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Determination method of denitration rate of nano titanium dioxide powder for flue gas denitration catalyst

A technology of nano-titanium dioxide and denitration catalyst is applied in the field of preparation of nano-titanium dioxide, which can solve the problems of inability to establish connection between denitrification catalysts and denitration activities, and achieve the effects of stable test results, easy operation and simple test.

Pending Publication Date: 2021-11-16
安徽迪诺环保新材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The technical problem to be solved by the present invention is that the existing identification of the performance of nano-titanium dioxide powder for denitrification catalysts is to directly detect various parameters through instruments, and it is impossible to determine the performance of nano-titanium dioxide powder for denitrification catalysts and the performance of denitrification catalysts. To establish a connection between the activity and the denitration rate of nano-titanium dioxide powder for flue gas denitrification catalyst, which can establish the relationship between the performance of nano-titanium dioxide powder for denitration catalyst and the denitration activity of denitration catalyst

Method used

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  • Determination method of denitration rate of nano titanium dioxide powder for flue gas denitration catalyst
  • Determination method of denitration rate of nano titanium dioxide powder for flue gas denitration catalyst
  • Determination method of denitration rate of nano titanium dioxide powder for flue gas denitration catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] (1) Powder prefabrication: Take two 10g samples from different sources with a specific surface area of ​​82.56m 2 / g denitrification catalyst with nano-titanium dioxide, add 0.14g ammonium metavanadate, 0.32g ammonium heptamolybdate, 0.2g triethanolamine, 50ml distilled water to it respectively, put it into a constant temperature water bath with stirring, set the temperature at 70°C, Stir at constant temperature until it is semi-dry to obtain two parts of semi-dry materials; (2) Powder calcination: transfer the above two parts of semi-dry materials to a crucible, put them in a 500°C oven for calcination for 1 hour, and obtain two parts of calcined powder Materials; (3) Prefabrication of test samples: Cool the above two calcined materials to room temperature, put them into a mortar, add about 1% PEO, CMC, grind them, slowly add distilled water and grind them carefully until the materials are solidified. (4) Test sample pressing: put the above two agglomerated samples int...

Embodiment 2

[0020] Example 2: The difference from Example 1 is that the surface area of ​​nano-titanium dioxide for denitration catalyst in step (1) is 98.14m 2 / g. The test results are shown in Table 2:

[0021]

[0022] Tests 2-1, 2-2, and 2-3 in Table 2 have two groups, representing two different sources of nano-titanium dioxide for denitration catalysts. It can be seen that under the same sample length, the out-of-stock rate and unit length The out-of-stock rate of the samples is different, indicating that the performance of the two different sources of nano-titanium dioxide for denitration catalysts has an impact on the out-of-stock rate of the catalyst. Through data comparison, it can be seen which source of nano-titanium dioxide for denitration catalyst has better performance. Compared with the test results of Example 1, it can be found that the larger the specific surface area, the higher the denitrification rate of the catalyst.

Embodiment 3

[0023] Embodiment 3: The difference with Embodiment 1 is that 0.16g ammonium metavanadate is added in the step (1), and the test results are shown in Table 3:

[0024]

[0025] Tests 3-1, 3-2, and 3-3 in Table 3 have two groups respectively, representing two different sources of nano-titanium dioxide for denitration catalysts. It can be seen that in the case of the same sample length, the out-of-stock rate and unit length The out-of-stock rate of the samples is different, indicating that the performance of the two different sources of nano-titanium dioxide for denitration catalysts has an impact on the out-of-stock rate of the catalyst. Through data comparison, it can be seen which source of nano-titanium dioxide for denitration catalyst has better performance. Compared with the test results of Example 1, it can be found that the higher the loading of active components, the higher the denitration rate of the catalyst.

[0026] In the present invention, the nano-titanium dio...

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Abstract

The invention discloses a determination method of the denitration rate of nano titanium dioxide powder for a flue gas denitration catalyst. The method comprises the following steps of: mixing a certain amount of V2O5 / MoO3 and nano titanium dioxide for the denitration catalyst, and calcining the mixture; adding CMC and PEO to extrude the denitration nano titanium dioxide powder into a sample with a certain volume and shape; and pre-treating the sample at the high temperature of 300 DEG C, and detecting the denitration rate of the sample through a micro catalyst activity detection device. The method has the advantages of stable test result, high reproducibility and the like.

Description

technical field [0001] The invention relates to the field of preparation of nano-titanium dioxide, in particular to a method for measuring the denitration rate of nano-titanium dioxide powder used as a flue gas denitration catalyst. Background technique [0002] With the continuous increase of national environmental protection monitoring, combustion denitrification using SCR flue gas denitrification technology has made great progress. From the initial power industry, it has expanded to various industries that use coal or straw incineration, such as glass, steel, coke ovens, and ships. The research on denitrification catalysts has also achieved unprecedented development, and the application of denitrification catalysts has expanded from the initial active temperature range of 350-400 to 150-200 degrees. From the initial vanadium-titanium system, the SCR denitrification catalytic system with many active components such as rare earth system and manganese system has been develo...

Claims

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Application Information

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IPC IPC(8): G01N31/10
CPCG01N31/10
Inventor 钱笑雄钱邦正赵义凯
Owner 安徽迪诺环保新材料科技有限公司