CN209565102U - A kind of gas purification wet electrical dust precipitator - Google Patents

A kind of gas purification wet electrical dust precipitator Download PDF

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Publication number
CN209565102U
CN209565102U CN201822190542.6U CN201822190542U CN209565102U CN 209565102 U CN209565102 U CN 209565102U CN 201822190542 U CN201822190542 U CN 201822190542U CN 209565102 U CN209565102 U CN 209565102U
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China
Prior art keywords
dust
corona discharge
shell
discharge electrode
gas purification
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Expired - Fee Related
Application number
CN201822190542.6U
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Chinese (zh)
Inventor
肖立春
王新
张雪艳
高珊
张萌
王雨川
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Yanshan University
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Yanshan University
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Priority to CN201822190542.6U priority Critical patent/CN209565102U/en
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Publication of CN209565102U publication Critical patent/CN209565102U/en
Expired - Fee Related legal-status Critical Current
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Abstract

The utility model relates to a kind of gas purification wet electrical dust precipitators, belong to gas purification field, including air inlet (1), shell (4), corona discharge electrode (5), dust collector pole (6), nozzle (7), air outlet (11), blowdown valve (12).Airflow-distribution board (2) of the coal gas from air inlet (1) through being located in it enters cylinder type shell (4), is formed by electric field channel corona discharge, dust charged and the dust catching process completed in corona discharge electrode (5) and dust collector pole (6).It is discharged after dehydration device (10) removes its water mist by air outlet (11).After the washing water that nozzle (7) sprays completes deashing to dust collecting pole plate, it is arranged at blowdown valve (12) discharge of shell (4) bottom.The device corona discharge electrode has auxiliary electrode, improves the arresting efficiency to submicron particles, and groove is equipped on pole plate, reduces the thermal deformation that pole plate is generated by gas temperature in the electric field.

Description

A kind of gas purification wet electrical dust precipitator
Technical field
The utility model relates to a kind of wet electrical dust precipitators of high pressure gas purification.The wet electrical dust precipitator installation In producer gas purification system, coal gas enters wet electrical dust precipitator after pre- dedusting and enters cabinet coal gas powder after its refined dedusting Dust content is reduced to 1mg/m3Below.
Background technique
Producer gas is the indispensable raw material of coal chemical industry, since the dust in coal gas mentions gas chamber and chemical industry It refines equipment and generates harm, it is therefore necessary to be removed before entering cabinet, its dust depth is reduced to 1mg/m3Below.Currently, being used for coal The equipment of gas purification mainly has cyclone dust collectors, wet scrubbing deduster and bag filter, and cyclone dust collectors are generally as pre- Deduster uses, and wet scrubbing deduster mainly uses the dust-extraction units such as stuffing washing tower, removes the dust in coal gas, can generate A large amount of washes, operation energy consumption are also higher.Bag filter is also easy to produce " leak-off pocket " phenomenon, and outlet dust concentration often surpasses Mark.Wet electrical dust precipitator is used in purification system, the dust concentration in coal gas can be effectively reduced, while greatly reducing system In water consume and power consumption, and meet requirement of the system to cleaner safety.
Summary of the invention
The purpose of this utility model is to provide a kind of wet electrical dust precipitators of high pressure gas purification, can using the device With the dust in effective coal gas, the dust concentration in coal gas is made to be less than 1mg/m3, stringent to gas quality to meet coal gas user Requirement.The device has the advantages that high-efficient, good reliability, water consume are low, running resistance is small.The device is in wet electrical dust precipitator Auxiliary electrode is increased in corona discharge electrode, improves the driving speed of dust in the electric field, and improve efficiency of dust collection.In anode plate Centre is provided with two grooves vertically downward, improves the intensity of pole plate.Shell of dust remover uses cylinder type, Ke Yishi The requirement for answering high pressure gas to purify.
The utility model is realized by following scheme:
Coal gas enters in deduster from deduster entrance, via the airflow channel that corona discharge electrode and dust collector pole form, in height Press corona discharge and the dust charged process completed under the action of DC power supply, it is charged after dust under the action of electric field force to receipts Dirt polar motion is simultaneously captured.There is nozzle in the top layout of electric field, the interior water mist sprayed can effectively wash pole plate and catch The dust of collection.It is small in the variation of dust catching area electric-force gradient due to increasing auxiliary electrode in wet electrical dust precipitator corona discharge electrode, Electric field strength is more uniform, therefore Charged can obtain constant driving force, to pole plate under the effect of consistent electric field power The more conventional electric precipitator of process " turbulence " phenomenon of movement is weak, and submicron particle lesser for partial size, turbulence intensity is small, institute To improve its arresting efficiency.Its dust collecting pole plate is equipped with windproof ditch using c-type plate, c-type plate both sides are widened, it is possible to reduce after trapping The secondary of dust carries under one's arms phenomenon, and in order to improve the bending strength of pole plate, groove is located among pole plate, reduces pole plate in electric field In by gas temperature generate thermal deformation.It is designed with coal gas explosion venting device on the air inlet and air outlet of deduster, ensure that and set Standby safety.Shell of dust remover uses cylinder type, and bearing capacity is improved to 35kPa or more.Air outlet is equipped with hundred Leaf window dehydration device can remove the water mist in coal gas and improve the calorific value of coal gas.
The utility model is compared with existing coal gas electrostatic precipitation technology, has the advantage that its corona discharge electrode with auxiliary electricity Pole improves the arresting efficiency to submicron particles, and groove is equipped on dust collecting pole plate, reduces pole plate in the electric field by coal gas The thermal deformation that temperature generates.
Detailed description of the invention
The utility model is described in further detail with reference to the accompanying drawings and examples.
Fig. 1 is gas purification wet electrical dust precipitator schematic diagram.
Fig. 2 is the corona discharge electrode and dust collector pole schematic diagram of wet electrical dust precipitator.
Specific embodiment
In Fig. 1, the wet electrical dust precipitator of high pressure gas purification include air inlet (1), shell (4), corona discharge electrode (5), Dust collector pole (6), nozzle (7), air outlet (11), blowdown valve (12).Airflow-distribution board (2) is located in conical air inlet (1), Shell (4) is cylinder type, and air inlet (1), shell (4) and air outlet (11) form airflow channel, and coal gas is from air inlet (1) through setting Airflow-distribution board (2) in it enters cylinder type shell (4), is discharged after purified by air outlet (11).Air inlet (1) and go out The first explosion venting device (3) and the second explosion venting device (9) are respectively equipped on air port (11), it, can be in coal gas using self-recovering type form It because explosion causes to realize safe venting of dust explosion when pressure overrate, and is automatically closed after the completion of venting of dust explosion, reduces the outer of coal gas It lets out.Corona discharge electrode (5) and dust collector pole (6) are arranged in shell (4), in being staggered, form high pressure necessary to electric precipitator works Electrostatic field.Nozzle (7) is arranged in the top of corona discharge electrode (5) and dust collector pole (6).High pressure gas is in corona discharge electrode (5) and dust collector pole (6) Corona discharge, dust charged and the dust catching process completed are formed by electric field channel.The gas washing sprayed by nozzle (7) Water completes deashing to dust collecting pole plate.The dehydration device (10) that purified coal gas is located in air outlet (11) removes its water mist After be discharged.Dust-laden washing water is discharged by the blowdown valve (12) for being arranged in shell (4) bottom.Conical air inlet (1) and air outlet (11) and the airflow channel of cylinder type shell (4) formation can make coal gas be in the form of a column flowing, and streamline distribution is more uniform, shell (4) pressure resistance reaches 35kPa or more.Regulating valve (8) can control the uninterrupted of Coal-gas Washing Water Using.Dehydration device (10) uses hundred Water mist content in coal gas is reduced to 10mg/m by leaf window shape formula3Below.
In Fig. 2, corona discharge electrode is made of corona wire (51) and auxiliary electrode (52), and corona wire spray point spacing is A, big Small to have an impact to electric current per unit length, size A is preferably 50~80mm;The spacing of corona wire (51) and auxiliary electrode (52) is B, Selection can get uniform field strength.Size B is preferably 250~280mm, size between the first auxiliary electrode pipe of auxiliary electrode (52) Size E is preferably 30~50mm between D and the second auxiliary electrode pipe.Dust collector pole is made of pole plate (61) repeated arrangement, pole plate (61) Use width for the c-type plate of 800mm, there is c-type radix saposhnikoviae ditch on both sides, have a longitudinal groove in the middle part of pole plate.

Claims (2)

1. a kind of gas purification wet electrical dust precipitator, including air inlet (1), shell (4), corona discharge electrode (5), dust collector pole (6), spray Mouth (7), air outlet (11), blowdown valve (12), which is characterized in that air inlet (1), air outlet (11) are cone, with cylinder type Shell (4) connects, and is respectively equipped with the first explosion venting device (3) and the second explosion venting device (9) on air inlet (1) and air outlet (11), Corona discharge electrode (5) and dust collector pole (6) are arranged in shell (4), and in being staggered, nozzle (7) is arranged in corona discharge electrode (5) and dust collector pole (6) top, dehydration device (10) are mounted in air outlet (11), and blowdown valve (12) is arranged in shell (4) bottom.
2. gas purification wet electrical dust precipitator according to claim 1, which is characterized in that corona discharge electrode (5) is by corona wire (51) it is formed with auxiliary electrode (52), corona wire spray point spacing is that A is 50~80mm, corona wire (51) and auxiliary electrode (52) Spacing B be 250~280mm, size between dimension D and the second auxiliary electrode pipe between the first auxiliary electrode pipe of auxiliary electrode (52) E is 30~50mm.
CN201822190542.6U 2018-12-25 2018-12-25 A kind of gas purification wet electrical dust precipitator Expired - Fee Related CN209565102U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201822190542.6U CN209565102U (en) 2018-12-25 2018-12-25 A kind of gas purification wet electrical dust precipitator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201822190542.6U CN209565102U (en) 2018-12-25 2018-12-25 A kind of gas purification wet electrical dust precipitator

Publications (1)

Publication Number Publication Date
CN209565102U true CN209565102U (en) 2019-11-01

Family

ID=68331067

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201822190542.6U Expired - Fee Related CN209565102U (en) 2018-12-25 2018-12-25 A kind of gas purification wet electrical dust precipitator

Country Status (1)

Country Link
CN (1) CN209565102U (en)

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

Granted publication date: 20191101

Termination date: 20201225

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