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A kind of SCR denitration catalyst and preparation method thereof

A technology of SCR catalyst and denitration catalyst, which is applied in the field of SCR denitration catalyst and its preparation, can solve the problems of insufficient commercial application of vanadium-based denitration catalyst, and achieve the effects of moderate strength, low preparation cost and improved economic benefits.

Active Publication Date: 2019-06-07
SICHUAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] The object of the present invention is to provide a kind of SCR denitration catalyst and its preparation method, aiming at solving the above-mentioned problem that the current vanadium-based denitration catalyst is insufficient in commercial application

Method used

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  • A kind of SCR denitration catalyst and preparation method thereof
  • A kind of SCR denitration catalyst and preparation method thereof
  • A kind of SCR denitration catalyst and preparation method thereof

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preparation example Construction

[0029] Such as figure 1 Shown, the preparation method of the SCR denitration catalyst of the embodiment of the present invention comprises the following steps:

[0030] S101: Preparation of the mixture: disperse the pottery clay, component 1 and component 2 in the solution solvent, and mix uniformly;

[0031] S102: Forming and drying: put the mixture into a mold, press and form it, and dry it at 110°C for 12 hours;

[0032] S103: Calcination: the dried product is calcined at high temperature for 2 hours, taken out and cooled, crushed and sieved to a particle size of 10-20 mesh;

[0033] S104: pickling treatment: soak the obtained crushed material in nitric acid solution at 80°C for 2 hours, rinse with deionized water until neutral, and dry;

[0034] S105: Preparation of the mixed solution: dissolving the precursor substances of manganese and cerium metals in a certain aqueous solution, stirring and mixing;

[0035] S106: mixing: soak the dried substance described in step S1...

Embodiment 1

[0047]Disperse clay, sodium silicate, and coal powder in water solvent according to the mass ratio of 50%: 15%: 35%. After ball milling and mixing evenly, put it into a mold (8mm in diameter) and press it under 10MPa, and place it in an oven at 110°C. Dry in medium for 12h. After drying, the sample was placed in an atmosphere furnace, calcined at 1000°C for 2 hours under the protection of nitrogen atmosphere, cooled to room temperature, crushed and sieved to 10-20 mesh. Soak the crushed sample in 50% nitric acid solution, heat at 80°C for 2h, rinse with deionized water until neutral, and dry at 110°C. Mix a certain amount of manganese nitrate and cerium nitrate to obtain a precursor solution, soak the acid-treated sample in the precursor solution, let it stand for 24 hours, dry it in a water bath at 60°C, dry it at 110°C for 12 hours, and place it under a nitrogen atmosphere at 400°C After calcination for 2 hours, the SCR catalyst was obtained. In the obtained SCR catalyst, ...

Embodiment 2

[0049] Disperse the clay, sodium silicate and coal powder in the water solvent according to the mass ratio of 60%: 15%: 25%. After the ball mill is mixed evenly, put it into a mold (8mm in diameter) and press it under 10MPa, and place it in an oven at 110°C. Dry in medium for 12h. After drying, the sample was placed in an atmosphere furnace, calcined at 1000°C for 2 hours under the protection of nitrogen atmosphere, cooled to room temperature, crushed and sieved to 10-20 mesh. Soak the crushed sample in 30% nitric acid solution, heat at 80°C for 2h, rinse with deionized water until neutral, and dry at 110°C. Mix a certain amount of manganese nitrate and cerium nitrate to obtain a precursor solution, soak the acid-treated sample in the precursor solution, let it stand for 24 hours, Ce is 10%, 60 ° C water bath drying, 110 ° C drying for 12 hours, 400 °C under nitrogen atmosphere for 2 h to obtain the SCR catalyst. In the obtained SCR catalyst, the proportion of Mn is 7%, and ...

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Abstract

The invention discloses an SCR denitration catalyst and a preparation method thereof. The SCR denitration catalyst includes potter's clay, a component 1, and a component 2. The ratio of potter's clay to the component 1 to the component 2, by mass percentage, is 45-60%:25-40%:15%. The catalyst is excellent in denitration efficiency and sulfur resistance at the flue-gas temperature of 120-240 DEG C, is low in cost and simple in preparation process, and can be used for low-temperature denitration after dedusting or dedusting desulfuration of flue gas treatment in a coal-fired power plant such as a thermal power plant. Compared with V2O5-WO3 / TiO2 sold in the market, the SCR catalyst is free of poisonous vanadium component and excellent in low-temperature (120-240 DEG C) activity. The catalyst takes low-cost resourceful potter's clay as a raw material, is low in preparation cost and simple in process, and is suitable for industrial mass production. The catalyst can bring economic benefit to industrial enterprises, and has bright application prospects in the field of denitration of industrial flue gas.

Description

technical field [0001] The invention belongs to the technical field of environmental protection, and in particular relates to an SCR denitration catalyst and a preparation method thereof. Background technique [0002] The energy structure dominated by coal has caused a large consumption of coal resources in my country. In flue gas from coal combustion, NO X It can cause environmental problems such as acid rain, photochemical smog and ground ozone, so it has become one of the key control objects in air pollutants. In recent years, the State Council's "12th Five-Year Plan for Energy Conservation and Emission Reduction" has vigorously promoted clean production for coal-fired industrial enterprises such as electric power; in July 2014, China's new standard for thermal power air pollution emissions - "Emission Standards for Air Pollutants for Thermal Power Plants" ( GB13223—2011) the emission requirement of nitrogen oxides is changed from 650mg / m 3 Increased to 100mg / m 3 . T...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/34B01D53/86B01D53/56
CPCB01D53/8628B01J23/34
Inventor 李建军张序刘勤刘勇军郭家秀楚英豪覃丽萍岑望来
Owner SICHUAN UNIV