CN2672078Y - Electric duster for blast furnace gas purifying - Google Patents
Electric duster for blast furnace gas purifying Download PDFInfo
- Publication number
- CN2672078Y CN2672078Y CN 200320105831 CN200320105831U CN2672078Y CN 2672078 Y CN2672078 Y CN 2672078Y CN 200320105831 CN200320105831 CN 200320105831 CN 200320105831 U CN200320105831 U CN 200320105831U CN 2672078 Y CN2672078 Y CN 2672078Y
- Authority
- CN
- China
- Prior art keywords
- electric precipitator
- blast furnace
- furnace gas
- gas purification
- duster
- 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
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Abstract
The utility model is applied in extract dust removing device for top gas purifying, also applied to the dust removing of other flammable and explosive gas, such as revolving furnace, dust removing of city gas, continuous casting and the flame cleaning and dust removing of rolled steel, etc. The electric duster for blast furnace gas purifying is composed of a body, water supply pipes, a nitrogen-charge exhausting pipe, an impulse vibrator, an explosion venting device. The body of the duster is a box. The inlet of the body is provided with an air flow distributing plate. A precipitation electrode and a discharge electrode are arranged in the body. A precipitation electrode cleaner and a water nozzle for the discharge electrode are positioned at the top of the duster. An electromagnetic hammer impulse vibrator is arranged at the top of the duster, while a bucket shape water yielding device is arranged at the lower part of the duster. The utility model has the advantages of reasonable structure, good effect on dust removing and lower price than imported devices.
Description
Technical field
The utility model is to be used for the smart dust removal installation that blast furnace gas purification is used, and is applicable to that also other are inflammable, the dedusting of explosion hazard gases, as the flame cleaning of converter, town gas dedusting, continuous casting and steel rolling and dedusting etc.
Background technology
At present, the dust removal installation of blast furnace gas generally all adopts import equipment, and dust removing effects is relatively good, but import equipment costs an arm and a leg, and conditions such as maintenance of the equipment also are subjected to certain limitation.
The utility model content
The purpose of this utility model provides a kind of reasonable price, well behaved blast furnace gas purification electric precipitator.This electric precipitator satisfies users' such as heater for rolling steel, boiler needs by the udst separation to blast furnace gas to guarantee the blast furnace gas dustiness.
The electric precipitator principle of work is a dusty gas by the electric precipitator loudspeaker that enter the mouth, after the airflow-distribution board current-sharing, enter electric field equably, the nozzle that is configured in import loudspeaker and electric field top sprays in the coal gas of the electric field of flowing through after making water fogging, make and be cleaned temperature of gas, pressure, humidity and reach the purification requirement, after containing the suspension liquid particle and entering electric field, by charged and under the effect of electrical forces, captured by dust collecting electrode, and flow in the ash bucket along dust collecting electrode, enter settling tank by ash bucket then, and the coal gas after purifying is discharged from the electric precipitator outlet by electric field.
Constitutional features of the present utility model is described below:
The blast furnace gas purification electric precipitator is characterized in that: blast furnace gas purification is made up of body, water supply line, inflated with nitrogen gas exhaust duct, pulse vibrator, explosion venting device with electric precipitator; The fly-ash separator body is a body structure, be provided with dust collecting electrode and discharge electrode in body interior, be provided with the water spouting nozzle of cleaning dust collecting electrode and discharge electrode at the electric precipitator top, the fly-ash separator lower end is provided with ash bucket, be provided with nitrogen purging device on the fly-ash separator body, the nitrogen discharge device is located at dust remover roof.For making the electric precipitator safe and stable operation, on electric precipitator, be provided with a plurality of explosion venting valves.
The beneficial effects of the utility model are: rational in infrastructure, and good dedusting effect, price is low than import equipment.Charged spray Cleaning for High Capacity technology sprays into atomized water and clears up dust collecting electrode and discharge electrode, does not need the cut off high power supply during spraying, and spraying intensity and spray controlling cycle system make the electric field cleaning performance keep splendid state, reduce working cost.The high-efficiency dust collecting device adopts proprietary bimodal plate template structure, make on the dust collecting electrode surface liquid film that forms continuous flow and increase gather dust electrode surface-area and reduce air-flow velocity near the collecting plate place.The dust collecting electrode surface scribbles the electric precipitation conductive anti-corrosion coating, has higher corrosion-resistant and wear resistance.Explosion venting device control for making the electric precipitator safe and stable operation, is provided with a plurality of explosion venting valves on electric precipitator.This explosion venting valve has releasing pressure automatically, automatically replies function, is safety device in the inflammable gas dedusting.The electromagnetic hammer rapping apparatus at deposit phenomenon on collecting plate and discharge electrode of plaster, has adopted top electromagnetic hammer pulse vibrator.The size and the shaking cycle of its rapping power are adjustable.At cold district, fly-ash separator body and all pipelines are provided with lagging facility.
Description of drawings
Fig. 1 is the front view of combustible gas electric precipitator.
Fig. 2 is the left view of combustible gas electric precipitator.
Fig. 3 is the vertical view of combustible gas electric precipitator.
Embodiment
See Fig. 1, blast furnace gas purification is made up of body 1, water supply line 13, inflated with nitrogen gas exhaust duct 11, pulse vibrator 5,6, explosion venting device with electric precipitator.Fly-ash separator body 1 is a body structure, is provided with airflow-distribution board 14 in the ingress of body 1, is provided with dust collecting electrode 2 and discharge electrode 3 in body interior, and dust collecting electrode 2 and discharge electrode 3 are fixing by suspension apparatus 4.For make on the dust collecting electrode surface liquid film that forms continuous flow and increase gather dust electrode surface-area and reduce air-flow velocity near the collecting plate place, dust collecting electrode 2 adopts dull and stereotyped or bimodal plate slab structure, scribble the special-purpose conductive anti-corrosion coating of electric precipitation on the dust collecting electrode surface, have higher erosion resistance and wear resistance.Discharge electrode adopts pipe linear formula of thorn or the linear formula of strand.
Be provided with the water spouting nozzle 8 of cleaning dust collecting electrode and discharge electrode at the electric precipitator top, water spouting nozzle 8 connects feeding apparatus 13, is used for spraying into atomized water and clears up dust collecting electrode and discharge electrode.
For making the electric precipitator safe and stable operation, on electric precipitator, be provided with a plurality of explosion venting valves 10, be provided with water trap 9 in the fly-ash separator exit.(Fig. 3)
Be directed to deposit phenomenon on collecting plate and discharge electrode of dust, be provided with electromagnetic hammer pulse vibrator 5,6 in the fly-ash separator bodies top.
At cold district, this dust removal installation is provided with attemperator, is provided with insulator insulation can 15 at the electric precipitator top, and explosion-proof INCREASEDSAFETY electric heater 7 (Fig. 2) is installed on insulator insulation can 15.
The fly-ash separator lower end is provided with ash bucket 16, and body is provided with nitrogen purging device 11, and nitrogen discharge device 12 is located at dust remover roof.
Claims (8)
1, blast furnace gas purification electric precipitator is characterized in that: blast furnace gas purification is made up of body, water supply line, inflated with nitrogen gas exhaust duct, pulse vibrator, explosion venting device with electric precipitator; The fly-ash separator body is a body structure, be provided with dust collecting electrode and discharge electrode in body interior, be provided with the water spouting nozzle of cleaning dust collecting electrode and discharge electrode at the electric precipitator top, the fly-ash separator lower end is provided with ash bucket, on the fly-ash separator body, be provided with nitrogen purging device, the nitrogen discharge device is located at dust remover roof, is provided with a plurality of explosion venting valves on electric precipitator.
2, blast furnace gas purification electric precipitator according to claim 1, it is characterized in that: the ingress at the electric precipitator upper body is provided with airflow-distribution board.
3, blast furnace gas purification electric precipitator according to claim 1 is characterized in that: be provided with the electromagnetic hammer pulse vibrator in the fly-ash separator bodies top.
4, blast furnace gas purification electric precipitator according to claim 1 is characterized in that: dust collecting electrode adopts slab construction.
5, blast furnace gas purification electric precipitator according to claim 1 is characterized in that: dust collecting electrode adopts bimodal plate slab structure.
6, blast furnace gas purification electric precipitator according to claim 1 is characterized in that: discharge electrode adopts the linear formula of pipe thorn.
7, blast furnace gas purification electric precipitator according to claim 1 is characterized in that: discharge electrode adopts the linear formula of strand.
8, blast furnace gas purification electric precipitator according to claim 1, it is characterized in that: dust removal installation is provided with attemperator, is provided with the insulator insulation can at the electric precipitator top, and explosion-proof INCREASEDSAFETY electric heater is installed on the insulator insulation can.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200320105831 CN2672078Y (en) | 2003-12-04 | 2003-12-04 | Electric duster for blast furnace gas purifying |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200320105831 CN2672078Y (en) | 2003-12-04 | 2003-12-04 | Electric duster for blast furnace gas purifying |
Publications (1)
Publication Number | Publication Date |
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CN2672078Y true CN2672078Y (en) | 2005-01-19 |
Family
ID=34474390
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 200320105831 Expired - Fee Related CN2672078Y (en) | 2003-12-04 | 2003-12-04 | Electric duster for blast furnace gas purifying |
Country Status (1)
Country | Link |
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CN (1) | CN2672078Y (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102274793A (en) * | 2011-05-11 | 2011-12-14 | 中冶南方工程技术有限公司 | Electrostatic precipitator with additional anion generators |
CN101429579B (en) * | 2007-11-06 | 2012-02-08 | 新日铁工程技术株式会社 | Purification method and apparatus for blast furnace gas |
CN106568197A (en) * | 2016-10-28 | 2017-04-19 | 江阴市国豪电热电器制造有限公司 | Tubular explosion-proof electric heater capable of automatically cleaning dirt |
CN108283870A (en) * | 2018-01-05 | 2018-07-17 | 安徽理工大学 | A kind of plasma exhaust gas Integrated Processing Unit |
-
2003
- 2003-12-04 CN CN 200320105831 patent/CN2672078Y/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101429579B (en) * | 2007-11-06 | 2012-02-08 | 新日铁工程技术株式会社 | Purification method and apparatus for blast furnace gas |
CN102274793A (en) * | 2011-05-11 | 2011-12-14 | 中冶南方工程技术有限公司 | Electrostatic precipitator with additional anion generators |
CN106568197A (en) * | 2016-10-28 | 2017-04-19 | 江阴市国豪电热电器制造有限公司 | Tubular explosion-proof electric heater capable of automatically cleaning dirt |
CN108283870A (en) * | 2018-01-05 | 2018-07-17 | 安徽理工大学 | A kind of plasma exhaust gas Integrated Processing Unit |
CN108283870B (en) * | 2018-01-05 | 2020-10-16 | 安徽理工大学 | Plasma waste gas comprehensive treatment device |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |