A mixed reaction device for scr denitrification of industrial flue gas

A technology for industrial flue gas and reaction devices, applied in mixers, shaking/oscillating/vibrating mixers, gas treatment, etc., can solve problems such as incomplete denitrification, inability to obtain interstitial mixing contact, and short contact time

Active Publication Date: 2022-01-28
湛江开发区隆源矿业有限公司
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  • Claims
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AI Technical Summary

Problems solved by technology

[0005] The purpose of the present invention is to provide a kind of industrial flue gas SCR denitrification mixing reaction device, to solve the above-mentioned background technology. Detachment after contact reaction, unable to obtain interstitial mixed contact, resulting in short contact time, insufficient reaction time, and incomplete denitrification

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  • A mixed reaction device for scr denitrification of industrial flue gas
  • A mixed reaction device for scr denitrification of industrial flue gas
  • A mixed reaction device for scr denitrification of industrial flue gas

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Embodiment Construction

[0029] Next, the technical solutions in the embodiments of the present invention will be described in connection with the drawings of the embodiments of the present invention, and it is understood that the described embodiments are merely the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, those of ordinary skill in the art without making all of the other embodiments given herein without creative efforts fall within the scope of the present invention.

[0030] See Figure 1-9 The present invention provides a technical solution: an industrial flue gas denitration SCR mixing reaction apparatus, comprising a denitrification tank 1, denitrification tank inner bottom wall 1 is fixedly connected with a cylindrical reactor shell 2, the bottom end of the cylindrical housing 2 through the reaction denitration 1 and which extend to the pool, the bottom ends of the cylindrical reactor shell 2 are respectively communicated wi...

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Abstract

The invention discloses an industrial flue gas SCR denitrification mixed reaction device in the technical field of industrial flue gas SCR denitrification, comprising a denitrification tank, the bottom of the inner wall of the denitrification tank is fixedly connected with a cylindrical reaction shell, and the bottom of the cylindrical reaction shell is end of the denitrification tank and extends to the bottom, the two ends of the bottom of the cylindrical reaction shell are respectively connected with a one-way ventilation valve and a one-way liquid injection valve, the bottom of the cylindrical reaction shell is fixedly installed with a motor, the The output end of the motor is fixedly connected with a stirring shaft, the top of the stirring shaft penetrates the cylindrical reaction shell and extends to its interior, and a connecting frame is slidably connected on the surface along the extending direction of the axis, and a stirring shaft is fixedly connected on the surface of the connecting frame. leaf; the whole denitrification mixing device of the present invention can carry out intermittent stay and mixing of the flue gas, so that the flue gas can be fully mixed with the denitrification liquid, and it passes through three different denitrification spaces, forming a three-layer denitrification, which is beneficial to the flue gas The denitrification is more thorough.

Description

Technical field [0001] The present invention relates to the field of industrial flue gas SCR denitration technology, in particular a industrial flue gas SCR denitration mixing reaction device. Background technique [0002] In the prior art, the invention of the invention, the invention, and the present invention, which is 201810603947.x, discloses a kiln SCR denitration process including the following steps: extraction kiln The extremely cold section high temperature flue gas is led to the kiln head; the high-temperature flue gas is introduced to the kiln head, and the high temperature flue gas in the kiln is mixed with the flue gas in the kiln head, and the flue gas temperature in the kiln rises to 350 ° C; High temperature flue gas after heating, the SCR denitration device is introduced; the SCR denitration device passes into the high-temperature flue gas, and the ammonia water is introduced into the SCR denitration apparatus, so that the ammonia water is reacted with the high ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/78B01D53/54B01F31/40
CPCB01D53/78B01D53/54B01D2258/0283B01F31/443B01F31/449
Inventor 范朝伟赵瑞壮王春刚郜国平陈晓强杜栏停
Owner 湛江开发区隆源矿业有限公司
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