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Preparation method of ultramicroporous high-specific-area denitrification catalyst material

A technology of denitration catalyst and high specific surface area, which is applied in the field of preparation of ultra-microporous and high specific surface area denitration catalyst materials, can solve the problems of secondary pollution, crystal form conversion and high cost, limiting the wide application of V2O5/TiO2 catalyst, etc. The effect of increasing the contact area, avoiding the addition of active components by impregnation and repeated roasting

Inactive Publication Date: 2015-01-14
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The main core technology of this catalyst is monopolized by foreign companies or R&D institutions, and the toxicity of its component vanadium materials may cause secondary pollution. At the same time, due to the catalyst carrier anatase TiO 2 The wide application of V2O5 / TiO2 catalysts is limited due to easy crystal transformation and high cost.

Method used

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  • Preparation method of ultramicroporous high-specific-area denitrification catalyst material
  • Preparation method of ultramicroporous high-specific-area denitrification catalyst material
  • Preparation method of ultramicroporous high-specific-area denitrification catalyst material

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Experimental program
Comparison scheme
Effect test

Embodiment approach 1

[0021] Add 2g of fatty alcohol polyoxyethylene ether, 0.6g of citric acid and 0.18g of copper nitrate into 30mL of ethanol solution containing 2.0g of 12M hydrochloric acid, stir at room temperature to completely dissolve the surfactant, and simultaneously add 3.06g of iso Aluminum propoxide, after stirring at 35°C for 24 hours, the reaction mixture was poured into a Petri dish and treated at 55°C for 48 hours. Finally, the samples were fired at 400°C for 5 hours. The denitrification catalyst material was obtained, and nitrogen adsorption characterization showed that its micropore diameter was 1.48nm and the specific surface area was 593m 2 / g.

[0022] Catalyst Activity Test Method

[0023] 0.3 g of the catalyst passed through a 50-mesh sieve was loaded into a reaction tube, and the temperature was controlled by a tube-type resistance furnace program. The mixed gas simulates flue gas and is provided by the corresponding steel cylinder. The proportion (volume fraction) of ...

Embodiment approach 2

[0028] Add 2g of fatty alcohol polyoxyethylene ether, 0.55g of malic acid and 0.35g of copper sulfate into 20mL of ethanol solution containing 2.0g of 16M nitric acid, stir at room temperature to completely dissolve the surfactant, and simultaneously add 3.06g of iso Aluminum propoxide, after stirring at 30°C for 24 hours, the reaction mixture was poured into a Petri dish and treated at 60°C for 48 hours. Finally the samples were fired at 450°C for 5 hours. The denitrification catalyst material was obtained, and nitrogen adsorption characterization showed that its micropore diameter was 1.7nm, and its specific surface area was 552m 2 / g.

[0029] Catalyst Activity Test Method

[0030] 0.3 g of the catalyst passed through a 50-mesh sieve was loaded into a reaction tube, and the temperature was controlled by a tube-type resistance furnace program. The mixed gas simulates flue gas and is provided by the corresponding steel cylinder. The proportion (volume fraction) of the cor...

Embodiment approach 3

[0035]Add 1.5g fatty alcohol polyoxyethylene ether, 0.75g salicylic acid and 0.45g copper nitrate to 30mL ethanol solution containing 2.0g 16M nitric acid, stir at room temperature to completely dissolve the surfactant, and add 4.08 g to the system at the same time g aluminum isopropoxide, stirred at 35°C for 24 hours, poured the reaction mixture into a Petri dish and treated at 60°C for 48 hours. Finally the samples were fired at 450°C for 5 hours. The denitrification catalyst material was obtained, and nitrogen adsorption characterization showed that its micropore diameter was 1.7nm and the specific surface area was 561m 2 / g.

[0036] Catalyst Activity Test Method

[0037] 0.3 g of the catalyst passed through a 50-mesh sieve was loaded into a reaction tube, and the temperature was controlled by a tube-type resistance furnace program. The mixed gas simulates flue gas and is provided by the corresponding steel cylinder. The proportion (volume fraction) of the correspondin...

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Abstract

The invention relates to a preparation method of an ultramicroporous high-specific-area denitrification catalyst material, belonging to the field of inorganic catalyst flue gas denitrification. The preparation method is characterized in that the pore size of the catalyst is 1-2nm, the high specific area is 550-600 m<2> / g, copper oxide is used as an active component, and the molecular proportion of the copper oxide is not lower than 5%. The synthesis method comprises the following steps: dissolving nonionic surfactant, organic carboxylic acid, inorganic acid and copper salt in an ethanol solution containing deionized water according to the proportion of the synthetic material, and meanwhile, adding an aluminum source while stirring; and after continuing stirring for some time, carrying out heat treatment solvent volatilization and high-temperature roasting on the reactants to prepare the high-specific-area denitrification catalyst. The preparation technique is simple and feasible, low in cost and easy for industrial amplification, and has environment-friendly effect. The methane (CH4) used as the reducer has high denitrification activity within the temperature range from 400 to 600 DEG C; and when the reaction temperature is higher than 600 DEG C, and the conversion rate of NO is up to 100%.

Description

technical field [0001] The invention discloses a method for preparing an ultra-microporous high specific surface area denitration catalyst material, which belongs to the field of inorganic catalyst flue gas denitrification, and specifically relates to a pore diameter between 1 and 2 nm and a high specific surface area of ​​550-600 m 2 SCR flue gas denitrification catalyst with high denitrification efficiency, low cost, simple process, environmental protection and no secondary pollution, using copper oxide as the active component, and the molecular ratio of copper oxide content is not less than 5% and its preparation method. Background technique [0002] NOx is one of the common pollutants in the atmosphere. As a primary pollutant, NOx itself will cause harm to human health. It can irritate people's eyes, nose, throat and lungs, and easily cause people to suffer from respiratory diseases. What's more serious is that NOx will also produce a variety of secondary pollution,...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/72B01J35/10B01D53/90B01D53/56
Inventor 李瑞丰李永峰陈佳琪马静红苏娇娇潘大海于峰王晓燕王万绪杨效益宋鹏王国勇邰秀梅李国晋
Owner TAIYUAN UNIV OF TECH