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Nitrogen oxide removal process based on hydrogen peroxide catalytic oxidation

A technology of hydrogen peroxide and nitrogen oxides, applied in the direction of heterogeneous catalyst chemical elements, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of high-efficiency denitration and catalytic denitration Low capacity, immature technology for removing nitrogen oxides, etc., to achieve excellent catalytic performance, promote activation and decomposition, and save resources

Inactive Publication Date: 2017-06-20
NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in its practical application to remove nitrogen oxides from flue gas, the way to stimulate hydrogen peroxide to activate and decompose is mostly ultraviolet light irradiation, and the technology of using its gas-phase catalytic oxidation combined with liquid-phase absorption to remove nitrogen oxides is not mature enough. And the most commonly used catalysts such as FeOx and ZrOx show low catalytic denitrification ability in the low temperature range, making it difficult to achieve efficient denitrification

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Adopt above-mentioned technology, described hydrogen peroxide catalytic activation catalyst, its preparation process comprises the following steps:

[0027] (1) Weigh 468g of cerium nitrate hexahydrate, dissolve it in 5800mL of deionized water, and configure it into a solution; add the configured solution to 6000g of nano-anatase TiO 2 carrier, and mixed and stirred in a mixer;

[0028] (2) The catalyst paste mixed uniformly in step (1) is ultrasonically treated for 1 hour and left to stand for 2 hours, dried in a blast drying oven at 110°C for 2 hours, roasted in a muffle furnace at 550°C for 5 hours, and then pulverized to obtain a powder Hydrogen peroxide catalytically activates the catalyst. The percentages by weight of the active components of the catalyst and the carrier are respectively: 3.0% of cerium dioxide and 97.0% of titanium dioxide.

[0029] The process was evaluated using simulated flue gas conditions, with 10% hydrogen peroxide solution as the oxidant...

Embodiment 2

[0031] Adopt the device identical with embodiment 1 structure, described hydrogen peroxide catalytic activation catalyst, its preparation process comprises the following steps:

[0032] (1) Weigh 382g of cobalt nitrate hexahydrate, dissolve it in 1850mL of deionized water, and configure it into a solution; add the configured solution to 2000g of nano-anatase TiO 2 carrier, and mixed and stirred in a mixer;

[0033] (2) Ultrasonicate the catalyst paste mixed uniformly in step (1) for 2 hours and let it stand for 4 hours, dry it in a blast drying oven at 110°C for 6 hours, roast it in a muffle furnace at 550°C for 6 hours, and then pulverize it to obtain a powder Hydrogen peroxide catalytically activates the catalyst. The catalyst active component and the weight percentage of the carrier are respectively: 5.0% of tricobalt tetroxide and 95.0% of titanium dioxide.

[0034] The process was evaluated using simulated flue gas conditions, with 20% hydrogen peroxide solution as the ...

Embodiment 3

[0036]Adopt the device identical with embodiment 1 structure, described hydrogen peroxide catalytic activation catalyst, its preparation process comprises the following steps:

[0037] (1) Weigh 730g of nickel nitrate hexahydrate, dissolve it in 4350mL of deionized water, and configure it into a solution; add the configured solution to 4500g of nano-anatase TiO 2 carrier, and mixed and stirred in a mixer;

[0038] (2) The carboxymethyl cellulose of the pseudo-boehmite of 150g, the glass fiber of 50g, the carboxymethyl cellulose of 67g is added in the mixture that obtains in step (1) and mixes and stirs, obtains catalyst paste;

[0039] (3) Place the catalyst paste mixed uniformly in step (2) on a stainless steel mesh plate, roll coating, crimping, shearing, drying in a blast drying oven at 110°C for 8h, and roasting in a muffle furnace at 550°C After 8 hours, the flat-plate hydrogen peroxide catalytic activation catalyst can be obtained. The weight percentages of the catalys...

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PUM

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Abstract

The invention relates to the fields of industrial catalysis and environmental management, and particularly relates to a nitrogen oxide removal process based on hydrogen peroxide catalytic oxidation. A hydrogen peroxide solution is directly sprayed into a flue after passing through an atomizer; after the hydrogen peroxide solution is mixed with flue gas, a mixture enters a catalyst layer; the mixture is activated under the contact action of a catalyst; NO in the flue gas is oxidized into high valence lyotropic nitrogen oxides such as NO2, N2O4, N2O5 and the like; absorption processing is carried out by using alkali slurry to remove the nitrogen oxides in the flue gas. The process is simple, easy to operate, compact in device structure, good in economy and flexible to regulate, has various mode configurations, and can implement efficient denitration. Meanwhile, the catalyst used in the technical process uses nano titanium dioxide as a carrier and uses one or more of ceric oxide, cobaltosic oxide, nickel oxide, chromium sesquioxide and manganese dioxide as active ingredients; the catalyst is low in price and simple in preparation process.

Description

technical field [0001] The invention relates to the field of industrial catalysis and environmental treatment, in particular to a process for removing nitrogen oxides based on catalytic oxidation of hydrogen peroxide. Background technique [0002] The main source of flue gas pollutants is the combustion of fuels, including coal, coke, heavy oil, diesel, coal gas, natural gas, etc. Harmful substances such as nitrogen oxides (NOx) produced along with fuel combustion will cause harm to human health and the surrounding environment. According to the "2015 China Environmental Status Bulletin" issued by the Ministry of Environmental Protection, my country's total nitrogen oxide emissions in 2015 were 18.518 million tons, of which industrial nitrogen oxide emissions are still the main source. Since 2011, policy documents related to environmental protection have become more and more strict, and strict regulations have been imposed on the reduction of total NOx emissions in various i...

Claims

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Application Information

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IPC IPC(8): B01D53/75B01D53/78B01D53/86B01J23/889B01D53/56
CPCB01D53/75B01D53/56B01D53/78B01D53/8628B01J23/002B01J23/8892B01J2523/00B01J2523/3712B01J2523/845B01J2523/847B01J2523/72B01J2523/67B01J2523/47
Inventor 陆强王琦仇志超傅玉唐诗洁董长青杨勇平
Owner NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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