CN112237991A - Wet electrostatic dust collector - Google Patents
Wet electrostatic dust collector Download PDFInfo
- Publication number
- CN112237991A CN112237991A CN202011229503.8A CN202011229503A CN112237991A CN 112237991 A CN112237991 A CN 112237991A CN 202011229503 A CN202011229503 A CN 202011229503A CN 112237991 A CN112237991 A CN 112237991A
- Authority
- CN
- China
- Prior art keywords
- anode
- driving shaft
- adsorption
- anode plate
- movable
- 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.)
- Granted
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/16—Plant or installations having external electricity supply wet type
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/45—Collecting-electrodes
- B03C3/53—Liquid, or liquid-film, electrodes
Abstract
The invention discloses a wet electrostatic dust removal device, which belongs to the technical field of industrial tail gas dust removal and comprises a shell, a movable anode device and a cathode electrode body; a movable anode device and a cathode electrode body are arranged in the shell; the movable anode device comprises a driving shaft, a driven shaft and an anode coil; the anode coil is wound on the driven shaft; the movable end of the anode coil is wound on the driving shaft; the driving shaft is used for autorotation, so that the anode is wound between the driving shaft and the driven shaft to form a movable anode plate; the adsorption surface of the anode plate is opposite to the cathode electrode body. The wet electrostatic dust removal device can continuously and automatically update the anode plate, prevent high-viscosity particles from being deposited on the surface of the anode plate, continuously maintain high-efficiency adsorption capacity, continuously supplement adsorption liquid through capillary phenomenon, and improve the adsorption removal capacity of the high-viscosity particles.
Description
Technical Field
The invention belongs to the technical field of industrial tail gas dust removal, and particularly relates to a wet electrostatic dust removal device.
Background
The existing electrostatic dust removal device adopts a cathode wire and an anode plate arranged in a dust removal shell, and high voltage is applied between the anode plate and the cathode wire to form a strong electric field. The process air flow enters an electric field along with the process air flow, high-adhesiveness particles are adsorbed on the anode plate under the action of coulomb force of a high-voltage electrostatic field, and the effect of dedusting and purifying industrial tail gas is achieved. But current anode plate is immovable, along with the increase of number of times of use, adsorbs a large amount of stickness particulate matters on the anode plate, and thickness constantly accumulates, leads to the adsorption efficiency decline of anode plate. The method for recovering the adsorption capacity of the anode plate is to artificially replace the anode plate, and the anode plate needs to be artificially checked and replaced in real time, thereby wasting time and labor.
Disclosure of Invention
The invention aims to provide a wet electrostatic dust removal device aiming at the defects, and aims to solve the problems that the adsorption capacity of an anode plate is reduced and the automatic updating of the adsorption capacity of the anode plate cannot be realized due to the fact that a large amount of sticky particles are adsorbed on the anode plate and the thickness is continuously accumulated along with the increase of the using times of the conventional electrostatic dust removal device. In order to achieve the purpose, the invention provides the following technical scheme:
a wet electrostatic dust collector comprises a shell 1, a movable anode device 2 and a cathode electrode body 3; a movable anode device 2 and a cathode electrode body 3 are arranged in the shell 1; the movable anode device 2 comprises a driving shaft 4, a driven shaft 5 and an anode roll 6; the anode coil 6 is wound on the driven shaft 5; the movable end of the anode roll 6 is wound on the driving shaft 4; the driving shaft 4 is used for rotating, so that the anode roll 6 is provided with a movable anode plate 7 between the driving shaft 4 and the driven shaft 5; the adsorption surface of the anode plate 7 is opposite to the cathode electrode body 3. According to the structure, industrial tail gas enters the shell 1, a high-voltage electrostatic field is formed between the anode plate 7 and the cathode electrode body 3, and sticky particles in the industrial tail gas are adsorbed on the adsorption surface of the anode plate 7 under the action of the electric field. Adsorb a large amount of stickness particulate matters on the anode plate, thickness constantly accumulates, leads to the adsorption efficiency of anode plate to begin to descend, and driving shaft 4 begins the rotation, rolls up anode plate 7 that adsorption efficiency descends on driving shaft 4, drives the anode simultaneously and rolls up 6 and pull out new anode plate, and new anode plate has high adsorption efficiency, can adsorb a large amount of stickness particulate matters, makes anode plate 7 constantly keep higher adsorption efficiency, does not need the people to go frequently to change anode plate 7, labour saving and time saving.
Further, the device also comprises a driven shaft liquid inlet pipe 8; a capillary micropore is formed in the driven shaft 5; the driven shaft liquid inlet pipe 8 is used for inputting adsorption liquid to the capillary micropores; the capillary micropores are used for transporting the adsorption liquid to the anode roll 6. According to the structure, the driven shaft 5 is internally provided with the capillary micropores, the driven shaft liquid inlet pipe 8 is used for inputting adsorption liquid to the capillary micropores, the adsorption liquid continuously infiltrates the anode roll 6 through the capillary phenomenon of the capillary micropores, so that the anode roll 6 is kept wet all the time, the pulled anode plate 7 is kept wet, and the adsorption capacity of the anode plate 7 is improved by the adsorption liquid.
Furthermore, the device also comprises a driving shaft liquid inlet pipe 9; the driving shaft 4 is internally provided with capillary micropores; the driving shaft liquid inlet pipe 9 is used for inputting adsorption liquid to the capillary micropores; the capillary micropores are used for transporting the adsorption liquid to the anode roll 6. According to the structure, the driving shaft 4 is internally provided with the capillary micropores, the driving shaft liquid inlet pipe 9 is used for inputting adsorption liquid to the capillary micropores, the adsorption liquid continuously infiltrates the movable end of the anode roll 6 through the capillary phenomenon of the capillary micropores, the pulled anode plate 7 is kept moist, and the adsorption liquid improves the adsorption capacity of the anode plate 7.
Furthermore, the driven shaft 5 and the driving shaft 4 are in a loose porous sponge honeycomb shape to form a capillary microporous pipe network. According to the structure, the driven shaft 5 and the driving shaft 4 are in a loose porous sponge honeycomb shape, so that a capillary microporous pipe network is formed, and the adsorption liquid can infiltrate the anode roll 6 in a large area. The pore size of the capillary pores is 50-100 microns, and the material includes but is not limited to stainless steel or polypropylene plastic microporous honeycomb network structure.
Further, the anode roll 6 is anode fiber soft paper.
Further, a liquid supply pipe 10 and a pump are also included; the liquid supply pipe 10 is communicated with the driven shaft liquid inlet pipe 8 and the driving shaft liquid inlet pipe 9; a pump is arranged on the liquid supply pipe 10. According to the structure, after the pump is started, the adsorption liquid is sucked into the liquid supply pipe 10, and then the adsorption liquid is supplied to the movable shaft liquid inlet pipe 8 and the driving shaft liquid inlet pipe 9 through the liquid supply pipe 10, so that the capillary micro-pipes of the driving shaft 4 and the driven shaft 5 are filled with the adsorption liquid.
Further, the device also comprises a controller, a motor, a particle thickness detector and a humidity detector; the particle thickness detector is used for detecting the thickness of particles adsorbed on the anode plate 7; the humidity detector is used for detecting the content of the adsorption liquid on the anode plate 7; the motor is used for driving the driving shaft 4 to rotate; the particle thickness detector, the humidity detector, the pump, the motor and the controller are electrically connected. According to the structure, when the humidity detector is used for detecting that the content of the adsorption liquid on the anode plate 7 is insufficient, the content information of the adsorption liquid is transmitted to the controller, the controller controls the pump to be started, the adsorption liquid is sucked into the liquid supply pipe 10, and the anode plate 7 is finally soaked. When the thickness of the particles on the anode plate 7 detected by the particle thickness detector reaches the accumulated upper limit, the upper limit signal is transmitted to the controller, and the controller controls the motor to drive the driving shaft 4 to rotate, so that the new anode plate 7 is pulled out. The automation degree is high, the anode plate 7 does not need to be replaced frequently by people, and time and labor are saved.
Further, the cathode electrode body 3 extends parallel to the adsorption surface of the anode plate 7; a plurality of discharge needles 11 are arranged on the cathode electrode body 3; the number of the movable anode devices 2 is two; the cathode electrode body 3 is located between two movable anode means 2. According to the structure, the cathode electrode body 3 is provided with the plurality of discharge needles 11, so that the distribution density of the electric field is improved. The number of the movable anode devices 2 is two, and the adsorption area of the anode plate 7 is increased.
Further, the preparation method of the adsorption solution adopts a nonionic surfactant TERIC 168: PEG: sodium carboxymethylcellulose: the water mass ratio is 2: 10: 5: 68, stirring and stirring for 60min at 3000r/min by using a stirrer 2000-. With the structure, the adsorption liquid can enhance the adsorption capacity of the anode plate 7.
The invention has the beneficial effects that:
the invention discloses a wet electrostatic dust removal device, which belongs to the technical field of industrial tail gas dust removal and comprises a shell, a movable anode device and a cathode electrode body; a movable anode device and a cathode electrode body are arranged in the shell; the movable anode device comprises a driving shaft, a driven shaft and an anode coil; the anode coil is wound on the driven shaft; the movable end of the anode coil is wound on the driving shaft; the driving shaft is used for autorotation, so that the anode is wound between the driving shaft and the driven shaft to form a movable anode plate; the adsorption surface of the anode plate is opposite to the cathode electrode body. The wet electrostatic dust removal device can continuously and automatically update the anode plate, avoids high-viscosity particles from depositing on the surface of the anode plate, continuously maintains high-efficiency adsorption capacity, continuously supplements adsorption liquid through capillary phenomenon, and improves the adsorption removal capacity of the high-viscosity particles.
Drawings
FIG. 1 is a schematic structural view of the present invention;
in the drawings: 1-outer shell, 2-movable anode device, 3-cathode electrode body, 4-driving shaft, 5-driven shaft, 6-anode roll, 7-anode plate, 8-driven shaft liquid inlet pipe, 9-driving shaft liquid inlet pipe and 10-liquid supply pipe.
Detailed Description
The present invention will be described in further detail below with reference to the drawings and the embodiments, but the present invention is not limited to the following examples.
The first embodiment is as follows:
see figure 1. A wet electrostatic dust collector comprises a shell 1, a movable anode device 2 and a cathode electrode body 3; a movable anode device 2 and a cathode electrode body 3 are arranged in the shell 1; the movable anode device 2 comprises a driving shaft 4, a driven shaft 5 and an anode roll 6; the anode coil 6 is wound on the driven shaft 5; the movable end of the anode roll 6 is wound on the driving shaft 4; the driving shaft 4 is used for rotating, so that the anode roll 6 is provided with a movable anode plate 7 between the driving shaft 4 and the driven shaft 5; the adsorption surface of the anode plate 7 is opposite to the cathode electrode body 3. According to the structure, industrial tail gas enters the shell 1, a high-voltage electrostatic field is formed between the anode plate 7 and the cathode electrode body 3, and sticky particles in the industrial tail gas are adsorbed on the adsorption surface of the anode plate 7 under the action of the electric field. Adsorb a large amount of stickness particulate matters on the anode plate, thickness constantly accumulates, leads to the adsorption efficiency of anode plate to begin to descend, and driving shaft 4 begins the rotation, rolls up anode plate 7 that adsorption efficiency descends on driving shaft 4, drives the anode simultaneously and rolls up 6 and pull out new anode plate, and new anode plate has high adsorption efficiency, can adsorb a large amount of stickness particulate matters, makes anode plate 7 constantly keep higher adsorption efficiency, does not need the people to go frequently to change anode plate 7, labour saving and time saving.
Example two:
see figure 1. A wet electrostatic dust collector comprises a shell 1, a movable anode device 2 and a cathode electrode body 3; a movable anode device 2 and a cathode electrode body 3 are arranged in the shell 1; the movable anode device 2 comprises a driving shaft 4, a driven shaft 5 and an anode roll 6; the anode coil 6 is wound on the driven shaft 5; the movable end of the anode roll 6 is wound on the driving shaft 4; the driving shaft 4 is used for rotating, so that the anode roll 6 is provided with a movable anode plate 7 between the driving shaft 4 and the driven shaft 5; the adsorption surface of the anode plate 7 is opposite to the cathode electrode body 3. According to the structure, industrial tail gas enters the shell 1, a high-voltage electrostatic field is formed between the anode plate 7 and the cathode electrode body 3, and sticky particles in the industrial tail gas are adsorbed on the adsorption surface of the anode plate 7 under the action of the electric field. Adsorb a large amount of stickness particulate matters on the anode plate, thickness constantly accumulates, leads to the adsorption efficiency of anode plate to begin to descend, and driving shaft 4 begins the rotation, rolls up anode plate 7 that adsorption efficiency descends on driving shaft 4, drives the anode simultaneously and rolls up 6 and pull out new anode plate, and new anode plate has high adsorption efficiency, can adsorb a large amount of stickness particulate matters, makes anode plate 7 constantly keep higher adsorption efficiency, does not need the people to go frequently to change anode plate 7, labour saving and time saving.
The device also comprises a driven shaft liquid inlet pipe 8; a capillary micropore is formed in the driven shaft 5; the driven shaft liquid inlet pipe 8 is used for inputting adsorption liquid to the capillary micropores; the capillary micropores are used for transporting the adsorption liquid to the anode roll 6. According to the structure, the driven shaft 5 is internally provided with the capillary micropores, the driven shaft liquid inlet pipe 8 is used for inputting adsorption liquid to the capillary micropores, the adsorption liquid continuously infiltrates the anode roll 6 through the capillary phenomenon of the capillary micropores, so that the anode roll 6 is kept wet all the time, the pulled anode plate 7 is kept wet, and the adsorption capacity of the anode plate 7 is improved by the adsorption liquid.
The device also comprises a driving shaft liquid inlet pipe 9; the driving shaft 4 is internally provided with capillary micropores; the driving shaft liquid inlet pipe 9 is used for inputting adsorption liquid to the capillary micropores; the capillary micropores are used for transporting the adsorption liquid to the anode roll 6. According to the structure, the driving shaft 4 is internally provided with the capillary micropores, the driving shaft liquid inlet pipe 9 is used for inputting adsorption liquid to the capillary micropores, the adsorption liquid continuously infiltrates the movable end of the anode roll 6 through the capillary phenomenon of the capillary micropores, the pulled anode plate 7 is kept moist, and the adsorption liquid improves the adsorption capacity of the anode plate 7.
Example three:
see figure 1. A wet electrostatic dust collector comprises a shell 1, a movable anode device 2 and a cathode electrode body 3; a movable anode device 2 and a cathode electrode body 3 are arranged in the shell 1; the movable anode device 2 comprises a driving shaft 4, a driven shaft 5 and an anode roll 6; the anode coil 6 is wound on the driven shaft 5; the movable end of the anode roll 6 is wound on the driving shaft 4; the driving shaft 4 is used for rotating, so that the anode roll 6 is provided with a movable anode plate 7 between the driving shaft 4 and the driven shaft 5; the adsorption surface of the anode plate 7 is opposite to the cathode electrode body 3. According to the structure, industrial tail gas enters the shell 1, a high-voltage electrostatic field is formed between the anode plate 7 and the cathode electrode body 3, and sticky particles in the industrial tail gas are adsorbed on the adsorption surface of the anode plate 7 under the action of the electric field. Adsorb a large amount of stickness particulate matters on the anode plate, thickness constantly accumulates, leads to the adsorption efficiency of anode plate to begin to descend, and driving shaft 4 begins the rotation, rolls up anode plate 7 that adsorption efficiency descends on driving shaft 4, drives the anode simultaneously and rolls up 6 and pull out new anode plate, and new anode plate has high adsorption efficiency, can adsorb a large amount of stickness particulate matters, makes anode plate 7 constantly keep higher adsorption efficiency, does not need the people to go frequently to change anode plate 7, labour saving and time saving.
The device also comprises a driven shaft liquid inlet pipe 8; a capillary micropore is formed in the driven shaft 5; the driven shaft liquid inlet pipe 8 is used for inputting adsorption liquid to the capillary micropores; the capillary micropores are used for transporting the adsorption liquid to the anode roll 6. According to the structure, the driven shaft 5 is internally provided with the capillary micropores, the driven shaft liquid inlet pipe 8 is used for inputting adsorption liquid to the capillary micropores, the adsorption liquid continuously infiltrates the anode roll 6 through the capillary phenomenon of the capillary micropores, so that the anode roll 6 is kept wet all the time, the pulled anode plate 7 is kept wet, and the adsorption capacity of the anode plate 7 is improved by the adsorption liquid.
The device also comprises a driving shaft liquid inlet pipe 9; the driving shaft 4 is internally provided with capillary micropores; the driving shaft liquid inlet pipe 9 is used for inputting adsorption liquid to the capillary micropores; the capillary micropores are used for transporting the adsorption liquid to the anode roll 6. According to the structure, the driving shaft 4 is internally provided with the capillary micropores, the driving shaft liquid inlet pipe 9 is used for inputting adsorption liquid to the capillary micropores, the adsorption liquid continuously infiltrates the movable end of the anode roll 6 through the capillary phenomenon of the capillary micropores, the pulled anode plate 7 is kept moist, and the adsorption liquid improves the adsorption capacity of the anode plate 7.
The driven shaft 5 and the driving shaft 4 are loose porous sponge honeycombs to form a capillary microporous pipe network. According to the structure, the driven shaft 5 and the driving shaft 4 are in a loose porous sponge honeycomb shape, so that a capillary microporous pipe network is formed, and the adsorption liquid can infiltrate the anode roll 6 in a large area. The pore size of the capillary pores is 50-100 microns, and the material includes but is not limited to stainless steel or polypropylene plastic microporous honeycomb network structure.
The anode roll 6 is anode fiber soft paper.
Also comprises a liquid supply pipe 10 and a pump; the liquid supply pipe 10 is communicated with the driven shaft liquid inlet pipe 8 and the driving shaft liquid inlet pipe 9; a pump is arranged on the liquid supply pipe 10. According to the structure, after the pump is started, the adsorption liquid is sucked into the liquid supply pipe 10, and then the adsorption liquid is supplied to the movable shaft liquid inlet pipe 8 and the driving shaft liquid inlet pipe 9 through the liquid supply pipe 10, so that the capillary micro-pipes of the driving shaft 4 and the driven shaft 5 are filled with the adsorption liquid.
The device also comprises a controller, a motor, a particle thickness detector and a humidity detector; the particle thickness detector is used for detecting the thickness of particles adsorbed on the anode plate 7; the humidity detector is used for detecting the content of the adsorption liquid on the anode plate 7; the motor is used for driving the driving shaft 4 to rotate; the particle thickness detector, the humidity detector, the pump, the motor and the controller are electrically connected. According to the structure, when the humidity detector is used for detecting that the content of the adsorption liquid on the anode plate 7 is insufficient, the content information of the adsorption liquid is transmitted to the controller, the controller controls the pump to be started, the adsorption liquid is sucked into the liquid supply pipe 10, and the anode plate 7 is finally soaked. When the thickness of the particles on the anode plate 7 detected by the particle thickness detector reaches the accumulated upper limit, the upper limit signal is transmitted to the controller, and the controller controls the motor to drive the driving shaft 4 to rotate, so that the new anode plate 7 is pulled out. The automation degree is high, the anode plate 7 does not need to be replaced frequently by people, and time and labor are saved.
The cathode electrode body 3 extends parallel to the adsorption surface of the anode plate 7; a plurality of discharge needles 11 are arranged on the cathode electrode body 3; the number of the movable anode devices 2 is two; the cathode electrode body 3 is located between two movable anode means 2. According to the structure, the cathode electrode body 3 is provided with the plurality of discharge needles 11, so that the distribution density of the electric field is improved. The number of the movable anode devices 2 is two, and the adsorption area of the anode plate 7 is increased.
The preparation method of the adsorption solution adopts a nonionic surfactant TERIC 168: PEG: sodium carboxymethylcellulose: the water mass ratio is 2: 10: 5: 68, stirring and stirring for 60min at 3000r/min by using a stirrer 2000-. With the structure, the adsorption liquid can enhance the adsorption capacity of the anode plate 7.
The above description is only a preferred embodiment of the present invention, and not intended to limit the scope of the present invention, and all modifications of equivalent structures and equivalent processes, which are made by using the contents of the present specification and the accompanying drawings, or directly or indirectly applied to other related technical fields, are included in the scope of the present invention.
Claims (9)
1. The utility model provides a wet electrostatic precipitator device which characterized in that: comprises a shell (1), a movable anode device (2) and a cathode electrode body (3); a movable anode device (2) and a cathode electrode body (3) are arranged in the shell (1); the movable anode device (2) comprises a driving shaft (4), a driven shaft (5) and an anode coil (6); the anode coil (6) is wound on the driven shaft (5); the movable end of the anode roll (6) is wound on the driving shaft (4); the driving shaft (4) is used for rotating, so that the anode roll (6) is provided with a movable anode plate (7) between the driving shaft (4) and the driven shaft (5); the adsorption surface of the anode plate (7) is opposite to the cathode electrode body (3).
2. A wet electrostatic precipitator as claimed in claim 1, wherein: the device also comprises a driven shaft liquid inlet pipe (8); capillary micropores are formed in the driven shaft (5); the driven shaft liquid inlet pipe (8) is used for inputting adsorption liquid into the capillary micropores; the capillary micropores are used for conveying the adsorption liquid to the anode roll (6).
3. A wet electrostatic precipitator as claimed in claim 2, wherein: the device also comprises a driving shaft liquid inlet pipe (9); the driving shaft (4) is internally provided with capillary micropores; the driving shaft liquid inlet pipe (9) is used for inputting adsorption liquid into the capillary micropores; the capillary micropores are used for conveying the adsorption liquid to the anode roll (6).
4. A wet electrostatic precipitator as claimed in claim 3, wherein: the driven shaft (5) and the driving shaft (4) are in a loose porous sponge honeycomb shape to form a capillary microporous pipe network.
5. A wet electrostatic precipitator as claimed in claim 3, wherein: the anode roll (6) is anode fiber soft paper.
6. A wet electrostatic precipitator as claimed in claim 3, wherein: also comprises a liquid supply pipe (10) and a pump; the liquid supply pipe (10) is communicated with the driven shaft liquid inlet pipe (8) and the driving shaft liquid inlet pipe (9); the liquid supply pipe (10) is provided with a pump.
7. The wet electrostatic precipitator of claim 6, wherein: the device also comprises a controller, a motor, a particle thickness detector and a humidity detector; the particle thickness detector is used for detecting the thickness of particles adsorbed on the anode plate (7); the humidity detector is used for detecting the content of the adsorption liquid on the anode plate (7); the motor is used for driving the driving shaft (4) to rotate; the particle thickness detector, the humidity detector, the pump, the motor and the controller are electrically connected.
8. A wet electrostatic precipitator as claimed in claim 1, wherein: the cathode electrode body (3) extends parallel to the adsorption surface of the anode plate (7); a plurality of discharge needles (11) are arranged on the cathode electrode body (3); the number of the movable anode devices (2) is two; the cathode electrode body (3) is positioned between the two movable anode devices (2).
9. A wet electrostatic precipitator as claimed in claim 2, wherein: the preparation method of the adsorption solution adopts a nonionic surfactant TERIC 168: PEG: sodium carboxymethylcellulose: the water mass ratio is 2: 10: 5: 68, stirring and stirring for 60min at 3000r/min by using a stirrer 2000-.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011229503.8A CN112237991B (en) | 2020-11-06 | 2020-11-06 | Wet electrostatic dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011229503.8A CN112237991B (en) | 2020-11-06 | 2020-11-06 | Wet electrostatic dust collector |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN112237991A true CN112237991A (en) | 2021-01-19 |
| CN112237991B CN112237991B (en) | 2023-02-24 |
Family
ID=74170048
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011229503.8A Active CN112237991B (en) | 2020-11-06 | 2020-11-06 | Wet electrostatic dust collector |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112237991B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117589945A (en) * | 2024-01-11 | 2024-02-23 | 武汉瑞气节能环保科技有限公司 | Wisdom air compressor station is with air detection device |
Citations (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06233945A (en) * | 1993-02-10 | 1994-08-23 | Daikin Ind Ltd | Winding type dust removing filter |
| JPH1119534A (en) * | 1997-07-04 | 1999-01-26 | Pioneer Electron Corp | Electrostatic air cleaner and dust collecting paper therefor |
| CN2566212Y (en) * | 2002-06-28 | 2003-08-13 | 煜丰科技股份有限公司 | Water evaporation cover capable of raising heat exchanging efficiency |
| CN102245751A (en) * | 2008-12-09 | 2011-11-16 | 花王株式会社 | Method for manufacturing detergent particles |
| CN102784719A (en) * | 2012-08-20 | 2012-11-21 | 山东大学 | Water internally-distributed type flexible dust collecting electrode device |
| JP2016064409A (en) * | 2014-09-17 | 2016-04-28 | パナソニックＩｐマネジメント株式会社 | Air cleaner |
| JP2016087538A (en) * | 2014-11-04 | 2016-05-23 | 帝人株式会社 | Dust remover |
| CN105797865A (en) * | 2016-05-10 | 2016-07-27 | 艾尼科环保技术(安徽)有限公司 | Flexible polar plate of wet electrostatic dust remover |
| CN106540809A (en) * | 2015-09-16 | 2017-03-29 | 武汉科技大学 | A kind of water logging self-cleaning cloth roller shutter wet electrostatic dust arrester installation |
| CN106765583A (en) * | 2017-01-12 | 2017-05-31 | 张宗炜 | The method of air cleaning unit and purify air |
| KR20170090217A (en) * | 2016-01-28 | 2017-08-07 | 케이씨코트렐 주식회사 | A electric precipitator with injection device forming a water film |
| CN207254551U (en) * | 2017-09-18 | 2018-04-20 | 保定坤泰环保节能科技有限公司 | A kind of novel air pollutes cleaning equipment |
| CN207462840U (en) * | 2017-09-28 | 2018-06-08 | 首例国际股份有限公司 | Dynamic wet type gas flow absorber |
| CN109174458A (en) * | 2018-08-31 | 2019-01-11 | 深圳市天得环境科技有限公司 | Wet type moisture film collecting electrode, wet type water film dust removal device and its application method |
| CN209613242U (en) * | 2019-02-21 | 2019-11-12 | 杨运海 | A kind of combination electrostatic field roller shutter type air cleaning facility |
| CN110793077A (en) * | 2019-10-12 | 2020-02-14 | 合肥三邦环保科技有限公司 | Combined type clarification plant of clean system of area monitoring |
| CN111729761A (en) * | 2020-06-25 | 2020-10-02 | 宁波市镇海西门专利技术开发有限公司 | Dust collection paper |
| CN213590793U (en) * | 2020-11-06 | 2021-07-02 | 中物院成都科学技术发展中心 | Wet electrostatic dust collector |
-
2020
- 2020-11-06 CN CN202011229503.8A patent/CN112237991B/en active Active
Patent Citations (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06233945A (en) * | 1993-02-10 | 1994-08-23 | Daikin Ind Ltd | Winding type dust removing filter |
| JPH1119534A (en) * | 1997-07-04 | 1999-01-26 | Pioneer Electron Corp | Electrostatic air cleaner and dust collecting paper therefor |
| CN2566212Y (en) * | 2002-06-28 | 2003-08-13 | 煜丰科技股份有限公司 | Water evaporation cover capable of raising heat exchanging efficiency |
| CN102245751A (en) * | 2008-12-09 | 2011-11-16 | 花王株式会社 | Method for manufacturing detergent particles |
| CN102784719A (en) * | 2012-08-20 | 2012-11-21 | 山东大学 | Water internally-distributed type flexible dust collecting electrode device |
| JP2016064409A (en) * | 2014-09-17 | 2016-04-28 | パナソニックＩｐマネジメント株式会社 | Air cleaner |
| JP2016087538A (en) * | 2014-11-04 | 2016-05-23 | 帝人株式会社 | Dust remover |
| CN106540809A (en) * | 2015-09-16 | 2017-03-29 | 武汉科技大学 | A kind of water logging self-cleaning cloth roller shutter wet electrostatic dust arrester installation |
| KR20170090217A (en) * | 2016-01-28 | 2017-08-07 | 케이씨코트렐 주식회사 | A electric precipitator with injection device forming a water film |
| CN105797865A (en) * | 2016-05-10 | 2016-07-27 | 艾尼科环保技术(安徽)有限公司 | Flexible polar plate of wet electrostatic dust remover |
| CN106765583A (en) * | 2017-01-12 | 2017-05-31 | 张宗炜 | The method of air cleaning unit and purify air |
| CN207254551U (en) * | 2017-09-18 | 2018-04-20 | 保定坤泰环保节能科技有限公司 | A kind of novel air pollutes cleaning equipment |
| CN207462840U (en) * | 2017-09-28 | 2018-06-08 | 首例国际股份有限公司 | Dynamic wet type gas flow absorber |
| CN109174458A (en) * | 2018-08-31 | 2019-01-11 | 深圳市天得环境科技有限公司 | Wet type moisture film collecting electrode, wet type water film dust removal device and its application method |
| CN209613242U (en) * | 2019-02-21 | 2019-11-12 | 杨运海 | A kind of combination electrostatic field roller shutter type air cleaning facility |
| CN110793077A (en) * | 2019-10-12 | 2020-02-14 | 合肥三邦环保科技有限公司 | Combined type clarification plant of clean system of area monitoring |
| CN111729761A (en) * | 2020-06-25 | 2020-10-02 | 宁波市镇海西门专利技术开发有限公司 | Dust collection paper |
| CN213590793U (en) * | 2020-11-06 | 2021-07-02 | 中物院成都科学技术发展中心 | Wet electrostatic dust collector |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117589945A (en) * | 2024-01-11 | 2024-02-23 | 武汉瑞气节能环保科技有限公司 | Wisdom air compressor station is with air detection device |
| CN117589945B (en) * | 2024-01-11 | 2024-04-12 | 武汉瑞气节能环保科技有限公司 | Wisdom air compressor station is with air detection device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN112237991B (en) | 2023-02-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN112237991B (en) | Wet electrostatic dust collector | |
| CN213590793U (en) | Wet electrostatic dust collector | |
| CN106955554A (en) | A kind of industrial air cleaner of self-cleaning | |
| CN209810586U (en) | Electrostatic flocking device | |
| CN207308096U (en) | A kind of slurries filtration deironing apparatus of lithium battery | |
| CN208414163U (en) | A kind of processing system for dyeing waste water | |
| CN108525403B (en) | Paint mist dry type filtering module and purifying device applied by same | |
| CN207445742U (en) | A kind of pre-classification disk filter | |
| CN113387416B (en) | Graphene composite photocatalytic glass fiber electrode material and preparation method thereof | |
| CN2784085Y (en) | Novel electromechanical integration electric precipitator | |
| CN211329873U (en) | Novel agricultural crushing machine matched dust remover group | |
| CN211799397U (en) | Organic waste gas processor | |
| CN211412352U (en) | Automatic centrifugal wet electrostatic dust collector | |
| CN212881650U (en) | A dust collector for metal silica flour production line | |
| CN203240673U (en) | Air purifier | |
| CN203253532U (en) | Hollow pole plate electrostatic dust removing apparatus formed from porous dielectric material | |
| CN206064012U (en) | A kind of automatically cleaning bag filter | |
| CN214555303U (en) | Improved winnowing system for mineral separation | |
| CN201308799Y (en) | Flat-bag pulsating composite dust remover combining electric dust removing with bag dust removing | |
| CN112316732A (en) | Device for rapidly infiltrating and cleaning membrane yarns and utilization method thereof | |
| CN220194293U (en) | Drying structure and bag-type dust remover | |
| CN2469981Y (en) | Efficient gas filtering device | |
| CN218951520U (en) | Double-flue dust remover for electrolytic cell | |
| CN211660695U (en) | Textile dust collecting device for fabric spinning | |
| CN215233035U (en) | FFU fan filter unit with peculiar smell remove device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |