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High-efficiency denitration system

A high-efficiency, denitrification technology, applied in the field of high-efficiency denitrification systems, can solve the problems of unfavorable energy conservation and environmental protection, increased energy consumption and investment of flue gas heating devices and flue gas coolers, etc.

Inactive Publication Date: 2021-06-08
湖州加怡新市热电有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] Regarding the related technologies mentioned above, the inventor believes that there are the following defects: the flue gas heating device and the flue gas cooler will increase additional energy consumption and investment, which is not conducive to energy conservation and environmental protection

Method used

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Embodiment Construction

[0036] The following is attached Figure 1-5 The application is described in further detail.

[0037] The embodiment of the present application discloses a high-efficiency denitrification system. refer to figure 1 , figure 2 , the high-efficiency denitrification system includes an air preheater 1 and an SCR reactor 3, wherein the air preheater 1 includes a shell 14 and a plurality of air pipes 16 placed in the shell 14, and the shell 14 is divided by a partition 15 There are three high-temperature zones 11, medium-temperature zone 12 and low-temperature zone 13 arranged in sequence. The flue gas is distributed in each temperature zone, and the air duct 16 is filled with cold air to cool down the flue gas in each temperature zone.

[0038] like figure 1 As shown, the entrance of the high temperature zone 11 is connected with a flue gas input channel 51, the high temperature zone 11 communicates with the medium temperature zone 12 through the through hole 17, and the outlet...

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Abstract

The invention relates to a high-efficiency denitration system, and the system comprises an air preheater, an SCR reactor, a flue gas conveying channel used for being connected between the air preheater and the SCR reactor and a flue gas output channel connected to the outlet end of the SCR reactor; a dust remover is arranged on the flue gas conveying channel, and a high-temperature area, a medium-temperature area and a low-temperature area are sequentially arranged in the air preheater; an inlet of the high-temperature area is connected with a flue gas input channel, the high-temperature area is communicated with the medium-temperature area through a through hole, one end of the flue gas conveying channel is communicated with an outlet of the medium-temperature area, and a temperature adjusting device used for adjusting the temperature of flue gas in the flue gas conveying channel is arranged in the middle section of the flue gas conveying channel; one end of the smoke output channel is connected with an inlet of the low-temperature area, and an outlet of the low-temperature area is connected with a smoke exhaust channel. The system has the effects of energy conservation and environmental protection.

Description

technical field [0001] This application relates to the field of flue gas denitrification technology, in particular to a high-efficiency denitrification system. Background technique [0002] China is rich in coal resources, and most of them are used by direct combustion methods, such as thermal power generation. In the combustion of coal, a large amount of nitrogen oxides NOx will be produced. If this gas is directly discharged into the atmosphere, it will produce highly corrosive acid rain. nitrogen) treatment. [0003] Among the existing denitrification methods, there are selective catalytic reduction (SCR) and selective non-catalytic reduction (SNCR). A selective reduction reaction is produced, and finally non-polluting nitrogen and water vapor are produced. The difference between the two methods is that SNCR is generally carried out in a boiler with a higher temperature (800-1200°C) because it does not have the help of a catalyst; while SCR uses a catalyst in the flue,...

Claims

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Application Information

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IPC IPC(8): B01D53/90B01D53/56F23J15/06F23J15/02
CPCB01D53/8631B01D53/90B01D2251/2062B01D2258/0283F23J15/022F23J15/06
Inventor 姚云松杨锦明陈辉
Owner 湖州加怡新市热电有限公司