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Method for preparing selective catalytic reduction (SCR) denitration catalyst by taking TiO2-ZnO as composite carrier

A technology of denitrification catalyst and composite carrier, which is applied in the field of selective catalytic reduction denitrification catalyst, can solve the problems of high cost, restricting the promotion and application of manganese-titanium system SCR catalyst, and high price, and achieves low cost, high low temperature activity and low cost Effect

Active Publication Date: 2014-07-02
BEIJING UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Although the currently used manganese-titanium system SCR catalyst has better low-temperature denitrification activity and is suitable for tail gas treatment of cement kilns, but TiO 2 The high cost of the carrier leads to the high price of the catalyst product of this system, which restricts the promotion and application of the manganese-titanium system SCR catalyst in the field of denitrification of cement tail gas

Method used

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  • Method for preparing selective catalytic reduction (SCR) denitration catalyst by taking TiO2-ZnO as composite carrier

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] A TiO 2 -ZnO is the preparation of the SCR denitration catalyst of the composite carrier comprising the following steps:

[0019] Add 14.40g of titanyl sulfate, 2.97g of zinc nitrate, 9.80g of manganese acetate, and 3.04g of cerium nitrate into 200mL of distilled water, and stir magnetically for 0.5h in a water bath at 60°C; Add it dropwise to the above solution, and add 50mL of 30% hydrogen peroxide solution dropwise to the solution, and continue to stir for 1h until the precipitate is completely formed; wash the separated precipitate twice with distilled water and absolute ethanol, and place it in an evaporating dish Put it in a drying oven at 70°C for 12 hours. The dried samples were ground and calcined at 450 °C for 4 h.

[0020] Denitrification rate test conditions: 1000ppmNO, 1000ppmNH 3 , 5%O 2 , N 2 As the carrier gas, the gas flow rate is 2000mL / min, and the space velocity is 27000h -1 . Under these conditions, the denitrification rate of the catalyst is...

Embodiment 2

[0022] A TiO 2 -ZnO is the preparation of the SCR denitration catalyst of the composite carrier comprising the following steps:

[0023] Add 11.20g of titanyl sulfate, 8.92g of zinc nitrate, 12.25g of manganese acetate, and 3.47g of cerium nitrate into 250mL of distilled water, stir magnetically for 0.5h in a water bath at 60°C; add 500mL (0.5mol / L) of sodium hydroxide The solution was added dropwise to the above solution, and 50mL of 30% hydrogen peroxide solution was added dropwise to the solution, and the stirring was continued for 1h until the precipitate was completely formed; the separated precipitate was washed twice with distilled water and absolute ethanol, and placed in the evaporation Place in a drying oven at 70°C for 12 hours. The dried samples were ground and calcined at 450 °C for 4 h.

[0024] Denitrification rate test conditions: 1000ppmNO, 1000ppmNH 3 , 5%O 2 , N 2 As the carrier gas, the gas flow rate is 2000mL / min, and the space velocity is 27000h -1 ...

Embodiment 3

[0026] A TiO 2 -ZnO is the preparation of the SCR denitration catalyst of the composite carrier comprising the following steps:

[0027] Add 9.60g of titanyl sulfate, 11.90g of zinc nitrate, 20.01g of manganese nitrate, and 2.98g of cerium trichloride into 300mL of distilled water, stir magnetically for 0.5h in a water bath at 80°C; Potassium solution was added dropwise to the above solution, and 60 mL of 30% hydrogen peroxide solution was added dropwise to the solution, and the stirring was continued for 1.5 h until a precipitate was completely formed; the separated precipitate was washed 3 times with distilled water and absolute ethanol respectively, and placed in In an evaporating dish, put it in a drying oven at 90°C for 10 hours. The dried samples were ground and calcined at 550 °C for 3 h.

[0028] Denitrification rate test conditions: 1000ppmNO, 1000ppmNH 3 , 5%O 2 , N 2 As the carrier gas, the gas flow rate is 2000mL / min, and the space velocity is 27000h -1 . Un...

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Abstract

The invention discloses a method for preparing a selective catalytic reduction (SCR) denitration catalyst by taking TiO2-ZnO as a composite carrier and belongs to the field of environmental catalytic materials. The method is characterized by comprising the following steps: respectively adding a titanium salt, a zinc salt, a manganese salt and a cerium salt into distilled water, magnetically stirring in a water bath at the temperature of 60-80 DEG C for 0.5-1 hour, dissolving, mixing and obtaining a precursor solution; dropwise adding a strong base solution with the concentration of 0.5-1.5mol / L into the precursor solution in the previous step, stirring in the water bath at the temperature of 60-80 DEG C, adding hydrogen peroxide with the mass percent of 30 percent, stirring for 1-2 hours until precipitation is complete; centrifuging, separating and washing the precipitate, drying under the condition of 450-600 DEG C and calcining for 2-5 hours. The prepared catalyst is high in low-temperature activity and low in cost. The denitration rate can be over 95 percent under the catalytic reaction conditions comprising 1000ppm NO, 1000ppm NH3, 5 percent of O2, carrier gas of N2, gas flow rate of 2000mL / min and air speed of 27000h-1.

Description

technical field [0001] The invention belongs to the field of environmental catalytic materials, in particular to a TiO 2 -ZnO is a composite carrier suitable for selective catalytic reduction (SCR) denitrification catalyst for cement kiln flue gas denitrification. Background technique [0002] Nitrogen oxides (NO X ) as one of the main pollutants of the atmosphere, including N 2 O, NO, NO 2 , N 2 o 3 , N 2 o 4 and N 2 o 5 Etc., its emission will cause problems such as acid rain, greenhouse effect and ozone depletion, which will cause serious harm to human beings and the ecological environment. The main pollutant in the tail gas of cement kiln is NO X and dust, of which NO X It mainly comes from nitrogen in high temperature fuel and nitrogen-containing compounds in raw materials. According to the data of the first national survey of pollution sources in 2007, the new dry process cement kiln NO X The average emission is 1100mg / Nm 3 . Therefore, the NO in the tai...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/34B01J32/00B01J35/10B01D53/56B01D53/86
Inventor 郭红霞吴晨光崔素萍马晓宇张良静项泽强田国兰
Owner BEIJING UNIV OF TECH