CN202410503U - High-pressure water mist selective non-catalytic reduction denitration device - Google Patents

High-pressure water mist selective non-catalytic reduction denitration device Download PDF

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Publication number
CN202410503U
CN202410503U CN 201220015683 CN201220015683U CN202410503U CN 202410503 U CN202410503 U CN 202410503U CN 201220015683 CN201220015683 CN 201220015683 CN 201220015683 U CN201220015683 U CN 201220015683U CN 202410503 U CN202410503 U CN 202410503U
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CN
China
Prior art keywords
catalytic reduction
water mist
burdening
pressure pump
storage tank
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
CN 201220015683
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Chinese (zh)
Inventor
许智远
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Henan Hailite Environmental Protection Technology Co., Ltd.
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Henan Hailite Electromechanical Manufacturing Co Ltd
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Priority to CN 201220015683 priority Critical patent/CN202410503U/en
Application granted granted Critical
Publication of CN202410503U publication Critical patent/CN202410503U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to a high-pressure water mist selective non-catalytic reduction denitration device, which can be used for effectively solving the problems of large denitration investment, high cost and low efficiency. According to a technical scheme for solving the problems, the high-pressure water mist selective non-catalytic reduction denitration device comprises a high-pressure pump unit, an ejector and a storage tank, wherein a urea cabin is connected with a burdening pool through a metering cabin; the burdening pool is connected with the inlet of a urea solution storage tank through a burdening conveying pump; the outlet of the storage tank is connected with the high-pressure pump unit through a mixer; the high-pressure pump unit is connected with a multi-layer ejector in a hearth; and tap water pipes are connected to the burdening pool, the storage tank and the mixer. The high-pressure water mist selective non-catalytic reduction denitration device has the advantages of high denitration efficiency, simple device, large treatment air volume, low cost, cleanliness, avoidance of secondary pollution, convenience for running and maintaining, safe and stable equipment performance and long service life.

Description

Heavy pressure fine spray SNCR denitration treating apparatus
Technical field
The utility model relates to gas processing device, particularly a kind of heavy pressure fine spray SNCR denitration treating apparatus.
Background technology
Along with rapid development of national economy, China has become production of energy and consumption big country.Consequent NOx discharge capacity also increases year by year, ranks first in the world at present, and in order to reduce the discharging of NOx, various countries have successively carried out big quantity research to coal-fired unit NOx control technology.Common gas denitrifying technology has SCR method, SNCR method, electron beam irradiation method etc., wherein SCR method and SNCR method comparative maturity.The wet flue gas denitration technology has desulfurization and denitrification integral technology, ozone oxidation absorption process and C1O2 oxidation absorption process etc.But use these traditional methods to handle that investment is big, operating cost is high, efficient is low.Provide a kind of denitrification apparatus simply efficient, with low cost, the technology cleaning imperative.
Summary of the invention
To above-mentioned situation, for overcoming existing technological deficiency, the purpose of the utility model just provides a kind of heavy pressure fine spray SNCR denitrification apparatus, can effectively solve big, high, the inefficient problem of cost of denitration investment of handling.
The technical scheme of the utility model is; Comprise high-pressure pump group, injector and holding vessel; The urea feed bin links to each other with dosing chamber through measuring chute, and dosing chamber links to each other with the import of urea liquid holding vessel through the batching delivery pump, and the holding vessel outlet is connected with the high-pressure pump group through blender; The high-pressure pump group is connected with the interior multilayer spray device of burner hearth, is connected to running water pipe on dosing chamber, holding vessel and the blender.
The utility model denitration efficiency is high, device is simple, handle large-minded, with low cost, clean cleaning does not exist secondary pollution, operation maintenance conveniently, equipment performance safety and stability, long service life.
Description of drawings
Accompanying drawing is the structural representation of the utility model.
The specific embodiment
Elaborate below in conjunction with the specific embodiment of accompanying drawing to the utility model.
By shown in Figure 1; The utility model comprises high-pressure pump group, injector and holding vessel; Urea feed bin 1 links to each other with dosing chamber 3 through measuring chute 2, and dosing chamber 3 links to each other with 5 imports of urea liquid holding vessel through batching delivery pump 4, and holding vessel 5 outlets are connected with high-pressure pump group 7 through blender 6; High-pressure pump group 7 is connected with the interior multilayer spray device 8 of burner hearth, is connected to running water pipe 9 on dosing chamber 3, holding vessel 5 and the blender 6.
Described injector 8 is to be made up of 10-16 the nozzle of installing on a plurality of heavy pressure fine spray shower nozzles and each heavy pressure fine spray shower nozzle, and shower nozzle is spherical or many prismatics, the bore of each nozzle≤100 μ m (the mist particle diameter 10-100 μ m of general ejection).
Multilayer spray device 8 is distributed with a plurality of high pressure fine mist combination type spray heads (not indicating among the figure) in the boiler thorax; 1 outlet of urea feed bin is connected with dosing chamber 3 through measuring chute 2; Running water gets into dosing chamber 3 through running water pipe 9; With urea dilution is 50% solution, and dosing chamber 3 is communicated with urea liquid holding vessel 5 through batching delivery pump 4, and running water is through running water pipe 9 entering holding vessels 5 further dilute urine cellulose solutions to 10%; Urea liquid storage tank 5 is communicated with high-pressure pump group 7 through blender 6; The urea absorption liquid is communicated with multilayer spray device 8 in the burner hearth through high-pressure pump group 7, because of running water links to each other with blender 6 through running water pipe 9, replenishes required water in the technical process according to the practical operation situation timely and appropriate discovery.
The working condition of the utility model is that SCNR is combined denitration with heavy pressure fine spray.The absorption liquid that contains urea is sent in the injector by the high-pressure pump group, forms the heavy pressure fine spray ejection through shower nozzle, fully contacts, reacts with NOx, after purified gas reaches the discharge standard of regulation, discharges burner hearth.Because adopt urea as absorption liquid, temperature is controlled at 900 ℃ ~ 1150 ℃ in the burner hearth.
The NOx pollutant can be efficiently removed in efficiently denitration of the utility model, and denitration efficiency reaches as high as more than 90%, and denitration effect substantially exceeds the existing pollutant emission standard of country.Thorough reducing NOx harmful substance, and can reach perfect denitration effect, gas after treatment can reach innoxious discharging fully, never produces secondary pollution, plays the effect of high-effective disinfecting sterilization simultaneously.
The utility model investment is low, handles large-mindedly, and clean-up effect is stablized the denitration efficiency height; There is not secondary pollution, equipment performance safety and stability, long service life; Improve the surrounding area air quality, help the beautifying city appearance of the city, improve health level; The protection people's health is the innovation on the denitrification apparatus.

Claims (4)

1. heavy pressure fine spray SNCR denitration treating apparatus; Comprise high-pressure pump group, injector and holding vessel; It is characterized in that; Urea feed bin (1) links to each other with dosing chamber (3) through measuring chute (2), and dosing chamber (3) links to each other with urea liquid holding vessel (5) import through batching delivery pump (4), and holding vessel (5) outlet is connected with high-pressure pump group (7) through blender (6); High-pressure pump group (7) is connected with the interior multilayer spray device (8) of burner hearth, is connected to running water pipe (9) on dosing chamber (3), holding vessel (5) and the blender (6).
2. heavy pressure fine spray SNCR denitration treating apparatus according to claim 1 is characterized in that, described injector (8) is to be made up of 10-16 the nozzle of installing on a plurality of heavy pressure fine spray shower nozzles and each heavy pressure fine spray shower nozzle.
3. heavy pressure fine spray SNCR denitration treating apparatus according to claim 2 is characterized in that, described shower nozzle is spherical or many prismatics.
4. heavy pressure fine spray SNCR denitration treating apparatus according to claim 2 is characterized in that, the bore of described each nozzle≤100 μ m.
CN 201220015683 2012-01-14 2012-01-14 High-pressure water mist selective non-catalytic reduction denitration device Expired - Lifetime CN202410503U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220015683 CN202410503U (en) 2012-01-14 2012-01-14 High-pressure water mist selective non-catalytic reduction denitration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220015683 CN202410503U (en) 2012-01-14 2012-01-14 High-pressure water mist selective non-catalytic reduction denitration device

Publications (1)

Publication Number Publication Date
CN202410503U true CN202410503U (en) 2012-09-05

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CN 201220015683 Expired - Lifetime CN202410503U (en) 2012-01-14 2012-01-14 High-pressure water mist selective non-catalytic reduction denitration device

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104437025A (en) * 2014-11-21 2015-03-25 江苏紫光吉地达环境科技有限公司 Novel device for selective non-catalytic reduction denitration
CN107261802A (en) * 2017-08-11 2017-10-20 河南海力特机电制造有限公司 Heavy pressure fine spray SNCR denitration system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104437025A (en) * 2014-11-21 2015-03-25 江苏紫光吉地达环境科技有限公司 Novel device for selective non-catalytic reduction denitration
CN107261802A (en) * 2017-08-11 2017-10-20 河南海力特机电制造有限公司 Heavy pressure fine spray SNCR denitration system

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20190319

Address after: No. 22 Ruida Road, Zhengzhou High-tech Industrial Development Zone, Henan Province

Patentee after: Henan Hailite Environmental Protection Technology Co., Ltd.

Address before: 450001, No. 22, Ruida Road, hi tech Zone, Henan, Zhengzhou

Patentee before: Hailite Electromechanical Mfg. Co., Ltd., He'nan Prov.

TR01 Transfer of patent right
CX01 Expiry of patent term

Granted publication date: 20120905

CX01 Expiry of patent term