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Method for improving low-temperature activity of coal ash-attapulgite manganese based selective catalytic reduction (SCR) catalyst

A SCR catalyst, manganese-based technology of protruding rods, applied in the direction of catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., to achieve the effects of diameter expansion, reduction of active component content, and opening and expansion of pores

Inactive Publication Date: 2014-08-06
HEFEI UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The present invention aims to provide an acid treatment method for improving the low-temperature activity of fly ash-attapulgite manganese-based SCR catalysts. 150℃) denitrification efficiency

Method used

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  • Method for improving low-temperature activity of coal ash-attapulgite manganese based selective catalytic reduction (SCR) catalyst
  • Method for improving low-temperature activity of coal ash-attapulgite manganese based selective catalytic reduction (SCR) catalyst
  • Method for improving low-temperature activity of coal ash-attapulgite manganese based selective catalytic reduction (SCR) catalyst

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] In this embodiment, the preparation process of fly ash-attapulgite manganese-based SCR catalyst is as follows:

[0032] 1. Preparation of composite carrier

[0033] Take fly ash and attapulgite at a mass ratio of 1:1, pulverize and mix uniformly to obtain particles with a particle size of 0.38-0.83mm, and place the particles in an air atmosphere at 300°C for 3 hours to obtain a composite carrier FA- PG.

[0034] 2. Preparation of pickling solution

[0035] Using CH with a mass concentration ≥ 99.5% 3 Preparation of COOH solution [H + ]=1.2mol / L pickling solution.

[0036] 3. Pickling pretreatment

[0037] Take 10g of FA-PG, and test the saturated water absorption of the composite carrier (impregnation solid-liquid ratio) by equal volume impregnation method: 0.8mL / g;

[0038] Take 20g of FA-PG and immerse it into the pickling solution prepared in step 2 according to the impregnation solid-to-liquid ratio, and let it stand for 12 hours; divide the pickling-treated c...

Embodiment 2

[0046] In this embodiment, the preparation process of fly ash-attapulgite manganese-based SCR catalyst is as follows:

[0047] 1. Preparation of composite carrier

[0048] The preparation method of step 1 is the same as embodiment 1.

[0049] 2. Preparation of pickling solution

[0050] Respectively use H with a mass concentration of 95-98% 2 SO 4 Sulfuric acid, nitric acid solution with a mass concentration of 65%, CH with a mass concentration ≥ 99.5% 3 Preparation of COOH solution and HCl solution with a mass concentration of 36-38% [H + ]=1.2mol / L pickling solution, and recorded as pickling solution 1, pickling solution 2, pickling solution 3 and pickling solution 4 in sequence.

[0051] 3. Pickling pretreatment

[0052] Take 10g of FA-PG, and test the saturated water absorption of the composite carrier (impregnation solid-liquid ratio) by equal volume impregnation method: 0.8mL / g;

[0053] Take four equal parts of FA-PG, respectively immerse in pickling solution 1, ...

Embodiment 3

[0060] 1. Preparation of composite carrier

[0061] The preparation method of step 1 is the same as embodiment 1.

[0062] 2. Preparation of pickling solution

[0063] Using CH with a mass concentration ≥ 99.5% 3 COOH solution was prepared separately [H + ]=0, 0.6, 1.2, 1.8, 2.4, 3, 4 and 5 mol / L pickling solutions, which are sequentially recorded as pickling solution a, pickling solution b, pickling solution c, pickling solution d, pickling solution Solution e, pickling solution f, pickling solution g and pickling solution h.

[0064] 3. Pickling pretreatment

[0065] Take 10g of FA-PG, and test the saturated water absorption of the composite carrier (impregnation solid-liquid ratio) by equal volume impregnation method: 0.8mL / g;

[0066] Take eight equal parts of FA-PG, dip them into the pickling solution a-h prepared in step 2 respectively according to the solid-to-liquid ratio of immersion, let it stand for 12 hours, take it out, dry it at 50°C for 2 hours, and then dr...

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Abstract

The invention discloses a method for improving low-temperature activity of a fly ash-attapulgite manganese based selective catalytic reduction (SCR) catalyst. The method includes a composite carrier preparation process, a catalyst loading process and an aftertreatment process of units, an acid-washing pre-treatment process is added after the composite carrier preparation process and before the acid-washing pre-treatment process, the acid-washing pre-treatment is that a composite carrier is immersed into an acid-washing liquid for standing for 11-13 hours, then the composite carrier is taken out to be dried for 2 hours at the temperature of 50 DEG C and then dried for 12 hours at the temperature of 110 DEG C to obtain the composite carrier which is subjected to the acid-washing pre-treatment, and [H+] in the acid-washing liquid is equal to 0.3-5 mol / L. The method is capable of obviously improving the denitration activity of the catalyst at the window with low temperature of 100-200 DEG C, the treatment method is simple and easy to achieve, the costs of used materials and processes are low, and the method is good in actual application values.

Description

1. Technical field [0001] The invention relates to the nitric oxide treatment of coal-burning flue gas in the field of environmental protection technology, in particular to an acid treatment method for improving the low-temperature SCR denitrification performance of fly ash-attapulgite manganese-based catalysts 2. Background technology [0002] Nitrogen oxides (NOx) are one of the main pollutants emitted during the combustion of fossil fuels, especially coal. It not only endangers human health, but also causes serious environmental problems such as acid rain and photochemical smog. Therefore, the control of NOx has always been a national priority. The focus of the research. Currently in NH 3 The Selective Catalytic Reduction (SCR) process for the reduction of NOx has been widely used. In SCR technology, the catalyst is the core, and the most mature industrial SCR catalyst in foreign countries is based on V 2 o 5 / TiO 2 , V 2 o 5 -WO 3 / TiO 2 , and its working temper...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/34B01J37/06B01D53/90B01D53/56
Inventor 张先龙贾小彬吴雪平张翠平杨保俊王百年
Owner HEFEI UNIV OF TECH