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Honeycombed SCR (selective catalytic reduction) denitrification catalyst for low-temperature flue gas denitrification and preparation method thereof

A denitrification catalyst and low-temperature flue gas technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of low NO conversion rate and easy falling off of active substances, etc. problems, to achieve the effect of increasing acidic adsorption sites, good flexibility and plasticity, and high denitrification efficiency

Active Publication Date: 2013-01-09
ZHEJIANG TIANLAN ENVIRONMENTAL PROTECTION TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, since the active material is loaded by impregnation, the active material is easy to fall off
The patent with application number 200510031743.6 uses TiO 2 It is a carrier, and the active components are oxides of Mn and variable valence metal iron or copper or vanadium or cerium or chromium, and the activity is close to 100% at 120 ° C, but the catalyst prepared by this method is granular and has great potential in industrial applications. big limitations
Patent application number 201010559955.2 to load TiO 2 -SiO 2 The coated cordierite honeycomb ceramic is used as the carrier, and the active components are oxides of Mn, Fe, Ce, Zr, W and other elements. 54.4%

Method used

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  • Honeycombed SCR (selective catalytic reduction) denitrification catalyst for low-temperature flue gas denitrification and preparation method thereof
  • Honeycombed SCR (selective catalytic reduction) denitrification catalyst for low-temperature flue gas denitrification and preparation method thereof
  • Honeycombed SCR (selective catalytic reduction) denitrification catalyst for low-temperature flue gas denitrification and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] 1) Dry mixing of carrier and solid powder. Weigh titanium tungsten powder 480.00g, titanium silicon powder 120.00g, manganese acetate 209.80g, cerium nitrate 41.96g, ferrous oxalate 20.98g, zirconium nitrate 20.98g, stearic acid 1.80g, zirconium nitrate and nitric acid after drying Cerium and manganese acetate were ground into powder, and put into a mixer for dry mixing for 20 minutes.

[0032] 2) Add acid, lye and water for conditioning. Measure 5.97g of lactic acid with a concentration of 85%, dilute it to 20g with water, add it to the uniformly mixed solid powder, stir for 10 minutes, and then add 51.47g of ammonia water with a concentration of 25%. 3) Add structural aids and water to adjust strength and structure. Add 48.70g of glass fiber and 4.40g of pulp cotton, after stirring for 15min, slowly add 7.34g of monoethanolamine and 63g of glycerin, continue stirring for 20min, then add 70g of distilled water step by step according to the principle of small amounts ...

Embodiment 2

[0038] 209.80g manganese acetate in embodiment 1 is replaced by 104.90g, 41.96g cerium nitrate is replaced by 20.98g, 5.97g lactic acid is replaced by 11.94g under the same concentration, 51.47g ammoniacal liquor is replaced by 64.34g under the same concentration, 70g distilled water Replaced with 96g, other steps are identical to make catalyst finished product. Under the same conditions, the measured NO conversion rate was 90.53%, and the axial and transverse mechanical strengths were 527.1N / cm and 135.2N / cm, respectively.

Embodiment 3

[0040] The 41.96g cerium nitrate in embodiment 1 is replaced by 33.25g cerium oxide, 5.97g lactic acid is replaced by 17.91g under the same concentration, diluted to 30g, 51.47g ammonia water is replaced by 77.20g under the same concentration, and 70g distilled water is replaced by 66g, other steps are identically made catalyst finished product. Under the same conditions, the measured NO conversion rate was 95.02%, and the axial and transverse mechanical strengths were 542.9N / cm and 144.2N / cm, respectively.

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Abstract

The invention discloses a honeycombed SCR (selective catalytic reduction) denitrification catalyst for low-temperature flue gas denitrification and a preparation method of the honeycombed SCR denitrification catalyst. According to the method, mixed powder of nano-anatase titanium tungsten powder and titanium silicon powder is used as a carrier of the catalyst; active components include metal compounds containing manganese, cerium, iron and zirconium; additives include an acid solution, an alkali solution, a structural promoter and a binder; and the honeycombed SCR denitrification catalyst, based on 100 parts of carrier, is prepared by the following raw materials by mass: 100 parts of carrier, 3-10 parts of manganese-containing precursor based on manganese, 1-6 parts of cerium-containing precursor based on cerium, 1-6 parts of iron-containing precursor based on iron, 0.5-8 parts of zirconium-containing precursor based on zirconium, 0.8-3 parts of acid solution, 5-15 parts of alkali solution, 11-29 parts of structural promoter, 1-6 parts of binder, and 13-26 parts of water. According to the catalyst prepared by the preparation method provided by the invention, the low-temperature (at 80-120 DEG C) activity of the SCR denitrification catalyst is effectively improved, and the strength and the molding rate of the monolithic honeycombed SCR denitrification catalyst are greatly improved.

Description

technical field [0001] The invention relates to the technical field of nitrogen oxide treatment, in particular to a honeycomb SCR denitration catalyst with high catalytic activity at low temperature and a preparation method thereof. Background technique [0002] Nitrogen oxides (NOx) are key pollutants to achieve multi-environmental objectives and comprehensively improve the quality of the atmospheric environment. They can cause acid deposition, trigger photochemical smog, accelerate the greenhouse effect, and seriously endanger human health. At present, my country's total NOx emissions have exceeded 18 million tons. If effective control measures are not taken, it is expected that my country's NOx emissions will increase rapidly in the next ten years, and will reach more than 30 million tons by 2020, which will undoubtedly become the world's No. A major NOx emitter. [0003] Among the numerous flue gas denitrification methods, selective catalytic reduction (SCR) technology i...

Claims

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Application Information

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IPC IPC(8): B01J23/889B01J35/04B01D53/90B01D53/56
Inventor 王岳军王瑞洋莫建松刘伟虞廷兴
Owner ZHEJIANG TIANLAN ENVIRONMENTAL PROTECTION TECH
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