CN103223279A - Aeration-type air purifying device - Google Patents

Aeration-type air purifying device Download PDF

Info

Publication number
CN103223279A
CN103223279A CN2013101519783A CN201310151978A CN103223279A CN 103223279 A CN103223279 A CN 103223279A CN 2013101519783 A CN2013101519783 A CN 2013101519783A CN 201310151978 A CN201310151978 A CN 201310151978A CN 103223279 A CN103223279 A CN 103223279A
Authority
CN
China
Prior art keywords
aeration
absorption
flow container
gas
absorption liquid
Prior art date
Application number
CN2013101519783A
Other languages
Chinese (zh)
Inventor
罗军杰
刘杰
Original Assignee
秦皇岛同力达环保能源工程有限公司
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 秦皇岛同力达环保能源工程有限公司 filed Critical 秦皇岛同力达环保能源工程有限公司
Priority to CN2013101519783A priority Critical patent/CN103223279A/en
Publication of CN103223279A publication Critical patent/CN103223279A/en

Links

Abstract

The invention discloses an aeration-type air purifying device comprising an absorption liquid tank. A clean air discharge port is arranged on the upper part of the absorption liquid tank. A dosing pump is arranged on one side of the absorption tank, and is connected with a dosing tank. Aeration pipes are distributed in the absorption liquid tank, and microporous aeration heads are distributed on the aeration pipes. The aeration pipes are connected with an external booster fan and an external air filter through air inlet pipes. According to the invention, with the aeration technology, exhaust gas is dissolved in the absorption liquid with a micro-bubble form. The exhaust gas enters the absorption liquid in a form of micro-bubbles, such that gas-liquid reaction effect is effectively improved. Also, the gas is subjected to the reaction in the absorption liquid tank, such that gas-liquid reaction time is effectively prolonged, and gas-liquid exchange is better realized. Also, a plurality of technologies such as aeration, dissolving, stirring, decomposition, and filtering are integrated and optimized, such that pollution to the atmospheric environment is reduced. The device is suitable for air purification treatments of factory plants of chemical, tire, waterproof roll material industries, and other industries causing odors.

Description

The aeration type air cleaning facility

Technical field

The present invention relates to industrial working, factory building peculiar smell treatment technology and equipment, is a kind of aeration type air cleaning facility specifically.Be applied to chemical industry, tire, waterproof roll industry and other have the air cleaning of plant area's factory building of peculiar smell to handle.

Background technology

Air quality environmental pollution at present is serious day by day, and haze weather is increasing, has had a strong impact on the people's productive life and healthy.Equally, for the factory building of industrial area, the gas that the workshop emits by air regenerating device, often contain some polluters, as stink organic matters such as dust, R-SH, SOx, methylbenzene, formaldehyde, H2S, Ammonia, methyl mercaptan ore deposits.These waste gas at first produce harmful effect to the resident's health around factory building, the workshop.Secondly the aggravation to air environmental pollution, haze weather exerts a certain influence.Be generally used for the factory building of industrial area, when gas that the workshop emits by air regenerating device is handled, be the form that adopts the gas-liquid exchange, the form that is dissolved in liquid with gas is reacted.Processing form by the spray column spray has shortened the gas liquid reaction time, has reduced the gas-liquid exchange process, has caused the gas liquid reaction weak effect, can not effectively handle the gas that emits.

Summary of the invention

The invention provides a kind of aeration type air cleaning facility, waste gas is injected absorption liquid with the form of microbubble, improved the effect of gas liquid reaction.In course of reaction, existing in absorption liquid all the time of microbubble changed the form of gas-liquid exchange in the past, and the form that is dissolved in liquid with gas is reacted.

Technical scheme of the present invention is: a kind of aeration type air cleaning facility, comprise the absorption flow container, and be positioned at and absorb flow container top the pure air floss hole is housed, this an absorption flow container wherein side is equipped with dosing pump and is connected with dosing tank; Wherein described absorption flow container inside be distributed with aerated conduit and on the micro porous aeration head that is distributed with, this aerated conduit is connected with outside booster fan, air cleaner by admission line.

Among the present invention, it has one and absorbs accessory system, and this absorption accessory system comprises the cleaning solution filter tank, and this cleaning solution filter tank port of export is connected with the import of absorption flow container, and cleaning solution filter tank entrance point is connected with the outlet of absorption flow container by connecting filter pump.

Among the present invention, between described absorption flow container (17) and pure air floss hole (16), demister (15) is installed.

The beneficial effects of the utility model are:

1, the aeration type air cleaning facility is introduced the aeration process in the water technology, and the form of waste gas with microbubble is dissolved in the absorption liquid.Waste gas is that the form with microbubble enters and absorbs liquid, has effectively improved the effect of gas liquid reaction.

2, borrow the spray column technology of having recommended, gas enters the absorption flow container and reacts, being equivalent to liquid surrounds gas and reacts, promptly react with the form of " water-soluble " in gas, changed the processing form of traditional spray column spray, effectively prolong the gas liquid reaction time, better realized the gas-liquid exchange.

3, draw the water technology that reflected, spray column technology and still formula gas liquid reaction technology and some other air purifying process, collaborative and multiple process combination reaches optimization together with multiple technologies such as aeration, dissolving, stirring, decomposition, filtration, coverings.

Description of drawings

Fig. 1 is a schematic diagram of the present invention.

The specific embodiment

The invention will be further described below in conjunction with accompanying drawing embodiment.

See a kind of aeration type air cleaning facility shown in Figure 1, comprise absorbing flow container 17, reach the upper and lower side that absorbs flow container 17 1 sides water supplement port 8 and drain 7 are housed respectively, utilize water supplement port 8 to carry out moisturizing.When clearing up absorption flow container 17, discharge by drain 7.Be respectively equipped with liquid level gauge 9 and agitator 6 in the described absorption flow container 17.In described absorption flow container 17, be distributed with aerated conduit 18, and on described aerated conduit 18, be distributed with micro porous aeration head 5, be connected by admission line 4 one ends of aerated conduit 18 with the outside.These admission line 4 other ends connect booster fan 3, are connected with air cleaner 2 by booster fan 3 again, comprise that also air cleaner 2 is provided with air intlet 1.The effect of the booster fan 3 of present embodiment is to enter aerated conduit 18 by booster fan 3 through air cleaner 2 filtered airs, increases pressure and makes air enter the absorption liquid that absorbs in the flow container 17.And the effect of air cleaner 2 is that contaminated air is entered the flue dust that air cleaner 2 is removed a part, and oil smoke reduces the waste of back absorption liquid, and some soot dust granules are trapped in the air cleaner 2, reduces the probability that micro porous aeration head 5 is stopped up.In the present embodiment, because contaminated air forms a lot of micro-bubbles through after the micro porous aeration head 5, bubble diameter is little, and the gas-liquid interface area is big, and bubble spreads in absorption liquid evenly, makes pollutant fill part and is absorbed by liquid absorption.Stir by 6 pairs of absorption liquids of agitator again, microbubble is in the process that rises, absorption liquid is in rotation at a high speed, to bubble clash into, promote, seethe, a series of state variation such as fragmentation, aggravate a course of reaction of microbubble and absorption liquid, forced pollutant and absorption liquid in the gas to react.Taken in by liquid at this process particle, harmful molecule also reacts with absorption liquid.The present invention is equipped with demister 15 absorbing flow container 17 tops, and is positioned at demister 15 tops pure air floss hole 16 is housed.Demister 15 effects of the present invention are to guarantee to discharge from the waste gas that absorption liquid comes out, and avoid the discharge of the liquid of absorption liquid with waste gas.In addition, the caliber that the delivery pipe of pure air floss hole 16 is positioned at highest point strengthens, and to guarantee that air further underspeeds when effluxing, prevents that absorption liquid from entering atmosphere.Described absorption flow container 17 wherein a side connect dosing pumps 11 by drug feeding pipeline 12, be connected with dosing tank 10 by dosing pump 11.Can in absorbing flow container 17, implement dosing like this.The present invention comprises that also absorbing flow container 17 is connected with external absorption accessory system.Present embodiment absorbs accessory system, comprises cleaning solution filter tank 14, and these cleaning solution filter tank 14 ports of export are connected with absorption flow container 17, and cleaning solution filter tank 14 entrance points connect and compose circulation absorption accessory system by connecting filter pump 13 with absorption flow container 17.The effect of this absorption accessory system is to avoid air contains after air cleaner 2 filters dust granules and suspension to enter the aeration absorption system, keep the absorption liquid cleaning, and regularly absorption liquid is filtered by filter pump 13, remove some impurity particles in the absorption liquid, medicine system is regularly replenished fresh medicament to the aeration absorption system, guarantees assimilation effect.

Claims (3)

1. an aeration type air cleaning facility comprises the absorption flow container, is positioned to absorb flow container top the pure air floss hole is housed, and this an absorption flow container wherein side is equipped with dosing pump and is connected with dosing tank; It is characterized in that, described absorption flow container (17) inside be distributed with aerated conduit (18) and on the micro porous aeration head (5) that is distributed with, this aerated conduit (18) is connected by booster fan (3), the air cleaner (2) of admission line (4) with the outside.
2. aeration type air cleaning facility according to claim 1, it is characterized in that, it has one and absorbs accessory system, this absorption accessory system comprises cleaning solution filter tank (14), this cleaning solution filter tank (14) port of export is connected with the import of absorption flow container (17), and cleaning solution filter tank (14) entrance point is connected with absorption flow container (17) outlet by connecting filter pump (13).
3. aeration type air purifying process equipment according to claim 1 is characterized in that, between described absorption flow container (17) and pure air floss hole (16) demister (15) is installed.
CN2013101519783A 2013-04-27 2013-04-27 Aeration-type air purifying device CN103223279A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2013101519783A CN103223279A (en) 2013-04-27 2013-04-27 Aeration-type air purifying device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2013101519783A CN103223279A (en) 2013-04-27 2013-04-27 Aeration-type air purifying device

Publications (1)

Publication Number Publication Date
CN103223279A true CN103223279A (en) 2013-07-31

Family

ID=48834061

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2013101519783A CN103223279A (en) 2013-04-27 2013-04-27 Aeration-type air purifying device

Country Status (1)

Country Link
CN (1) CN103223279A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103611375A (en) * 2013-12-09 2014-03-05 林玲 Air haze purifier
CN103806519A (en) * 2014-02-24 2014-05-21 王红亮 Toilet bowl with air purification function
CN104759171A (en) * 2015-03-26 2015-07-08 徐州工程学院 Compound industrial dust removal device
CN105617707A (en) * 2016-03-02 2016-06-01 温州市亿一机械有限公司 Exhaust gas recycling and heat exchange system
CN105771485A (en) * 2016-04-27 2016-07-20 京东方科技集团股份有限公司 Purifier
CN105833625A (en) * 2015-01-14 2016-08-10 李俊德 Gas filtering cylinder structure
CN106268140A (en) * 2016-09-04 2017-01-04 佛山市恒学科技服务有限公司 A kind of triethylamine exhaust gas cleaner and purification method
CN106732308A (en) * 2017-01-13 2017-05-31 浙江大学 A kind of micro- bubbling gas-liquid reactor

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2483076Y (en) * 2001-04-23 2002-03-27 崔同顺 Boiling reaction tank of tail gas purifying apparatus
US20020174773A1 (en) * 2001-05-24 2002-11-28 Kuai-Chung Cheng Dust Recovery device
AU2003212698A1 (en) * 2002-03-19 2003-09-29 Bum-Hong Kim Waste gas purifier
CN200963566Y (en) * 2006-09-28 2007-10-24 宜兴和亿昌环保有限公司 Flue gas desulfurizing spraying adsorption tower
CN201701843U (en) * 2010-05-31 2011-01-12 西安昊芯自动化工程有限公司 Blowing-bath type dust collection desulfurizer
CN102319534A (en) * 2011-08-25 2012-01-18 江西金达莱环保研发中心有限公司 Method for exhaust gas purification
CN202315599U (en) * 2011-12-06 2012-07-11 重庆生竹科技发展有限公司 Water bath dust removing system

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2483076Y (en) * 2001-04-23 2002-03-27 崔同顺 Boiling reaction tank of tail gas purifying apparatus
US20020174773A1 (en) * 2001-05-24 2002-11-28 Kuai-Chung Cheng Dust Recovery device
AU2003212698A1 (en) * 2002-03-19 2003-09-29 Bum-Hong Kim Waste gas purifier
CN200963566Y (en) * 2006-09-28 2007-10-24 宜兴和亿昌环保有限公司 Flue gas desulfurizing spraying adsorption tower
CN201701843U (en) * 2010-05-31 2011-01-12 西安昊芯自动化工程有限公司 Blowing-bath type dust collection desulfurizer
CN102319534A (en) * 2011-08-25 2012-01-18 江西金达莱环保研发中心有限公司 Method for exhaust gas purification
CN202315599U (en) * 2011-12-06 2012-07-11 重庆生竹科技发展有限公司 Water bath dust removing system

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103611375A (en) * 2013-12-09 2014-03-05 林玲 Air haze purifier
CN103611375B (en) * 2013-12-09 2016-08-31 林玲 Air haze purifier
CN103806519A (en) * 2014-02-24 2014-05-21 王红亮 Toilet bowl with air purification function
CN105833625B (en) * 2015-01-14 2018-02-16 李俊德 A kind of gas filtration tube structure
CN105833625A (en) * 2015-01-14 2016-08-10 李俊德 Gas filtering cylinder structure
CN104759171A (en) * 2015-03-26 2015-07-08 徐州工程学院 Compound industrial dust removal device
CN105617707A (en) * 2016-03-02 2016-06-01 温州市亿一机械有限公司 Exhaust gas recycling and heat exchange system
CN105771485A (en) * 2016-04-27 2016-07-20 京东方科技集团股份有限公司 Purifier
CN106268140A (en) * 2016-09-04 2017-01-04 佛山市恒学科技服务有限公司 A kind of triethylamine exhaust gas cleaner and purification method
CN106732308A (en) * 2017-01-13 2017-05-31 浙江大学 A kind of micro- bubbling gas-liquid reactor

Similar Documents

Publication Publication Date Title
CN203556253U (en) Novel waste gas treatment system
CN203916433U (en) A kind of gas cleaning plant
CN203017884U (en) Plastic and metal molded vapor-phase oxidation process treatment system for collecting waste gas
CN202105575U (en) Wet type waste gas comprehensive control apparatus
KR101443157B1 (en) Apparatus for purification of pollution gas
CN103949131A (en) Photochemistry coupling low-temperature plasma waste gas treatment device
CN103505969A (en) Waste gas and dust treating device
CN201959716U (en) Combination ammonia desulfurization tower
CN204522619U (en) A kind of waste gas, PM2.5 particle, haze absorption cleaning car
CN204672123U (en) A kind of waste gas purification tower with swirling flow plate
CN202460438U (en) Desulfurizing liquid oxidation and purification combined device
CN206655728U (en) A kind of automobile exhaust gas processing apparatus
CN102755818B (en) UV spray painting waste gas purification system and method
CN201988299U (en) Waste gas purifying device
CN204345686U (en) A kind of Cremation Machine device for purifying and treating tail gas
CN202835409U (en) Smoke dust waste-heat utilization and dust removing device of low-capacity boiler
CN207445855U (en) A kind of waste gas purification filter net device for production equipment
CN205700102U (en) A kind of exhaust gas purification and treatment device of band gas washing function
CN105727720A (en) Spiral bubble flue gas cleaning device
CN202909625U (en) Painting organic waste gas treatment device
CN105268296A (en) Acid mist purifying tower
CN204051377U (en) Effective integrated soda acid and organic exhaust gas adsorption device
CN103263812A (en) Water curtain type paint mist filter
CN205461573U (en) A spray column for exhaust -gas treatment
CN104338436B (en) A kind of efficient processing high concentration is mixed the deodoration system of foul smell

Legal Events

Date Code Title Description
PB01 Publication
C06 Publication
SE01 Entry into force of request for substantive examination
C10 Entry into substantive examination
CB02 Change of applicant information

Address after: 066004 No. 8 Jinshan North Road, Qinhuangdao economic and Technological Development Zone, Hebei, China

Applicant after: QINHUANGDAO TONGLIDA ENVIRONMENTAL ENERGY CORP.

Address before: 066004 Hebei city of Qinhuangdao Province Economic and Technological Development Zone, Golden Hill Road No. 8

Applicant before: Qinhuangdao TONGLIDA Environmental Energy Engineering Co., Ltd.

COR Change of bibliographic data
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20130731

WD01 Invention patent application deemed withdrawn after publication