalyst has a good nitric oxide removal rate, water resistance and sulfur resistance when the temperature of flue gas ranges from 150 DEG C to 250 DEG C. The method includes dissolving ammonium metavanadate, transition metal salts and titanium and tungsten powder in water; and drying and calcining the mixed liquor to prepare the low-temperature SCR denitration catalyst. The prepared catalyst is good in low-temperature activity, and can keep the good nitric oxide removal rate, the water resistance and the sulfur resistance at the temperature ranging from 150 DEG C to 250 DEG C. In addition, owing to the high activity and poison resistance at the temperature ranging from 150 DEG C to 250 DEG C, the catalyst can be applied to the field of flue gas after the flue gas flows via dust catchers of thermal power plants and flue gas, with the temperature ranging from 150 DEG C to 250 DEG C, of industrial furnaces and the like, and denitration catalyst technology and application breakthrough is realized.

Description

technical field [0001] The invention relates to a preparation method of a low-temperature SCR denitration catalyst. The denitration catalyst still has good nitrogen oxide removal rate and water and sulfur resistance performance at a flue gas temperature of 150-250° C., and belongs to the technical field of catalysis. Background technique [0002] During the "Twelfth Five-Year Plan" period, the country's control over nitrogen oxide emissions has become more and more stringent, and pure low-nitrogen combustion technology can no longer meet the requirements of current emission standards. Selective catalytic reduction (SCR) technology is due to its efficient and reliable denitrification Performance has begun to be applied in domestic coal-fired power plants. The main principle of SCR is based on NH 3 As a reducing agent, under the action of denitrification catalyst, NO x reduced to N 2 . [0003] At present, vanadium-tungsten-titanium catalyst is the most widely used. Due to...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/888B01J23/30B01D53/90B01D53/56
Inventor 王仁虎彭光军肖雨亭
Owner JIANGSU LONGYUAN CATALYST CO LTD
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