CN201906554U - Waste-gas secondary treatment purification device - Google Patents

Waste-gas secondary treatment purification device Download PDF

Info

Publication number
CN201906554U
CN201906554U CN2010206574825U CN201020657482U CN201906554U CN 201906554 U CN201906554 U CN 201906554U CN 2010206574825 U CN2010206574825 U CN 2010206574825U CN 201020657482 U CN201020657482 U CN 201020657482U CN 201906554 U CN201906554 U CN 201906554U
Authority
CN
China
Prior art keywords
purification tower
gas
utility
model
waste
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 - Fee Related
Application number
CN2010206574825U
Other languages
Chinese (zh)
Inventor
蒋皓
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.)
JIANGSU ENVIFRP ANTISEPSIS EQUIPMENT Co Ltd
Original Assignee
JIANGSU ENVIFRP ANTISEPSIS EQUIPMENT 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 JIANGSU ENVIFRP ANTISEPSIS EQUIPMENT Co Ltd filed Critical JIANGSU ENVIFRP ANTISEPSIS EQUIPMENT Co Ltd
Priority to CN2010206574825U priority Critical patent/CN201906554U/en
Application granted granted Critical
Publication of CN201906554U publication Critical patent/CN201906554U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

The utility model relates to a waste-gas secondary treatment purification device, comprising a primary purification tower, a secondary purification tower and a fan capable of pressing gas into the secondary purification tower from the primary purification tower, wherein the primary purification tower is internally provided with a first anti-corrosion water-circulating pump, a first spraying device and a first filtering filler device, and the outlet of the primary purification tower is provided with a liquid-removal device. In the utility model, by adopting a secondary purification treatment mode, acidic waste gas generated in industrial production can be further purified and treated, so that the finally discharged waste water and gas can reach the atmospheric emission standard.

Description

A kind of waste gas two stage treatment purifier
Technical field
The utility model relates to the treatment of waste gas system, especially a kind of two stage treatment purifier to the acid waste gas that produced in production of polysilicon.。
Background technology
Prosperity and development along with photovoltaic industry, increasing medium-sized and small enterprises begin crystalline silicon material is processed and handled, and most enterprise most when the silicon material is corroded all be to adopt the mixed liquor of nitric acid, hydrofluoric acid and hydrochloric acid to carry out the product corrosion, thereby will produce Main Ingredients and Appearance is the escaping gas of nitrogen oxide, a spot of hydrogen fluoride gas, a spot of hydrogen chloride gas and chlorine hydrogen silane, and the initial concentration of the sour gas that is produced is all at 150mg/m 3More than.And according to the requirement of " discharge standard of air pollutants ", when the aiutage height was 30m, the highest permission concentration of emission of secondary discharge standard NOx was 240mg/m 3, the highest permission rate of discharge is 4.4kg/h; The highest permission concentration of emission of secondary discharge standard HF is 9mg/m 3, the highest permission rate of discharge is 0.59kg/h; The highest permission concentration of emission of secondary discharge standard HCL is 100mg/m 3, the highest permission rate of discharge is 1.4kg/h, therefore, exhaust gas discharging concentration is respectively after the treatment and purification: NOX<240mg/m 3, HF<9mg/m 3, HCL<100mg/m 3
At present, in order to reach this standard-required, processing mode to this type of sour gas on the market is to handle or other simple exhaust-gas treatment modes through the one-level wet purification, but, because the feature of a large amount of nitrogen oxide, hydrogen fluoride gas and the hydrogen chloride gas that are produced in process of production shows as burst, intermittent, and concentration is higher, so simple exhaust-gas treatment mode can't be real waste gas is improved comprehensively handled.
The utility model content
The technical problems to be solved in the utility model is: a kind of simple in structure, waste gas purifying efficiency is high, final toxic emission concentration is little waste gas two stage treatment purifier is provided.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of waste gas two stage treatment purifier, comprise first class purification tower, secondary purification tower and gas can be pressed into blower fan in the secondary purification tower from the first class purification tower, be provided with the first corrosion-resistant water circulating pump, first spray equipment and the first filter packing device in the described first class purification tower, the exit of described first class purification tower is provided with dewatering device.
The beneficial effects of the utility model are, solved the defective that exists in the background technology, the mode that adopts secondary purification to handle can further be carried out purified treatment with the acid waste gas that is produced in the industrial production, makes last waste water and gas of discharging can reach the standard of airborne release.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is the structural representation of preferred embodiment of the present utility model;
Among the figure: 1, first class purification tower; 11, dewatering device; 2, secondary purification tower; 21, take off the mist device; 3, blower fan; 31, volume damper; 4, gauze filter.
The specific embodiment
With preferred embodiment the utility model is described in further detail in conjunction with the accompanying drawings now.These accompanying drawings are the schematic diagram of simplification, basic structure of the present utility model only is described in a schematic way, so it only show the formation relevant with the utility model.
A kind of waste gas two stage treatment purifier as shown in Figure 1, comprise first class purification tower 1, secondary purification tower 2 and gas can be pressed into blower fan 3 in the secondary purification tower 2 from first class purification tower 1, described first class purification tower 1 is by the air inlet of pipeline connection blower fan 3, and described secondary purification tower 2 is connected by the gas outlet of pipeline with blower fan 3.
Blower fan 3 described in the utility model is the fiberglass centrifugal fan, and blower fan 3 is by variable-frequency motor driving work, and having in the blower fan 3 by carbon steel is the impeller of skeleton, and the gas outlet of blower fan 3 is provided with volume damper 31 in order to regulate the size of blower fan 3 air quantity.Described blower fan 3 quantity are set to two, normal a use, and another is as standby fan 3, to move according to regular switchover operation of ruuning situation or failover.
All be provided with corrosion-resistant water circulating pump, spray equipment and filter packing device in first class purification tower 1 described in the utility model and the secondary purification tower 2, the exit of described first class purification tower 1 is provided with dewatering device 11, and the exit of secondary purification tower 2 is provided with takes off mist device 21.
The utility model is provided with gauze filter 4 in order to guarantee the normal operation of spray equipment at the water circulating pump inlet, damages water pump and plug nozzle in case foreign material enter, and influence is used.The shower nozzle material is a RPP, through single injection-molded, and intensity height, long service life.
Cleaning principle of the present utility model is: acid waste gas is at first sucked in the first class purification tower 1 by blower fan 3, after waste gas is distributed by the water conservancy diversion distribution apparatus in the tower, contact processing with reverse direct intersection of absorbent solution, enter inner core filler zone then and carry out repeatedly repeatedly filler filtration of liquid phase reactor, make waste gas in tower, have the long time fully to filter contact, produce liquid film and spray generation mass transfer reaction, guarantee qualified discharge.Contain sour waste gas behind first class purification tower 1 abundant absorption cleaning, and dewatering device 11 through being provided with in the tower exit, after removing the water smoke in the system, be pressed into secondary purification tower 2 by blower fan 3 again, absorb and after the interception of multilayer filler absorbs processing through the multilayer spray once more at tower inner acidic waste gas and absorption liquid, guarantee qualified discharge, after the tower exit be provided with take off 21 demists of mist device after discharge drum discharging atmosphere.Waste water enters Sewage Disposal through pipeline, focuses on.
What describe in the above specification is the specific embodiment of the present utility model, various not illustrating is construed as limiting flesh and blood of the present utility model, the person of an ordinary skill in the technical field after having read specification can to before the described specific embodiment make an amendment or be out of shape, and do not deviate from the essence and the scope of utility model.

Claims (1)

1. waste gas two stage treatment purifier, it is characterized in that: comprise first class purification tower (1), secondary purification tower (2) and gas can be pressed into the interior blower fan (3) of secondary purification tower (2) from first class purification tower (1), be provided with the first corrosion-resistant water circulating pump, first spray equipment and the first filter packing device in the described first class purification tower (1), the exit of described first class purification tower (1) is provided with dewatering device (11).
CN2010206574825U 2010-12-14 2010-12-14 Waste-gas secondary treatment purification device Expired - Fee Related CN201906554U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010206574825U CN201906554U (en) 2010-12-14 2010-12-14 Waste-gas secondary treatment purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010206574825U CN201906554U (en) 2010-12-14 2010-12-14 Waste-gas secondary treatment purification device

Publications (1)

Publication Number Publication Date
CN201906554U true CN201906554U (en) 2011-07-27

Family

ID=44298764

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010206574825U Expired - Fee Related CN201906554U (en) 2010-12-14 2010-12-14 Waste-gas secondary treatment purification device

Country Status (1)

Country Link
CN (1) CN201906554U (en)

Similar Documents

Publication Publication Date Title
US11014044B2 (en) Waste gas purification system and method
CN205699973U (en) The special tail gas clean-up of a kind of Industrial Boiler, waste heat recovery processing device
CN106861415B (en) Flue gas purification system and method
CN208115480U (en) A kind of emission-control equipment of co-oxidation
CN212068318U (en) Small-size domestic waste incinerator flue gas minimum discharge integration processing system
CN108580044A (en) A kind of high-efficiency environment friendly plant gas dust removal and filtration equipment
CN111001271A (en) Small-size washing tower is used in lithium hexafluorophosphate production
CN201906556U (en) Waste gas treatment and purification device
CN201906553U (en) Waste-gas secondary treatment and purification device with fan
CN201940173U (en) Secondary waste gas treatment purifier
CN204093277U (en) Trimethylamine waste gas pollution control and treatment system
CN201921624U (en) Exhaust gas purification device
CN207734819U (en) A kind of burning boiler emission-control equipment
CN207324501U (en) A kind of desulphurization denitration purifying and dedusting device of flue gas
CN201906554U (en) Waste-gas secondary treatment purification device
CN206404519U (en) A kind of exhaust treatment system
CN106039913B (en) A kind of flue gas purification system
CN201949789U (en) Absorption treatment device for acidolysis tail gas of titanium white
CN205392152U (en) Exhaust -gas treatment equipment based on AOP advanced oxidation technologies
CN208097826U (en) A kind of purification of chemical waste gas equipment
CN208642164U (en) A kind of recycling of waste gas purification uses equipment
CN207614648U (en) A kind of device of UV photodissociation processing organic exhaust gas
CN201399321Y (en) Flue gas purification device utilizing semidry method
CN206240301U (en) A kind of high-efficiency desulfurization denitrification apparatus for industrial waste gas
CN202538635U (en) Secondary absorption device of exhaust gas employing comprehensive recovery process of eodymium iron boron scrap

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Assignee: JIANGSU HUA HONG NEW ENERGY CO., LTD.

Assignor: Jiangsu Envifrp Antisepsis Equipment Co., Ltd.

Contract record no.: 2014320000576

Denomination of utility model: Waste-gas secondary treatment purification device

Granted publication date: 20110727

License type: Exclusive License

Record date: 20140715

LICC Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model
EC01 Cancellation of recordation of patent licensing contract

Assignee: JIANGSU HUA HONG NEW ENERGY CO., LTD.

Assignor: Jiangsu Envifrp Antisepsis Equipment Co., Ltd.

Contract record no.: 2014320000576

Date of cancellation: 20160803

LICC Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110727

Termination date: 20171214

CF01 Termination of patent right due to non-payment of annual fee