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Flue gas denitration catalyst and preparation method and application thereof

A denitration catalyst, catalyst technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc., can solve environmental hazards, narrow activity temperature window, catalyst carrier and activity Due to the high price of components and raw materials, the effects of good anti-poisoning performance, wide active temperature window and good anti-poisoning performance are achieved.

Active Publication Date: 2011-08-31
SHANDONG GEMSKY ENVIRONMENTAL PROTECTION TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, the catalyst carrier and active component raw materials described in the patent (CN 101069855A) are relatively expensive; the catalyst described in the patent (CN 1724149A) has good activity but a narrow activity temperature window, and it has good SCR only when it is above 100°C Denitrification activity; the catalyst described in the patent (CN 101468314A) is added with highly toxic vanadium oxide, which will cause environmental harm in both production and recycling

Method used

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  • Flue gas denitration catalyst and preparation method and application thereof
  • Flue gas denitration catalyst and preparation method and application thereof
  • Flue gas denitration catalyst and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] Raw material preparation and calculation:

[0032] Weigh the mass of the carrier, measure the total pore volume of the carrier, and calculate the amount of the cocatalyst precursor and the catalytically active component precursor based on the total mass of the catalytically active component and the cocatalyst being 15% of the carrier mass.

[0033] Specific steps:

[0034] (1) Take the co-catalyst precursor according to the elemental molar ratio of Fe / Cu / Si 1:1:1: iron nitrate, copper nitrate and orthosilicic acid, mix and dissolve in deionized water with a volume equal to the total pore volume of the carrier, and use ammonia water Adjust the pH of the solution to be 5;

[0035] (2) Soak the honeycomb ceramic carrier in a citric acid aqueous solution with a mass percentage concentration of 15% for 48 hours, take it out and dry it, then immerse the honeycomb ceramic carrier in the solution obtained in step (1), let stand for 48 hours, filter out and air-dry;

[0036] (...

Embodiment 2

[0046] Raw material preparation and calculation:

[0047] Weigh the mass of the carrier, measure the total pore volume of the carrier, and calculate the amount of the cocatalyst precursor and the catalytically active component precursor based on the total mass of the catalytically active component and the cocatalyst being 30% of the carrier mass.

[0048] Specific steps:

[0049] (1) Take a certain amount of co-catalyst precursor: ferric nitrate, dissolve in deionized water with a volume equal to the total pore volume of the carrier, and adjust the pH of the solution to 7 with ammonia water;

[0050] (2) Soak the molecular sieve carrier in a dilute hydrochloric acid aqueous solution with a concentration of 20% by mass for 40 hours, take it out and dry it, then soak the molecular sieve carrier in the solution obtained in step (1), let it stand for 48 hours, filter out and air-dry;

[0051] (3) The solid obtained in step (2) is roasted at 800°C for 4h;

[0052] (4) Measure the...

Embodiment 3

[0058] Raw material preparation and calculation:

[0059] Weigh the mass of the carrier, measure the total pore volume of the carrier, and calculate the amount of the cocatalyst precursor and the catalytically active component precursor based on the total mass of the catalytically active component and the cocatalyst being 20% ​​of the carrier mass.

[0060] Specific steps:

[0061] (1) Take a certain amount of co-catalyst precursor: copper chloride, dissolve in deionized water with a volume equal to the total pore volume of the carrier, and adjust the pH of the solution to 6 with ammonia water;

[0062] (2) The activated carbon fiber carrier is soaked in the dilute nitric acid aqueous solution of 15% in mass percentage concentration for 24h, takes out and dries, then the activated carbon fiber carrier is soaked in the solution that step (1) obtains, let stand for 24h and then filter out and air-dry;

[0063] (3) The solid obtained in step (2) is roasted at 500°C for 6h;

[0...

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PUM

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Abstract

The invention discloses a flue gas denitration catalyst. The catalyst comprises a carrier and a catalytic activity component, wherein the catalytic activity component is manganese, cobalt and cerium composite oxide, wherein the molar ratio of the manganese element to the cobalt element to the cerium element is 1:0.1-1:0.1-1. A preparation method of the flue gas denitration catalyst comprises the following steps of: (1) taking a soluble manganese salt, a soluble cobalt salt and a soluble cerium salt, wherein the molar ratio of the manganese element to the cobalt element to the cerium element is 1:0.1-1:0.1-1, dissolving the salts in deionized water, and adding ammonia water to adjust the pH value to between 5 and 7; (2) soaking a carrier in aqueous solution of citric acid, diluted hydrochloric acid or diluted nitric acid for 24 to 48 hours, drying the carrier, soaking the carrier in the solution of the step (1), standing the carrier for 24 hours and drying the carrier; and (3) roastingthe prepared sample in step (2) in air, and cooling the sample. The flue gas denitration catalyst has the advantages of simple preparation method, high poisoning resistance, no secondary pollution toenvironment, wide activity temperature window, low activity starting temperature and the like.

Description

technical field [0001] The invention relates to a flue gas denitrification catalyst and its preparation and application. Background technique [0002] Nitrogen oxides mainly come from fuel combustion in industrial production (accounting for 90% of total human emissions) and transportation fuel combustion emissions, and some come from nitric acid plants, sulfuric acid plants, nitrogen fertilizer plants, fuel plants, pharmaceutical plants, etc. Enterprise emissions are one of the main sources of air pollution. With the continuous acceleration of my country's industrialization process, NO X Pollution is getting worse. In the Air Pollutant Emission Standards for Thermal Power Plants (Draft for Comment) promulgated in 2010, the state stipulates that 200mg / m 3 emission concentration limit. At the same time, during the "Twelfth Five-Year Plan" period, my country will increase energy conservation and emission reduction, increase denitrification (NO X Removal) this restrictive h...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/889B01D53/90B01D53/56
Inventor 祝社民张舒扬沈岳松卫平波沈树宝
Owner SHANDONG GEMSKY ENVIRONMENTAL PROTECTION TECH CO LTD
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