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Low-temperature denitrification catalyst and preparation method thereof

A low-temperature denitrification and catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems of low denitrification activity, poor resistance to water and sulfur dioxide, etc., and achieve good nitrogen selectivity, Strong water and sulfur dioxide resistance, high denitrification activity

Inactive Publication Date: 2019-11-19
上海毅帆环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The first aspect of the present invention is to provide a low-temperature denitration agent to solve the main problems of the denitration catalysts in the prior art, such as low denitration activity at low temperature, poor water resistance and sulfur dioxide resistance, etc.

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Embodiment 1

[0042] Embodiment 1, the preparation of low-temperature denitration catalyst A

[0043] The preparation of the low-temperature denitration catalyst of this embodiment, the specific steps are as follows:

[0044] (1), the cerium precursor cerium nitrate of 8.68g, the neodymium precursor neodymium nitrate hexahydrate of 8.77g and 34.03g butyl titanate are dissolved with 100ml deionized water respectively, obtain cerium precursor solution, neodymium precursor solution and titanium precursor solution.

[0045] (2) Fully mix the metal precursor solution in step (1) to obtain a mixed precursor solution, and add 17.58 g of urea and stir for 1 hour to make the stirring uniform, and obtain a catalyst combustion liquid.

[0046] (3), the catalyst combustion solution in step (2) is placed in a ceramic crucible, slowly heated to 250 ° C in an air atmosphere, and maintained at this temperature for 2 hours, to obtain the initial product;

[0047] (4) The initial product of step (3) was calc...

Embodiment 2

[0049] Embodiment 2, the preparation of low-temperature denitration catalyst B

[0050] The preparation of the low-temperature denitration catalyst of this embodiment, the specific steps are as follows:

[0051] (1), the cerium precursor cerium nitrate of 8.68g, the neodymium precursor neodymium nitrate hexahydrate of 13.15g and 34.03g butyl titanate are dissolved with 100ml deionized water respectively, obtain cerium precursor solution, neodymium precursor solution and titanium precursor solution.

[0052] (2) Fully mix the metal precursor solution in step (1) to obtain a mixed precursor solution, add 18.73 g of urea and stir for 1 hour to make the stirring uniform, and obtain a catalyst combustion liquid.

[0053] (3), the catalyst combustion solution in step (2) is placed in a ceramic crucible, slowly heated to 300°C in an air atmosphere, and maintained at this temperature for 1h, to obtain the initial product;

[0054] (4) The initial product of step (3) was calcined at ...

Embodiment 3

[0056] Embodiment 3, the preparation of low-temperature denitration catalyst C

[0057] The preparation of the low-temperature denitration catalyst of this embodiment, the specific steps are as follows:

[0058] (1), 8.68g of cerium precursor cerium nitrate, 17.53g of neodymium precursor neodymium nitrate hexahydrate and 24g of titanium sulfate were dissolved in 100ml deionized water respectively to obtain cerium precursor solution, neodymium precursor solution and titanium precursor solution .

[0059] (2) Fully mix the metal precursor solution in step (1) to obtain a mixed precursor solution, add 17.51 ​​g of urea and stir for 1 hour to make the stirring uniform, and obtain a catalyst combustion liquid.

[0060] (3) Place the catalyst combustion solution in step (2) in a ceramic crucible, slowly heat to 350°C in an air atmosphere, and maintain the temperature for 0.5h to obtain the primary product;

[0061] (4) The initial product of step (3) was calcined at 400°C for 6 ho...

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Abstract

The invention discloses a low-temperature denitrification catalyst, which comprises a carrier and active components supported on the carrier, wherein the carrier is titanium dioxide, the active components are cerium and neodymium, and a molar ratio of cerium to neodymium to titanium is (0.1-0.3):(0.2-0.4):1. The invention further discloses a preparation method of the low-temperature denitrification catalyst, wherein the preparation method comprises: respectively dissolving formula amounts of cerium nitrate, neodymium nitrate and a titanium source with deionized water, completely mixing to obtain a mixed precursor solution, adding 4-6 wt% of urea, and stirring uniformly to obtain a catalyst combustion liquid; slowly heating the catalyst combustion liquid to a temperature of 250-400 DEG C inan air atmosphere, and maintaining the temperature for 0.5-2 h to obtain an initial product; and calcining the initial product for 4-6 h at a temperature of 400-550 DEG C to obtain the low-temperature denitrification catalyst. According to the present invention, the prepared low-temperature denitrification catalyst has characteristics of high denitrification activity, good nitrogen selectivity, strong water resistance, and strong sulfur dioxide resistance; and the preparation method has characteristics of simplified preparation process, low energy consumption, high utilization rate, environment protection and no pollution.

Description

technical field [0001] The invention belongs to the technical field of flue gas denitrification, and in particular relates to a low-temperature denitrification catalyst and a preparation method thereof. Background technique [0002] In the prior art, for NO in stationary source flue gas x An effective method for the removal of is to use NH 3 For selective catalytic reduction (SCR), the mainstream commercial catalyst used in the SCR reaction is V 2 o 5 -WO 3 / TiO 2 . Although catalyst V 2 o 5 -WO 3 / TiO 2 It has high activity and high sulfur resistance, but there are still some problems: [0003] (1) The cost of catalyst is high, resulting in high cost of denitrification. [0004] (2) The operating temperature must be higher than 623K (about 350°C). Since the temperature of the flue gas decreases after dedusting and desulfurization, it cannot reach the catalyst V 2 o 5 -WO 3 / TiO 2 Therefore, the SCR reaction bed must be arranged before the air preheater, dust...

Claims

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Application Information

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IPC IPC(8): B01J23/10B01J35/10B01D53/86B01D53/56
CPCB01J23/10B01J23/002B01D53/8628B01D53/56B01D2257/404B01D2258/0283B01J35/60
Inventor 彭皓朱双波郭瑞堂
Owner 上海毅帆环保科技有限公司