CN202460442U - Acid mist absorption processing device of high-pressure water mist - Google Patents

Acid mist absorption processing device of high-pressure water mist Download PDF

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Publication number
CN202460442U
CN202460442U CN2011205383257U CN201120538325U CN202460442U CN 202460442 U CN202460442 U CN 202460442U CN 2011205383257 U CN2011205383257 U CN 2011205383257U CN 201120538325 U CN201120538325 U CN 201120538325U CN 202460442 U CN202460442 U CN 202460442U
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CN
China
Prior art keywords
pressure fine
regeneration cycle
pressure water
absorption
mist
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Expired - Lifetime
Application number
CN2011205383257U
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Chinese (zh)
Inventor
许智远
许洪远
任志全
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Henan Hailite Environmental Protection Technology Co., Ltd.
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Henan Hailite Electromechanical Manufacturing Co Ltd
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Priority to CN2011205383257U priority Critical patent/CN202460442U/en
Application granted granted Critical
Publication of CN202460442U publication Critical patent/CN202460442U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to an acid mist absorption processing device of high-pressure water mist, effectively solving the problems that the acid mist investment is large, the cost is high and a secondary pollution is easy to generate. The solving technical scheme is as follows: the device comprises a high-pressure water mist pump unit, an absorbing tower and a regeneration cycle pool, wherein multiple high-pressure water mist combination shower nozzles are distributed in the absorbing tower in a multi-layer form; the air inlet of the absorbing tower is connected with a collection cover through a draught fan, and the exhaust port of the absorbing tower is communicated with a chimney through a demister; the discharge opening of the absorbing tower is communicated with the regeneration cycle pool, and the regeneration cycle pool is communicated with the inlet of the high-pressure water mist pump unit through a high-pressure rubber tube; and the outlet of the high-pressure water mist pump unit is communicated with the high-pressure water mist combination shower nozzles in the absorbing tower, and the regeneration cycle pool is respectively connected with a soda solution storage bin and an absorption solution storage bin. Compared with the traditional processing method, the processing device provided by the utility model has the advantages of high acid mist removal efficiency, simple device, cheap cost, clean technology, is convenient for operation and maintenance, does not generate no secondary pollution and the like.

Description

Heavy pressure fine spray acid mist absorption treating device
Technical field
The utility model relates to gas processing device, particularly a kind of heavy pressure fine spray acid mist absorption treating device.
Background technology
Becoming increasingly abundant and industrial expansion of Along with people's material life; Rubbish that productive life produced and waste water and gas severe contamination people's living environment; The processing of the acid mist gas that produces in sour process in industries such as chemical industry, electronics, metallurgy, plating, weaving (chemical fibre), machine-building; More become the problem that we must face and solve, domestic common processing acid mist has liquid absorption method, solid absorption method, filtration method, static demist method, mechanical type demist method etc. at present.But, use traditional method to handle that investment is big, operating cost is high, be prone to produce secondary pollution for the volatile organic waste gas and the acid mist of big flow, low concentration.The problem that so, how to provide the acid mist treating apparatus of a kind of simply efficient, with low cost, technology cleaning, non-secondary pollution to become in the industry to be concerned about.
Summary of the invention
To above-mentioned situation, for overcoming the defective of prior art, the purpose of the utility model just provides a kind of heavy pressure fine spray acid mist absorption treating device, can effectively solve to handle that the acid mist investment is big, cost is high, be prone to produce secondary pollution problem.
The technical scheme that the utility model solves is; Comprise heavy pressure fine spray pump group, absorption tower and regeneration cycle pond; Multilayer is distributed with a plurality of high pressure fine mist combination type spray heads in the absorption tower, and the absorption tower air inlet links to each other with collecting hood through air-introduced machine, and the absorption tower exhaust outlet is communicated with chimney through demister; The absorption tower discharge outlet is communicated with the regeneration cycle pond; The regeneration cycle pond is connected with the import of heavy pressure fine spray pump group through high-pressure rubber pipe, and heavy pressure fine spray pump group outlet is connected with high pressure fine mist combination type spray head in the absorption tower through high-pressure rubber pipe, and the regeneration cycle pond links to each other with the absorption liquid storage warehouse with alkali storage compartment respectively.
The utility model is compared with traditional processing method, and it has, advantages such as device simple, with low cost, technology cleaning, operation maintenance convenience, non-secondary pollution high except that acid mist efficient.
Description of drawings
Fig. 1 is the structure frame figure of the utility model.
The specific embodiment
Elaborate below in conjunction with the specific embodiment of accompanying drawing to the utility model.
Provide by accompanying drawing; The utility model comprises heavy pressure fine spray pump group, absorption tower and regeneration cycle pond; Multilayer is distributed with a plurality of high pressure fine mist combination type spray heads (not indicating among the figure) in the absorption tower 1, and the absorption tower air inlet is connected with collecting hood 5 through air-introduced machine 4, and the absorption tower exhaust outlet is communicated with chimney 7 through demister 6; The absorption tower discharge outlet is communicated with regeneration cycle pond 3; Regeneration cycle pond 3 is connected with 2 imports of heavy pressure fine spray pump group through high-pressure rubber pipe, and heavy pressure fine spray pump group 2 outlet is connected with high pressure fine mist combination type spray head in the absorption tower 1 through high-pressure rubber pipe, and the regeneration cycle pond links to each other with absorption liquid storage warehouse 8 with alkali storage compartment 9 respectively.
Described regeneration cycle pond 3 partly is made up of regeneration, circulation, Guan Chisan successively, and wherein regenerating section links to each other with absorption liquid storage warehouse 8 with heavy pressure fine spray pump group 2, and cyclic part links to each other with absorption tower 1, and pipe pond part links to each other with alkali storage compartment 9; Regeneration, circulation, Guan Chi are identical, and pipe pond part is to add alkali lye to regulate the Ph value; Regenerated reactor partly is the material that the alkali of consumption generated during acid mist absorbed and newly adds raw material reaction, from newly-generated alkali; Circulatory pool partly is exactly regularly to salvage sediment, and the solution that contains the material that alkali that acid mist consumes in absorbing generates of clarification is transported in the regenerated reactor.
10-16 nozzle is installed on the described high pressure fine mist combination type spray head, and sprayer body is spherical or many prismatics.
The working condition of the utility model is that acid mist is collected by collecting hood after deacidify in the air-introduced machine entering absorption tower.The absorption liquid that contains plumper is sent into high pressure fine mist combination type spray head by heavy pressure fine spray pump group and is formed the heavy pressure fine spray ejection; Fully contact, react with acid mist; After purified gas reaches the discharge standard of regulation, remove supersaturation moisture content wherein, discharge through chimney through demister.To different types of acid mist, can select the plumper of variety classes and variable concentrations for use.Waste water recycles after dosing is handled in circulatory pool, and sediment regularly drags for clearly, transports outward.
The utility model can efficiently remove acid mist; Can efficiently remove major pollutants such as volatile organic matter (VOC), inorganic matter, hydrogen sulfide, ammonia, sulfuric acid mist class; And various stinks; The depickling mist is most effective to be reached more than 99%, and the depickling fog effect substantially exceeds the existing pollutant emission standard of country.Can thoroughly decompose poisonous and harmful substance in the acid mist, and can reach perfect deacidification effect, the acid mist after decomposing 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 stable, removes acid mist efficient height; There is not secondary pollution, equipment performance safety and stability, long service life; Can eliminate acid mist fully, 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 acid mist treating apparatus.

Claims (3)

1. heavy pressure fine spray acid mist absorption treating device; Comprise heavy pressure fine spray pump group, absorption tower and regeneration cycle pond; It is characterized in that; The interior multilayer in absorption tower (1) is distributed with a plurality of high pressure fine mist combination type spray heads, and the absorption tower air inlet is connected with collecting hood (5) through air-introduced machine (4), and the absorption tower exhaust outlet is communicated with chimney (7) through demister (6); The absorption tower discharge outlet is communicated with regeneration cycle pond (3); Regeneration cycle pond (3) is connected with heavy pressure fine spray pump group (2) import through high-pressure rubber pipe, and heavy pressure fine spray pump group (2) outlet is connected with high pressure fine mist combination type spray head in absorption tower (1) through high-pressure rubber pipe, and the regeneration cycle pond links to each other with absorption liquid storage warehouse (8) with alkali storage compartment (9) respectively.
2. heavy pressure fine spray acid mist absorption treating device according to claim 1; It is characterized in that; Described regeneration cycle pond (3) partly is made up of regeneration, circulation, Guan Chisan successively; Wherein regenerating section links to each other with absorption liquid storage warehouse (8) with heavy pressure fine spray pump group (2), and cyclic part links to each other with absorption tower (1), and pipe pond part links to each other with alkali storage compartment (9).
3. heavy pressure fine spray acid mist absorption treating device according to claim 1 is characterized in that, 10-16 nozzle is installed on the described high pressure fine mist combination type spray head, and sprayer body is spherical or many prismatics.
CN2011205383257U 2011-12-21 2011-12-21 Acid mist absorption processing device of high-pressure water mist Expired - Lifetime CN202460442U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011205383257U CN202460442U (en) 2011-12-21 2011-12-21 Acid mist absorption processing device of high-pressure water mist

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011205383257U CN202460442U (en) 2011-12-21 2011-12-21 Acid mist absorption processing device of high-pressure water mist

Publications (1)

Publication Number Publication Date
CN202460442U true CN202460442U (en) 2012-10-03

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Family Applications (1)

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CN2011205383257U Expired - Lifetime CN202460442U (en) 2011-12-21 2011-12-21 Acid mist absorption processing device of high-pressure water mist

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CN (1) CN202460442U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102886197A (en) * 2012-10-22 2013-01-23 巨石集团有限公司 Treatment method for fluorine-containing waste gas
CN104356061A (en) * 2014-10-23 2015-02-18 河南省科学院高新技术研究中心 Efficient absorption method for 2-cyanopyridine
CN104492214A (en) * 2014-12-17 2015-04-08 中国兵器科学研究院宁波分院 Device and method for removing acid mist
CN105413410A (en) * 2015-12-31 2016-03-23 天津君议台科技发展有限公司 Device for recycling and purifying acid mist of pickling line
CN105536442A (en) * 2015-12-31 2016-05-04 天津君议台科技发展有限公司 Acid regeneration acid mist recycling and purifying device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102886197A (en) * 2012-10-22 2013-01-23 巨石集团有限公司 Treatment method for fluorine-containing waste gas
CN104356061A (en) * 2014-10-23 2015-02-18 河南省科学院高新技术研究中心 Efficient absorption method for 2-cyanopyridine
CN104492214A (en) * 2014-12-17 2015-04-08 中国兵器科学研究院宁波分院 Device and method for removing acid mist
CN105413410A (en) * 2015-12-31 2016-03-23 天津君议台科技发展有限公司 Device for recycling and purifying acid mist of pickling line
CN105536442A (en) * 2015-12-31 2016-05-04 天津君议台科技发展有限公司 Acid regeneration acid mist recycling and purifying device

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Legal Events

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

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20121003