CN202376901U - High Pressure water mist stench gas processing equipment - Google Patents

High Pressure water mist stench gas processing equipment Download PDF

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Publication number
CN202376901U
CN202376901U CN 201120538338 CN201120538338U CN202376901U CN 202376901 U CN202376901 U CN 202376901U CN 201120538338 CN201120538338 CN 201120538338 CN 201120538338 U CN201120538338 U CN 201120538338U CN 202376901 U CN202376901 U CN 202376901U
Authority
CN
China
Prior art keywords
absorption tower
high pressure
pressure fine
heavy pressure
fine spray
Prior art date
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 201120538338
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Chinese (zh)
Inventor
许智远
莫许钚
靳玉甫
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.
Original Assignee
Henan Hailite Electromechanical Manufacturing Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Henan Hailite Electromechanical Manufacturing Co Ltd filed Critical Henan Hailite Electromechanical Manufacturing Co Ltd
Priority to CN 201120538338 priority Critical patent/CN202376901U/en
Application granted granted Critical
Publication of CN202376901U publication Critical patent/CN202376901U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to high pressure water mist stench gas processing equipment which can effectively solve the problem that the stench gas has large investment and high cost, and is easy to generate secondary pollution. The technical scheme of the utility model is that the high pressure water mist stench gas processing equipment comprises a high pressure water mist pump group, an absorption tower and a circulating pool, wherein multiple layers of high pressure water mist combination shower nozzles are distributed in the absorption tower; the air inlet of the absorption tower is communicated with a collecting cover through a fan, and an exhaust port of the absorption tower is communicated with a chimney through a demister; a dewatering port of the absorption tower is communicated with the circulating pool, and the circulating pool is communicated with the inlet of the high pressure water mist pump group through high pressure glue pipes; and the outlet of the high pressure water mist pump group is communicated with the high pressure water mist combination shower nozzles in the absorption tower through the high pressure glue pipes, and the circulating pool is respectively connected with an absorption liquid storing bin, an alkali liquor storing bin and an oxidizer storing bin. Compared with the traditional processing method, the high pressure water mist stench gas processing equipment provided by the utility model has the advantages of high deodorization efficiency, simple device, low cost, clean technology, and convenience in operating maintenance, and has no secondary pollution and the like.

Description

Heavy pressure fine spray is handled foul gas equipment
Technical field
The utility model relates to gas processing device, and particularly a kind of heavy pressure fine spray is handled foul gas equipment.
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 foul gas that produces in occasions such as industrial and agricultural production, municipal wastewater, Treatment of Sludge and garbage transfer stations; More become the problem that we must face and solve, domestic common processing foul gas has firing method, oxidizing process, absorption method, bioanalysis 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 foul gas of big flow, low concentration.The problem that so, how to provide the foul gas 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 and handles foul gas equipment, can effectively solve to handle that the foul gas 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 circulatory pool; 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 is connected 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 circulatory pool; Circulatory pool 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 circulatory pool links to each other with absorption liquid storage warehouse, alkali storage compartment and oxidant storage warehouse respectively.
The utility model is compared with traditional processing method, and it has advantages such as deodorization efficiency height, simple, with low cost, the technological cleaning of device, operation maintenance convenience, non-secondary pollution.
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 circulatory pool; Multilayer is distributed with a plurality of high pressure fine mist combination type spray heads 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 circulatory pool 3; Circulatory pool 3 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 1 through high-pressure rubber pipe, and circulatory pool links to each other with absorption liquid storage warehouse 8, alkali storage compartment 9 and oxidant (clorox) storage warehouse 10 respectively.
Described heavy pressure fine spray pump group comprises the first heavy pressure fine spray pump 2a and the second heavy pressure fine spray pump 2b at least.
Described absorption tower 1 has two (providing two among the figure) at least, and each absorption tower discharge outlet all is communicated with circulatory pool, and the high pressure fine mist combination type spray head in each absorption tower is communicated with circulatory pool through the heavy pressure fine spray pump.
Described circulatory pool is to be made up of left side clear water reserviors, grey pond, right side clear water reserviors three parts successively; Wherein clear water reserviors part in left side links to each other with the absorption liquid storage warehouse 8 and the first heavy pressure fine spray pump 2a; Ash pond part links to each other with alkali storage compartment 9, and clear water reserviors part in right side links to each other with the oxidant storage warehouse 10 and the second heavy pressure fine spray pump 2b.The left side clear water reserviors add sulfuric acid, as first order absorption liquid; The ash pond adds alkali lye, with the reactant salt that the first order generates, and deduction Ph value, deposition; The right side clear water reserviors, the clear water reserviors through clear solutions inflow right side in grey pond add oxidant (clorox), as second level absorption liquid.
The working condition of the utility model is that foul gas is collected after air-introduced machine gets in the absorption tower by collecting hood and carried out deodorizing.The absorption liquid that contains deodorant 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 foul gas; After purified gas reaches the discharge standard of regulation, remove supersaturation moisture content wherein, discharge through chimney through demister.To different types of foul gas, can select the deodorant 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 stench; Can efficiently remove major pollutants such as volatile organic matter (VOC), inorganic matter, hydrogen sulfide, ammonia, thio-alcohol; And various foul smells; Deodorization efficiency reaches as high as more than 99%, and deodorising effect substantially exceeds the existing odorant pollutant discharge standard (GB 14554-93) of country.Can thoroughly decompose poisonous and harmful substance in the foul gas, and can reach perfect deodorizing effect, the foul gas 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, the deodorization efficiency height; There is not secondary pollution, equipment performance safety and stability, long service life; Can eliminate foul gas 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 foul gas treating apparatus.

Claims (4)

1. a heavy pressure fine spray is handled foul gas equipment; Comprise heavy pressure fine spray pump group, absorption tower and circulatory pool; 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 circulatory pool (3); Circulatory pool (3) 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 absorption tower (1) through high-pressure rubber pipe, and circulatory pool links to each other with absorption liquid storage warehouse (8), alkali storage compartment (9) and oxidant storage warehouse (10) respectively.
2. heavy pressure fine spray according to claim 1 is handled foul gas equipment, it is characterized in that described heavy pressure fine spray pump group comprises the first heavy pressure fine spray pump (2a) and the second heavy pressure fine spray pump (2b) at least.
3. heavy pressure fine spray according to claim 1 is handled foul gas equipment; It is characterized in that; Described absorption tower (1) has two at least, and each absorption tower discharge outlet all is communicated with circulatory pool, and the high pressure fine mist combination type spray head in each absorption tower is communicated with circulatory pool through the heavy pressure fine spray pump.
4. heavy pressure fine spray according to claim 1 is handled foul gas equipment; It is characterized in that; Described circulatory pool (3) is to be made up of left side clear water reserviors, grey pond, right side clear water reserviors three parts successively; Wherein clear water reserviors part in left side links to each other with the absorption liquid storage warehouse (8) and the first heavy pressure fine spray pump (2a), and grey pond part links to each other with alkali storage compartment (9), and clear water reserviors part in right side links to each other with the oxidant storage warehouse (10) and the second heavy pressure fine spray pump (2b).
CN 201120538338 2011-12-21 2011-12-21 High Pressure water mist stench gas processing equipment Expired - Lifetime CN202376901U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201120538338 CN202376901U (en) 2011-12-21 2011-12-21 High Pressure water mist stench gas processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201120538338 CN202376901U (en) 2011-12-21 2011-12-21 High Pressure water mist stench gas processing equipment

Publications (1)

Publication Number Publication Date
CN202376901U true CN202376901U (en) 2012-08-15

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ID=46625423

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201120538338 Expired - Lifetime CN202376901U (en) 2011-12-21 2011-12-21 High Pressure water mist stench gas processing equipment

Country Status (1)

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CN (1) CN202376901U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106334432A (en) * 2015-07-14 2017-01-18 上海三卿环保科技有限公司 Device and method for activation of oxidizing agent through desulphurization denitration circulation solution

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106334432A (en) * 2015-07-14 2017-01-18 上海三卿环保科技有限公司 Device and method for activation of oxidizing agent through desulphurization denitration circulation solution

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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

Effective date of registration: 20190326

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: 20120815

CX01 Expiry of patent term