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CN201211462Y - High pressure fine water mist desulfurizing-dusting apparatus with prepositive dry dust collector - Google Patents

High pressure fine water mist desulfurizing-dusting apparatus with prepositive dry dust collector
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Publication number
CN201211462Y
CN201211462YCNU2008200710284UCN200820071028UCN201211462YCN 201211462 YCN201211462 YCN 201211462YCN U2008200710284 UCNU2008200710284 UCN U2008200710284UCN 200820071028 UCN200820071028 UCN 200820071028UCN 201211462 YCN201211462 YCN 201211462Y
Authority
CN
China
Prior art keywords
absorption tower
communicated
high pressure
pressure pump
absorption column
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
CNU2008200710284U
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Chinese (zh)
Inventor
许智远
叶兆平
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 Electromechanical Manufacturing 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 LtdfiledCriticalHenan Hailite Electromechanical Manufacturing Co Ltd
Priority to CNU2008200710284UpriorityCriticalpatent/CN201211462Y/en
Application grantedgrantedCritical
Publication of CN201211462YpublicationCriticalpatent/CN201211462Y/en
Anticipated expirationlegal-statusCritical
Expired - Lifetimelegal-statusCriticalCurrent

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Abstract

The utility model relates to a high pressure fine water fog desulfurating and dedusting device with a front dry separator, which can effectively solve the problems of large rebuilding difficulty, large investment and high maintenance cost. The device comprises a dry separator, absorption columns and a high pressure pump. An induced draft fan on the flue of a fume inlet is communicated with a first absorption column through the dry separator. An outlet end of a second absorption column that is communicated with the first absorption column is provided with a demister which is communicated with a chimney. The first absorption column is connected with a flow tank through a pipeline, and is connected with an outlet end of the high pressure pump on the spraying pipe. The second absorption column is connected with the flow tank. A dynamic filter is connected with the high pressure pump, and the front end of the high pressure pump is provided with a centrifugal pump that is communicated with an alkali circulating water tank. The flow tank is communicated with the alkali circulating water tank through a lauter tank. The first absorption column and the second absorption column are respectively provided with fine water fog spray heads that are respectively communicated with the spraying pipe. The device is simple in structure, small in floor space, comparatively low in investment, energy saving and environment-friendly, is an innovation for the prior dedusting and desulfurating device, and has good economic benefits and social benefits.

Description

A kind of high-pressure fine water mist desulfurized dust collector with front-located dry precipitator
One, technical field
The utility model relates to desulfurating dust-removing equipment, particularly a kind of high-pressure fine water mist desulfurized dust collector with front-located dry precipitator.
Two, background technology
China's atmosphere polluting problem is more serious at present, has caused the great attention of Party and government, and national in recent years the appearance in succession with the atmosphere method is 20 multi-section laws and regulations of core, and dynamics is big unprecedented.Show according to China Environmental State Bulletin: " air environmental pollution of China is still based on coal smoke type, and major pollutants are sulfur dioxide (SO2) and flue dust, coal-burning boiler such as thermal power plant, iron and steel, metallurgy etc. reduce discharging sulfur dioxide (SO at present2) main path have: coal washing, lime stone (lime) gypsum wet, sea water desulfuration method, a flue gas recirculation sulfuration bed doctor treatment, electronic beam method desulfurization etc. surplus in the of totally ten the desulfurizer of kind of technology in commercialized running or carried out industrial demonstration.The method of the dedusting of coal-burning boiler such as thermal power plant, iron and steel, metallurgy etc. has electric precipitation and bag-type dust at present.Lower and the operating cost of the flue gas desulfur device desulfuration efficiency of middle and small burn coal boiler also compares higher, energy-conservation, the development trend that reduces discharging that have been not suitable for that country proposes; If coal-burning boiler does not reach national specified discharge standard and will be ordered within a certain time explosion in view of national policy, narrow and smallly use traditional method upgrading difficulty very big again and the enterprise that is using middle-size and small-size desulfation dust-extraction device is often local, and output investment ratio is bigger, maintenance cost is also than higher, so improvement is imperative.
Three, utility model content
At above-mentioned situation, for overcoming the defective of prior art, the purpose of the utility model just provides a kind of high-pressure fine water mist desulfurized dust collector with front-located dry precipitator, it is big effectively to solve the transformation difficulty, investment is big, the problem that maintenance cost is high, the utility model is realized by the following technical solutions: include dry collector, absorption tower and high-pressure pump, on the flue of gas approach air-introduced machine is housed, and be connected with first absorption tower through dry collector, first absorption tower is communicated with second absorption tower through flue, on the pipeline of the second absorption tower port of export demister is housed, demister is connected with chimney, first absorption tower links to each other with sedimentation basin through pipeline, and it is continuous with the high-pressure pump port of export on the shower, second absorption tower links to each other with sedimentation basin through pipeline, and it is continuous with shower, the dynamic filter rear end links to each other with the entrance point of high-pressure pump, the dynamic filter front end is equipped with the centrifugal pump that is communicated with the alkali circulating water chennel, sedimentation basin is communicated with the alkali circulating water chennel through filter pocket, and the short transverse along tower in first absorption tower and second absorption tower is equipped with the multilayer fine mist spray head that is connected with shower successively.
The utility model is simple in structure, and floor space is little, and output investment ratio is lower, and energy-saving and environmental protection are the innovations greatly on the existing dust-removal and desulfurizing equipment, and good economic and social benefit is arranged.
Four, description of drawings
Fig. 1 is a structural front view of the present utility model.
Fig. 2 is an absorption tower of the present utility model section of structure.
Five, the specific embodiment
Below in conjunction with accompanying drawing the specific embodiment of the present utility model is elaborated.
By Fig. 1, Fig. 2 provides, the utility model includes dry collector, absorption tower and high-pressure pump, on the flue 7 of gas approach air-introduced machine 5 is housed, and be connected with first absorption towers 1 through dry collector 3, first absorption tower 1 is communicated with second absorption tower 2 through flue, demister 4 is housed on the pipeline of the second absorption tower port of export, demister is connected with chimney 6, first absorption tower links to each other with sedimentation basin 11 through pipeline 15, and it is continuous with 8 ports of export of the high-pressure pump on the shower, second absorption tower 2 links to each other with sedimentation basin 11 through pipeline 16, and it is continuous with shower 18, dynamic filter 9 rear ends link to each other with the entrance point of high-pressure pump 8, the dynamic filter front end is equipped with the centrifugal pump 10 that is communicated with alkali circulating water chennel 13, sedimentation basin 11 is communicated with alkali circulating water chennel 13 through filter pocket 12, and the multilayer fine mist spray head 17 that is connected with shower is equipped with successively with second absorption tower, 2 interior short transverses along tower in first absorption tower 1.
In order to guarantee result of use, said high-pressure pump outlet conduit links to each other with second absorption tower 2 through threeway; Alkali circulating water chennel inlet is equipped with joins alkali groove 14; Said demister is a vertical dismountable, but the periodic flushing demister guarantees that because of issuable dead angle knot ash in the long-time running demister efficiently turns round; Novel JNS corrosionproof steel against sulfuric acid at dew point can be adopted in said first absorption tower, second absorption tower, its tower body, and inwall is coated glass resin flake coating or other corrosion resistance material layer to improve the corrosion resistance of equipment, increases the service life.
Working condition of the present utility model is, flue gas is introduced into dry collector 3 through primary dust removing by air-introduced machine 5 through flue 7, flue gas through pre-dedusting enters first absorption tower 1 and second absorption tower 2 by flue, all be furnished with multilayer fine mist spray head 17 in two absorption towers, short transverse along tower is placed successively, the water that adds desulfurizing agent (NaOH) is sent into shower nozzle 17 and is formed superfine water smoke ejection through pipeline by high-pressure pump 8, flue gas runs into the heavy pressure fine spray of downward high speed ejection in the uphill process in the absorption tower, gas, Gu, the liquid three-phase fully contacts, also have a spot of small grain size dust fully to contact with thin water smoke, constantly cohesion becomes bulky grain, under the effect of gravity, land, and be discharged in the sedimentation basin 11 SO2The heavy pressure fine spray seizure, reacting generating salt and the sulphite that are contained alkaline matter, flue gas cool-down, frequent impact, it is big that droplet merges change, and sedimentation also is discharged in the sedimentation basin 11, adds white lime [Ca (OH) in sedimentation basin2], the formation mass concentration is 1.8 ‰ solution, white lime [Ca (OH)2] generate NaOH with the reaction of sulfate and sulphite after, through filter pocket 12 filtrations, Separation of Solid and Liquid, supernatant flows in the alkali circulating water chennel 13, in circulating water chennel 13, add the NaOH or the NaOH aqueous solution (the NaOH aqueous solution is dissolved in water by NaOH and forms) by joining alkali groove 14, in alkali circulating water chennel 13, inject water purification simultaneously, stir, the formation mass concentration is 2 ‰ NaOH solution, be pumped in the heavy pressure fine spray system by centrifugal pump 10 and recycle, form Closed Recirculation for Ash Water, prevent secondary pollution, and reduce alkali consumption and operation cost
Flue gas after the once desulfurization dedusting enters second absorption tower 2 through pipeline by first absorption tower 1, also has micro-small grain size dust to be removed by two to three layers of thin water smoke of two towers, also also has a spot of SO2Be absorbed through two to three layers of thin water smoke, reaction, generate sulfate and sulphite etc. and be removed with dustshot, flue gas is after demister 4 is removed contained supersaturation moisture, the flue gas that reaches discharge standard or discharging standards delivered in the chimney 6 entered atmosphere.
Technical characterstic of the present utility model is:
1) desulfurization dust-removing efficiency height, SR is little;
2) required desulfurizing tower volume is little, and investment cost is relatively low;
3) the consumption liquid measure is little, gas liquid ratio is low, and alkali consumption also lacks than additive method;
4) the coal-fired rate range of Shi Yonging is big;
5) system is reliable, and operating cost is low;
Learn by above-mentioned situation, the utlity model has smoke elimination efficiently, dedusting, desulfurizing function and corrosion-resistant, wear-resistant, characteristics such as life cycle is long, be fit to use all over the world, also can add other expands apparatus function as denitrfying agent, defluorinating agent etc., to adapt to more and more higher from now on environmental requirement, integrate desulfurization, dedusting function, cost reduces with traditional comparing greatly, and can realize long-term efficient running, meet energy-conservation, reduction of discharging requirement that country proposes, thereby produce good economic benefit and social benefit.

Claims (5)

1, a kind of high-pressure fine water mist desulfurized dust collector with front-located dry precipitator, include dry collector, absorption tower and high-pressure pump, it is characterized in that, air-introduced machine (5) is housed on the flue of gas approach (7), and be connected with first absorption tower (1) through dry collector (3), first absorption tower (1) is communicated with second absorption tower (2) through flue, demister (4) is housed on the pipeline of the second absorption tower port of export, the same chimney of demister (6) is connected, first absorption tower (1) links to each other with sedimentation basin (11) through pipeline (15), and high-pressure pump (8) port of export on the same shower (18) links to each other, second absorption tower (2) links to each other with sedimentation basin (11) through pipeline (16), and same shower (18) links to each other, the entrance point of the same high-pressure pump in dynamic filter (9) rear end (8) links to each other, dynamic filter (9) front end is equipped with the centrifugal pump (10) that is communicated with alkali circulating water chennel (13), sedimentation basin (11) is communicated with alkali circulating water chennel (13) through filter pocket (12), and first absorption tower (1) is equipped with the multilayer fine mist spray head (17) that is connected with shower successively with second absorption tower (2) interior short transverse along tower.
CNU2008200710284U2008-06-162008-06-16High pressure fine water mist desulfurizing-dusting apparatus with prepositive dry dust collectorExpired - LifetimeCN201211462Y (en)

Priority Applications (1)

Application NumberPriority DateFiling DateTitle
CNU2008200710284UCN201211462Y (en)2008-06-162008-06-16High pressure fine water mist desulfurizing-dusting apparatus with prepositive dry dust collector

Applications Claiming Priority (1)

Application NumberPriority DateFiling DateTitle
CNU2008200710284UCN201211462Y (en)2008-06-162008-06-16High pressure fine water mist desulfurizing-dusting apparatus with prepositive dry dust collector

Publications (1)

Publication NumberPublication Date
CN201211462Ytrue CN201211462Y (en)2009-03-25

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Family Applications (1)

Application NumberTitlePriority DateFiling Date
CNU2008200710284UExpired - LifetimeCN201211462Y (en)2008-06-162008-06-16High pressure fine water mist desulfurizing-dusting apparatus with prepositive dry dust collector

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN101298022B (en)*2008-06-162010-12-08河南海力特机电制造有限公司High-pressure fine water mist desulfurized dust collector with front-located dry precipitator and using method thereof
CN112169574A (en)*2019-07-052021-01-05福建省坤宁环保工程有限公司Coal fired boiler SOx/NOx control clean system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN101298022B (en)*2008-06-162010-12-08河南海力特机电制造有限公司High-pressure fine water mist desulfurized dust collector with front-located dry precipitator and using method thereof
CN112169574A (en)*2019-07-052021-01-05福建省坤宁环保工程有限公司Coal fired boiler SOx/NOx control clean system

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DateCodeTitleDescription
C14Grant of patent or utility model
GR01Patent grant
AV01Patent right actively abandoned

Granted publication date:20090325

Effective date of abandoning:20080616


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