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WO2020085231A1 - Dust removal device - Google Patents

Dust removal device Download PDF

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Publication number
WO2020085231A1
WO2020085231A1 PCT/JP2019/041053 JP2019041053W WO2020085231A1 WO 2020085231 A1 WO2020085231 A1 WO 2020085231A1 JP 2019041053 W JP2019041053 W JP 2019041053W WO 2020085231 A1 WO2020085231 A1 WO 2020085231A1
Authority
WO
WIPO (PCT)
Prior art keywords
nozzle
counter electrode
blower
droplet
air
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.)
Ceased
Application number
PCT/JP2019/041053
Other languages
French (fr)
Japanese (ja)
Inventor
上田 泰稔
怜 竹井
長安 弘貢
正志 清澤
亮太 文
晴治 香川
一明 三宅
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.)
Mitsubishi Power Ltd
Mitsubishi Power Environmental Solutions Ltd
Original Assignee
Mitsubishi Hitachi Power Systems Ltd
Mitsubishi Hitachi Power Systems Environmental Solutions 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 Mitsubishi Hitachi Power Systems Ltd, Mitsubishi Hitachi Power Systems Environmental Solutions Ltd filed Critical Mitsubishi Hitachi Power Systems Ltd
Publication of WO2020085231A1 publication Critical patent/WO2020085231A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F7/00Ventilation
    • F24F7/003Ventilation in combination with air cleaning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02Plant or installations having external electricity supply
    • B03C3/16Plant or installations having external electricity supply wet type
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/66Applications of electricity supply techniques
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/66Applications of electricity supply techniques
    • B03C3/70Applications of electricity supply techniques insulating in electric separators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/74Cleaning the electrodes
    • B03C3/78Cleaning the electrodes by washing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B5/00Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means
    • B05B5/025Discharge apparatus, e.g. electrostatic spray guns
    • B05B5/053Arrangements for supplying power, e.g. charging power
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B5/00Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means
    • B05B5/08Plant for applying liquids or other fluent materials to objects
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F6/00Air-humidification, e.g. cooling by humidification
    • F24F6/12Air-humidification, e.g. cooling by humidification by forming water dispersions in the air
    • F24F6/14Air-humidification, e.g. cooling by humidification by forming water dispersions in the air using nozzles

Definitions

  • the present disclosure relates to a dust removing device.
  • At least one embodiment of the present invention aims to provide a dust remover capable of removing fine particles floating in the air in a relatively wide space.
  • a dust removing device At least one nozzle, which is arranged at the blowout part of the blown air, is capable of ejecting the supplied liquid as droplets, and is connected to the ground;
  • the counter electrode includes a counter electrode having a shape surrounding at least a half circumference of one opening, and one counter electrode is provided for one of the nozzles, and the counter electrode is arranged in a direction in which the nozzle ejects a droplet.
  • a high voltage generator for applying a high voltage to the counter electrode which has a ground terminal connected to the ground and connected to an output terminal, Equipped with The current flowing between the nozzle and the ground is, when a leakage current does not flow between the nozzle and the counter electrode, per injection amount of the droplet of 1 liter / min and the opening area of the blowing portion. It is less than 0.3 milliamps / (square meter liter / minute) per square meter.
  • the amount is less than 0.3 mA / (square meter liter / minute) per 1 liter / minute and per 1 square meter opening area of the air outlet, it is effective for the fine particles in the atmosphere in the above-mentioned relatively wide space and outdoors.
  • the droplets can be charged so that they can be selectively collected.
  • the nozzle is configured to eject the droplet in a conical shape
  • the first distance from the jetting position of the droplet in the nozzle to the intersection of the plane including the counter electrode and the center line of the cone is r (millimeter)
  • the intersection is
  • the second distance that is the minimum distance between the counter electrode and the counter electrode is a 0 (millimeter)
  • the ejection angle at which the nozzle ejects the droplet is ⁇ (degrees)
  • the droplets ejected in a conical shape from the nozzle pass through the region inside the counter electrode in the opening surrounded by the counter electrode. Can be made. As a result, it is possible to prevent the counter electrode from getting wet with droplets, and it is possible to suppress the flow of leakage current between the nozzle and the counter electrode.
  • the first distance is 5 mm or more and 200 mm or less
  • the second distance is 5 mm or more and 50 mm or less.
  • the high voltage applied to the counter electrode forms the droplet at the nozzle ejection position, that is, at the nozzle tip.
  • the strength of the applied electric field can be sufficiently increased.
  • the ejection angle of the nozzle is 30 degrees or more and 100 degrees or less.
  • the configuration of (4) by setting the ejection angle of the nozzle to 30 degrees or more and 100 degrees or less, wetting of the counter electrode with droplets can be suppressed, and the electric field strength required for charging the droplets can be reduced. Can be secured.
  • the at least one nozzle has a droplet diameter of 10 ⁇ m or more and 300 ⁇ m or less in terms of Sauter average diameter.
  • the droplets can be ejected.
  • a blower for blowing the air containing the droplets In some embodiments, in any of the configurations of (1) to (5) above, And a blower for blowing the air containing the droplets, The nozzle and the electrode unit are attached to the housing of the blower.
  • the air blown from the blower can diffuse the droplets into a relatively wide space, so that dust can be removed in a relatively wide space.
  • the nozzle and the electrode portion are installed at positions where the droplets can be effectively diffused by the air blown from the blower. It becomes easy to do.
  • a support portion configured by an insulating material and supporting the electrode portion, A scavenging nozzle configured to inject a gas toward the support portion, Is further provided.
  • the high-voltage current applied to the counter electrode may flow as a leakage current to the ground side via the supporting part wet with the droplet.
  • the configuration of (7) above by injecting gas from the scavenging nozzle toward the support portion, it is possible to suppress liquid droplets from adhering to the support portion and suppress the generation of leakage current. .
  • It further comprises a support portion configured to be formed of a water-repellent insulating material, or formed of an insulating material and having a surface subjected to a water-repellent treatment, for supporting the electrode portion.
  • the high-voltage current applied to the counter electrode may flow as a leakage current to the ground side through the supporting part wet with the liquid droplets.
  • the water repellency can prevent the droplet from adhering to the supporting portion.
  • the droplet contacts the supporting portion it is possible to prevent the entire surface of the supporting portion from getting wet with the liquid. Thereby, the generation of leakage current can be suppressed.
  • the droplets can be uniformly applied to the flow of air blown from the blower by ejecting the droplets from the plurality of nozzles.
  • An air blower for blowing air containing the droplets the blower having the blowing portion;
  • a direction changing device configured to change the blowing direction of air from the blower, Is further provided.
  • An air blower for blowing air containing the droplets the blower having the blowing portion;
  • a direction changing device configured to change the blowing direction of air from the blower, Further equipped with,
  • the direction changing device is configured to be able to set the air blowing direction so that the air can be blown at least above the horizontal direction.
  • the direction changing device in the configuration of (10) or (11), is capable of setting the air blowing direction so that air can be blown upward at an elevation angle of 0 degrees or more. Has been done.
  • the direction changing device sets an ejection direction of the droplet from the at least one nozzle to an air from the blower. It is configured to be changeable in the same direction as the air blowing direction of.
  • the jetting direction of the droplets from the nozzle can be changed to the same blowing direction of the air from the blower, the droplets can be efficiently applied to the flow of air blown from the blower. it can.
  • expressions such as “identical”, “equal”, and “homogeneous” that indicate that they are in the same state are not limited to strict equality, but also include tolerances or differences in the degree to which the same function is obtained. It also represents the existing state.
  • the representation of a shape such as a quadrangle or a cylindrical shape does not only represent a shape such as a quadrangle or a cylindrical shape in a geometrically strict sense, but also an uneven portion or a chamfer within a range in which the same effect can be obtained.
  • the shape including parts and the like is also shown.
  • the expressions “comprising”, “comprising”, “comprising”, “including”, or “having” one element are not exclusive expressions excluding the existence of other elements.
  • FIG. 1 is a perspective view schematically showing the appearance of a dust remover according to some embodiments.
  • FIG. 2 is a view of a dust removing device according to some embodiments as seen from a downstream side in a blowing direction of a blower described later, and shows a main part.
  • FIG. 3 is a side view of the dust remover according to some embodiments, and schematically shows the configuration of the main part.
  • the dust remover 1 includes a blower 10, a nozzle 20, an electrode unit 30, and a high voltage generator 40.
  • a blower 10 is a blower for blowing air including droplets 2 (see FIG. 3) ejected by a nozzle 20 described later.
  • the blower 10 according to some embodiments includes an impeller 12 that is rotated by a driving force of a motor (not shown) inside a casing 11 having a cylindrical shape, for example, and the cylindrical casing 11 is rotated by the rotation of the impeller 12. Air is sucked in from one end and blown in from the left side to the right side in the drawing as shown by an arrow C in FIG. 3, and is discharged from the blowing section 13 at the other end.
  • the nozzle 20 is a nozzle capable of ejecting the liquid supplied from the supply pump 29 as droplets, and is generally also called a spray nozzle.
  • the liquid supplied to the nozzle 20 is water, for example.
  • the nozzle 20 is attached to the supply pipe 22 and arranged in the blowout air blower 13. More specifically, the nozzle 20 is arranged at a position separated from the blowout portion 13 at the other end of the housing 11 of the blower 10 on the downstream side in the blowing direction.
  • the supply pipe 22 is attached to the housing 11 of the blower 10 by the pipe attachment portion 24.
  • multiple nozzles 20 are provided. In the example shown in FIGS. 1 and 2, eight nozzles 20 are provided, but the number of nozzles 20 may be one or more.
  • the nozzle 20 ejects droplets toward the downstream side of the blower 10 in the blowing direction.
  • the nozzle 20 is configured to eject the droplet 2 in a conical shape.
  • the nozzle 20 according to some embodiments is configured to be capable of ejecting a droplet having a droplet diameter of 10 ( ⁇ m) or more and 300 ( ⁇ m) or less in average Sauter diameter.
  • the ejection angle ⁇ of the nozzle 20 according to some embodiments is 30 degrees or more and 100 degrees or less. The droplet diameter and the spray angle ⁇ will be described in detail later.
  • the nozzle 20 is connected to the ground 9. Specifically, the nozzle 20 according to some embodiments is connected to the ground 9 via the supply pipe 22, for example, by connecting the supply pipe 22 to the ground 9.
  • the nozzle 20 and the supply pipe 22 are formed of a conductive member such as metal.
  • the electrode unit 30 includes a plurality of counter electrodes 31 and an electrode support member 35 that supports the plurality of counter electrodes.
  • Each of the counter electrodes 31 according to some embodiments has a shape surrounding the periphery of the opening 33.
  • Each of the counter electrodes 31 according to some embodiments has, for example, an annular shape.
  • Each of the counter electrodes 31 may have, for example, an elliptical ring shape, or may have a polygonal shape such as a rectangular shape surrounding the periphery of the opening 33.
  • the counter electrodes 31 may have the same size or different sizes.
  • the counter electrodes 31 may have the same shape or different shapes. Further, each of the counter electrodes 31 does not necessarily have to have a closed shape, and may have, for example, a shape that surrounds the periphery of the opening 33 for at least a half circumference or more.
  • one counter electrode is provided for one nozzle 20.
  • a plurality of counter electrodes 31 are supported by an electrode support member 35.
  • the counter electrode 31 is arranged apart from the nozzle 20 in the direction in which the nozzle 20 ejects droplets, and is supported by the support unit 51 made of an insulating material. Specifically, one end of the columnar support portion 51 is fixed to the mounting portion 15 provided at the other end of the casing 11 of the blower 10, and the electrode support member 35 of the electrode portion 30 is fixed to the other end of the support portion 51. Has been done.
  • the high voltage generator 40 is a device capable of generating a high voltage of, for example, 1 kilovolt or more.
  • the ground terminal 42 is connected to the ground 9, and a high voltage can be applied to the counter electrode 31 (electrode portion 30) connected to the output terminal 41.
  • the blower 10 is supported by the blower support portion 61 so as to be able to rise and fall, as indicated by an arrow A in FIG. 1.
  • the blower 10 is rotatable about the central axis CL by the turning device 65 as shown by an arrow B in FIG. 1. That is, the blower 10 can rotate in a plane parallel to the mounting surface of the turning device 65, such as the floor.
  • the direction changing device 60 configured to change the blowing direction of the air from the blower includes the blower support portion 61 and the turning device 65.
  • the liquid (water) supplied from the supply pump 29 can be sprayed as droplets by the plurality of nozzles 20. Then, in the dust removing device 1 according to some embodiments, by applying the high voltage generated by the high voltage generating device 40 to the counter electrode 31, the droplet 2 sprayed from the nozzle 20 is applied to the counter electrode 31. It can be charged to the opposite polarity of the applied voltage. Further, in the dust removing device 1 according to some embodiments, it is possible to diffuse the charged droplets 2 to the surroundings by blowing air from the blower 10 in a relatively large space such as a gymnasium or an indoor stadium or outdoors. it can. The charged droplets 2 can collect fine powder in the air by electrostatic force. The fine powder collected in the droplet 2 falls on the ground together with the droplet 2. Thus, for example, in a relatively large space such as a gymnasium or an indoor arena, or outdoors, fine particles in the atmosphere can be efficiently collected and removed by the charged droplets 2.
  • FIG. 4 is a schematic diagram for explaining the mechanism of charging the droplet 2.
  • a high voltage from the high voltage generator 40 is applied to the counter electrode 31, the liquid ejected from the nozzle 20 is generated by the electric field formed by the potential difference between the counter electrode 31 and the nozzle 20 connected to the ground 9.
  • the drop 2 is dielectrically polarized.
  • a negative high voltage is applied to the counter electrode 31 from the high voltage generator 40, in the droplet 2 immediately before being ejected from the nozzle 20, a region near the counter electrode 31 is positively charged, and the counter electrode 31 is charged. Areas far from 31 are negatively charged.
  • the polarization charge induced in the region far from the counter electrode 31 flows to the ground (ground 9) through the conductive nozzle 20 and the supply pipe 22. As a result, the droplet 2 ejected from the nozzle 20 is positively charged.
  • the dust remover 1 it is possible to charge the droplet 2 sprayed from the nozzle 20 to a polarity opposite to the polarity of the voltage applied to the counter electrode 31 by dielectric polarization. it can.
  • the dust remover 1 since the dust remover 1 according to some embodiments includes the nozzle 20, the electrode unit 30, and the high-voltage generator 40, a relatively large amount of the droplet 2 generated by the nozzle 20 is subjected to dielectric polarization. Can be charged by. In the dust remover 1 according to some embodiments, it is not necessary to apply a current to the counter electrode 31 to charge the droplet 2 because of the principle of charging the droplet 2 by dielectric polarization. Therefore, in the dust remover 1 according to some embodiments, the total value of the currents flowing from the high voltage generator 40 to all the counter electrodes 31 is the same as when the leakage current does not flow between the nozzle 20 and the counter electrode 31. In addition, it is possible to suppress it to less than 0.1 (mA), for example.
  • mA 0.1
  • the high voltage generator 40 having a relatively low output power causes a relatively large amount of liquid with an effective charge amount for collecting fine particles in the atmosphere.
  • the drop 2 can be charged.
  • the particles 2 in the atmosphere can be efficiently collected and removed by the charged droplets 2 in a relatively large space such as a gymnasium or an indoor stadium or outdoors.
  • the dust remover 1 since it is not necessary to pass a current through the counter electrode 31 to charge the droplet 2, the high-voltage high-voltage generator 40 has a large output. It is unnecessary, and the cost of the high voltage generator 40 can be suppressed.
  • the dust removers 1 in principle, it is not necessary to apply a current to the counter electrode 31 to charge the droplet 2. Therefore, by ensuring the insulation of the counter electrode 31 (electrode portion 30) so that the leakage current does not flow between the nozzle 20 and the counter electrode 31, almost all the current flowing from the high voltage generator 40 to the counter electrode 31 is generated. You can choose not to. Thereby, the rated output of the high voltage generator 40 can be reduced, and the cost of the high voltage generator 40 can be further suppressed.
  • FIG. 5 is a diagram for explaining the positional relationship between the nozzle 20 and the counter electrode 31.
  • the positional relationship between the nozzle 20 and the counter electrode 31 will be described.
  • the nozzle 20 is configured to eject the droplet 2 in a conical shape. Therefore, in order to prevent the liquid droplets 2 ejected from the nozzle 20 from directly contacting the counter electrode 31, in the dust removers 1 according to some embodiments, the positional relationship between the nozzle 20 and the counter electrode 31 is as follows. The formula (1) described in (3) is satisfied.
  • the second distance L2, which is the minimum distance between the counter electrode 31 and the counter electrode 31, is a 0 (millimeter)
  • the ejection angle at which the nozzle 20 ejects the droplet 2 is ⁇ (degrees).
  • the relationship is expressed by the following equation (1). r ⁇ a 0 / tan ( ⁇ / 2) (1)
  • the droplet 2 that is conically ejected from the nozzle 20 can pass through the region inside the counter electrode 31 in the opening 33 surrounded by the counter electrode 31.
  • the counter electrode 31 it is possible to prevent the counter electrode 31 from getting wet with the liquid droplet 2, and it is possible to prevent a leakage current from flowing between the nozzle 20 and the counter electrode 31.
  • the ejection angle of the nozzle 20 is preferably 30 degrees or more and 100 degrees or less, as described above. That is, when the spray angle is large, the counter electrode 31 is likely to be wet with the droplet 2. Therefore, current leakage is likely to occur, and it becomes difficult to secure the electric field strength necessary for charging the droplets. Therefore, by setting the ejection angle of the nozzle 20 to 30 degrees or more and 100 degrees or less, it is possible to prevent the counter electrode 31 from getting wet with the droplet 2 and to secure the electric field strength necessary for charging the droplet.
  • the second distance L2 which is the minimum distance between the intersection C1 and the counter electrode 31, is 5 (mm). It is better to be 50 (mm) or less.
  • the first distance L1 from the tip 20a of the nozzle 20 to the intersection C1 is preferably 5 (mm) or more and 200 (mm) or less.
  • the second distance L2 is the inner radius of the counter electrode 31.
  • FIG. 6 is a diagram for further explaining the first distance L1.
  • the electric field strength formed at the tip 20a of the nozzle 20 is generally expressed by the following equation (2), and when the inner radius and the outer radius of the counter electrode 31 are determined, the electric field strength becomes a maximum value.
  • the distance (first distance L1) is determined.
  • E ⁇ r / (a ⁇ a 0 ) ⁇ ⁇ 1 / (a 2 + r 2 ) 0.5 ⁇ 1 / (a 0 2 + r 2 ) 0.5 ⁇ ⁇ V 0
  • a is the outer radius L3 (m) of the counter electrode 31
  • a 0 is the inner radius L2 (m) of the counter electrode 31 as described above.
  • r is the first distance L1 (m) from the tip 20a of the nozzle 20 to the intersection C1 as described above.
  • V 0 is a voltage (V) applied to the counter electrode.
  • E is the electric field intensity (V / m) at the tip 20a of the nozzle 20.
  • the applied voltage V 0 is preferably 5 (kV) or more and 80 (kV) or less.
  • the droplet ejection position in the nozzle 20 by the high voltage applied to the counter electrode 31 That is, the strength of the electric field formed at the tip 20a of the nozzle 20 can be sufficiently increased. If the first distance L1 does not fall within the above range due to, for example, the insulating structure of the electrode portion 30, the inner radius and the outer radius of the counter electrode 31 are adjusted so that the electric field strength E becomes equal to the first distance. It is good to make it maximum with respect to L1.
  • the nozzle 20 is configured to be capable of ejecting a liquid droplet having a Sauter mean diameter of 10 ( ⁇ m) or more and 300 ( ⁇ m) or less.
  • a Sauter mean diameter 10 ( ⁇ m) or more and 300 ( ⁇ m) or less.
  • the fine particles in the atmosphere are droplets. Can be effectively collected.
  • the dust remover 1 since the dust remover 1 according to some embodiments includes the blower 10, the droplets 2 can be diffused into a relatively wide space by the air blown from the blower 10, so that the dust in the relatively wide space is removed. It can be performed. Further, in the dust remover 1 according to some embodiments, since the nozzle 20 and the electrode unit 30 are attached to the housing 11 of the blower 10, it is possible to effectively diffuse the droplets 2 by blowing air from the blower 10. It becomes easy to install the nozzle 20 and the electrode part 30 at a position where the above can be achieved.
  • FIG. 7 is a view of a dust removing device according to another embodiment as viewed from the downstream side of the blower in the blowing direction, and shows the main part.
  • a scavenging nozzle 71 is further provided in addition to the dust removers 1 according to some of the above-described embodiments.
  • the scavenging nozzle 71 is a nozzle configured to be able to inject gas toward the support portion 51 that supports the electrode portion 30.
  • the scavenging nozzle 71 is arranged on the outer side in the radial direction of the housing 11 with respect to the support portion 51, and as shown by an arrow b, the housing is shown.
  • Gas can be ejected from the outside of the body 11 in the radial direction toward the inside.
  • two scavenging nozzles 71 are arranged for one support portion 51, but if at least one scavenging nozzle 71 is arranged. Good.
  • the high-voltage current applied to the counter electrode 31 is leaked to the ground side via the support portion 51 wet with the droplet 2 and the housing 11 of the blower 10. It may flow.
  • the droplet 2 is attached to the support portion 51 by injecting gas from the scavenging nozzle 71 toward the support portion 51. It is possible to suppress the occurrence of leakage current.
  • the scavenging nozzle 71 may be provided for all of the supporting portions 51, or may be provided only for the supporting portion 51 that is easily wetted in the most frequently used postures among the postures of the blower 10. Good.
  • the support portion 51 is made of a water-repellent insulating material, or is made of an insulating material and the surface thereof is subjected to a water-repellent treatment. It is good to have Accordingly, even if the droplet 2 comes into contact with the support portion 51, it is possible to suppress the droplet 2 from adhering to the support portion 51 due to its water repellency. Further, even if the droplet 2 comes into contact with the support portion 51, it is possible to prevent the entire surface of the support portion 51 from getting wet with the liquid. Thereby, the generation of leakage current can be suppressed.
  • a plurality of nozzles 20 are provided on the downstream side of the blower with respect to the flow of air blown by the blower 10. Accordingly, by ejecting the droplets 2 from the plurality of nozzles 20, the droplets 2 can be uniformly applied to the flow of air blown from the blower 10.
  • the flow velocity of the blown air blown out from the blowout portion 13 of the blower 10 is preferably 5 (m / sec) or more.
  • the flow velocity of the blown air blown out from the blowing portion 13 is equal to that of the liquid ejected from the nozzle 20.
  • the ejection speed of the droplet 2 is preferably 0.5 times or more.
  • the dust remover 1 includes a direction changing device 60 configured to change the blowing direction of air from the blower. Therefore, by changing the blowing direction of the air from the blower 10 by the direction changing device 60, it is possible to easily change the direction in which the droplets 2 are scattered, with the arrangement position of the dust removing device 1 as the starting point.
  • the direction changing device 60 may be configured to be able to set the air blowing direction so that the air can be blown at least above the horizontal direction.
  • the dust removing device 1 arranged at a low position on the floor or the like can collect fine particles floating in the space above the floor.
  • the direction changing device 60 is configured to be able to set the air blowing direction so that the air can be blown upward at an elevation angle of 0 degrees or more, more preferably, an elevation angle of 30 degrees or more. It is good to have been. This makes it possible to effectively disperse the droplets 2 that drop with the passage of time at a position away from the dust removing device 1.
  • the direction changing device 60 is configured to be able to change the ejection direction of the droplet 2 from the nozzle 20 to the same direction as the blowing direction of the air from the blower 10. That is, in the dust remover 1 according to some embodiments, the plurality of nozzles 20 are attached to the housing 11 of the blower 10 via the supply pipe 22 and the pipe attachment portion 24. In the dust removing device 1 according to some embodiments, the direction changing device 60 can change the posture of the housing 11 of the blower 10. Therefore, the jetting direction of the droplet 2 from the nozzle 20 can be changed to the same blowing direction of the air from the blower 10, so that the droplet 2 can be efficiently applied to the flow of air blown from the blower 10.
  • the spray amount of the liquid may be 0.01 (l / min) or more per region 1 (m 3 ) where the fine particles are removed.
  • the electric field strength formed at the tip 20a of the nozzle 20 is preferably 0.5 (kV / cm) or more and 10 (kV / cm) or less.
  • the droplet diameter of the droplet 2 is preferably 10 ( ⁇ m) or more and 300 ( ⁇ m) or less in terms of Sauter average diameter.
  • the polarization charge amount q per unit area when the droplet 2 is assumed to be a sphere is expressed by the following equation (4).
  • q 3 ⁇ ⁇ 0 ⁇ E ⁇ ( ⁇ s ⁇ 1) / ( ⁇ s +2) (4)
  • ⁇ 0 is the dielectric constant in vacuum
  • ⁇ 0 8.854 ⁇ 10 ⁇ 12 (F / m).
  • the charge amount Qp of one droplet 2 is the product of the polarization charge amount q per unit area and the surface area s of one droplet 2, and is given by the following equation (5).
  • this charge amount (Np ⁇ Qp) is a value when the spray amount is 9 (l / min), it is 0.015 (mA) when converted per spray amount 1 (l / min).
  • the value of this current (0.015 (mA)) represents the amount of charge carried by the droplets 2 sprayed at a spray rate of 1 (l / min) as a current. Further, since the droplet 2 is diffused into the atmosphere by the blown air blown from the blower 10, the current value calculated as described above is divided by the opening area of the blowout portion 13 of the blower 10 to obtain the blower. It is possible to obtain the apparent current density of the blown air containing the droplets 2 in the blowing portion 13 of 10.
  • the inner diameter of the blowout portion 13 of the blower 10 is, for example, 300 (mm)
  • the value of the current flowing between the nozzle 20 and the ground 9 is, as described above, per unit time carried by the droplet 2. Equal to the amount of charge. Therefore, by measuring the value of the current flowing between the nozzle 20 and the ground 9, the amount of charge carried by the droplet 2 per unit time can be obtained. Furthermore, by measuring the flow rates of the liquids supplied to all the nozzles 20, the apparent current density of the blown air containing the droplets 2 in the blowout part 13 of the blower 10 can be calculated as the spray amount 1 (l / min). It can be obtained as a value around.
  • the blown air containing the droplets 2 in the blowout unit 13 of the blower 10 is also taken into consideration.
  • the apparent current density may be 0.3 (mA / m 2 ) or less per spray amount 1 (l / min). That is, when the leakage current does not flow between the nozzle 20 and the counter electrode 31, the current flowing between the nozzle 20 and the ground 9 is about 1 (l / min) of the ejection amount of the droplet 2 and the blowing portion. It is considered that it may be 0.3 (mA / (m 2 ⁇ l / min) or less per opening area 1 (m 2 ) of 13.
  • the current flowing between the nozzle 20 and the ground 9 causes the droplet ejection amount 1 Even if it is 0.3 mA / (mA / (m 2 ⁇ l / min) or less per (l / min) and the opening area 1 (m 2 ) of the blowout portion 13, for example, in a gymnasium or an indoor stadium.
  • the droplets can be charged so as to effectively collect fine particles in the atmosphere in such a relatively large space or outdoors.
  • the current density (10 (mA / m 2 )) needs to be the above in the cross section where the droplets are sprayed.
  • the counter electrode 31 is replaced with one discharge electrode for performing corona discharge, and the other discharge electrode for performing corona discharge is arranged in the blowing portion 13.
  • the current density (10 (mA / m 2 )) is at least in the region between the discharge electrodes, in the region where the blowout portion 13 is projected when the blowout portion 13 is viewed from the downstream side in the blowing direction.
  • the present invention is not limited to the above-described embodiments, and includes forms obtained by modifying the above-described embodiments, and forms obtained by appropriately combining these forms.

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Abstract

This dust removal device comprises: at least one nozzle that is disposed in a blow-out part for blown air, is capable of spraying a supplied liquid in the form of droplets, and is connected to ground; an electrode part that includes a counter electrode which is shaped so as to surround at least half of the circumference of one opening, with one counter electrode provided for one nozzle, and with the counter electrode being disposed so as to be separated from the nozzle in the direction in which the nozzle sprays the droplets; and a high-voltage generation device that has a ground terminal connected to ground, and that is for applying a high voltage to the counter electrode which is connected to an output terminal. If a leakage current is not flowing between the nozzle and the counter electrode, the current flowing between the nozzle and ground is no greater than 0.3 milliamperes (square meters/liter per minute) for every 1 liter per minute of droplet spray and every 1 square meter of the opening surface area of the blow-out part.

Description

除塵装置Dust remover

 本開示は、除塵装置に関する。 The present disclosure relates to a dust removing device.

 空気中に浮遊するPM(Particulate Matter)等の微粒子を除去するために、例えば、帯電させた液滴によって空気中の微粒子を捕集することが考えられる。
 例えば、特許文献1に記載された空気浄化装置では、平板に設けた微細孔から吐出された水柱を静電霧化によって微細化することで、帯電した液滴を生成することができる。該空気浄化装置では、帯電した液滴を室内に供給することによって空気中に含まれる粉塵等を除去することができる(特許文献1参照)。
In order to remove fine particles such as PM (Particulate Matter) floating in the air, it is conceivable to collect the fine particles in the air by charged droplets, for example.
For example, in the air purification device described in Patent Document 1, charged water droplets can be generated by atomizing the water column discharged from the fine holes provided in the flat plate by electrostatic atomization. In the air purification device, dust or the like contained in the air can be removed by supplying the charged droplets into the room (see Patent Document 1).

特開2006-97960号公報JP 2006-97960A

 しかし、特許文献1に記載の空気浄化装置では、平板に設けた微細孔から吐出された水柱を静電霧化によって微細化するため、多量の液滴を生成することが困難である。そのため、空気を浄化できるのは、家庭内空間やオフィス等の比較的狭い空間に限られてしまう。 However, in the air purification device described in Patent Document 1, it is difficult to generate a large amount of liquid droplets because the water column discharged from the fine holes provided in the flat plate is atomized by electrostatic atomization. Therefore, the air can be purified only in a relatively narrow space such as a home space or an office.

 上述の事情に鑑みて、本発明の少なくとも一実施形態は、比較的広い空間において空気中に浮遊する微粒子を除去することができる除塵装置を提供することを目的とする。 In view of the above-mentioned circumstances, at least one embodiment of the present invention aims to provide a dust remover capable of removing fine particles floating in the air in a relatively wide space.

(1)本発明の少なくとも一実施形態に係る除塵装置は、
 送風空気の吹出し部に配置され、供給された液体を液滴として噴射可能であり、接地に接続されている、少なくとも1つのノズルと、
 1つの開口の周囲を少なくとも半周以上囲む形状を有する対向電極を含み、前記ノズルの1つに対して1つの前記対向電極が設けられ、前記ノズルが液滴を噴射する方向に前記対向電極が前記ノズルから離間して配置される電極部と、
 接地端子が前記接地に接続され、出力端子に接続された前記対向電極に高電圧を印加するための高電圧発生装置と、
を備え、
 前記ノズルと前記接地との間を流れる電流は、前記ノズルと前記対向電極との間で漏洩電流が流れていない場合に、前記液滴の噴射量1リットル/分あたり及び前記吹出し部の開口面積1平方メートルあたりで、0.3ミリアンペア/(平方メートル・リットル/分)以下である。
(1) A dust removing device according to at least one embodiment of the present invention,
At least one nozzle, which is arranged at the blowout part of the blown air, is capable of ejecting the supplied liquid as droplets, and is connected to the ground;
The counter electrode includes a counter electrode having a shape surrounding at least a half circumference of one opening, and one counter electrode is provided for one of the nozzles, and the counter electrode is arranged in a direction in which the nozzle ejects a droplet. An electrode portion arranged apart from the nozzle,
A high voltage generator for applying a high voltage to the counter electrode, which has a ground terminal connected to the ground and connected to an output terminal,
Equipped with
The current flowing between the nozzle and the ground is, when a leakage current does not flow between the nozzle and the counter electrode, per injection amount of the droplet of 1 liter / min and the opening area of the blowing portion. It is less than 0.3 milliamps / (square meter liter / minute) per square meter.

 上述したように、上記特許文献1に記載の空気浄化装置では、平板に設けた微細孔から吐出された水柱を静電霧化によって微細化するため、多量の液滴を生成することが困難である。
 その点、上記(1)の構成によれば、ノズルによって比較的多量の液滴を生成できる。そして、上記(1)の構成によれば、対向電極と接地されているノズルとの電位差によって形成される電界によって、ノズルから噴射される液滴を誘電分極させて、対向電極に印加された電圧の極性とは逆の極性に該液滴を帯電させることができる。このように、誘電分極によって液滴を帯電させるという原理から、液滴を帯電させるために対向電極に電流を流す必要はない。また、液滴の噴射量を増やしても、液滴1つあたりの誘電分極による電荷量は減らない。
 したがって、出力電力が比較的小さい高電圧発生装置によって、大気中の微粒子を捕集するのに効果的な電荷量で比較的多量の液滴を帯電させることができる。これにより、例えば体育館や屋内競技場のような比較的広い空間や、屋外において大気中の微粒子を帯電させた液滴で効率的に捕集して除去できる。
 また、上記(1)の構成によれば、上述したように、液滴を帯電させるために対向電極に電流を流す必要はないので、大出力の高電圧発生装置が不要であり、高電圧発生装置のコストを抑制できる。
 なお、発明者らが鋭意検討した結果、ノズルと対向電極との間で漏洩電流が流れないように対向電極の絶縁を確保することで、ノズルと接地との間を流れる電流が液滴の噴射量1リットル/分あたり及び吹出し部の開口面積1平方メートルあたりで、0.3ミリアンペア/(平方メートル・リットル/分)以下であっても、上述した比較的広い空間や屋外における大気中の微粒子を効果的に捕集できるように液滴を帯電できる。
As described above, in the air purification apparatus described in Patent Document 1, since the water column discharged from the fine holes provided in the flat plate is atomized by electrostatic atomization, it is difficult to generate a large amount of droplets. is there.
On the other hand, according to the above configuration (1), a relatively large amount of droplets can be generated by the nozzle. According to the configuration of (1), the electric field formed by the potential difference between the counter electrode and the grounded nozzle causes the liquid droplets ejected from the nozzle to be dielectrically polarized, and the voltage applied to the counter electrode. The droplet can be charged with a polarity opposite to that of. In this way, from the principle of charging the liquid droplets by dielectric polarization, it is not necessary to apply a current to the counter electrode to charge the liquid droplets. Further, even if the ejection amount of the droplets is increased, the charge amount due to the dielectric polarization per droplet does not decrease.
Therefore, it is possible to charge a relatively large amount of liquid droplets with a charge amount effective for collecting fine particles in the atmosphere by the high voltage generator having a relatively small output power. As a result, it is possible to efficiently collect and remove fine particles in the atmosphere with charged droplets in a relatively large space such as a gymnasium or an indoor stadium, or outdoors.
Further, according to the configuration of (1), as described above, since it is not necessary to supply a current to the counter electrode to charge the liquid droplet, a high-output high-voltage generator is not required, and a high-voltage generation is possible. The cost of the device can be suppressed.
As a result of intensive studies by the inventors, by ensuring the insulation of the counter electrode so that a leakage current does not flow between the nozzle and the counter electrode, the current flowing between the nozzle and the ground is ejected from the droplet. Even if the amount is less than 0.3 mA / (square meter liter / minute) per 1 liter / minute and per 1 square meter opening area of the air outlet, it is effective for the fine particles in the atmosphere in the above-mentioned relatively wide space and outdoors. The droplets can be charged so that they can be selectively collected.

(2)幾つかの実施形態では、上記(1)の構成において、
 前記ノズルは、前記液滴を円錐状に噴射するように構成され、
 前記ノズルと前記対向電極との関係は、前記ノズルにおける前記液滴の噴射位置から前記対向電極を含む平面と前記円錐の中心線との交点までの第1距離をr(ミリメートル)とし、前記交点と前記対向電極との最小距離である第2距離をa(ミリメートル)とし、前記ノズルが前記液滴を噴射する噴射角度をθ(度)とすると、次式(1)
  r<a/tan(θ/2)・・・(1)
で表される。
(2) In some embodiments, in the configuration of (1) above,
The nozzle is configured to eject the droplet in a conical shape,
Regarding the relationship between the nozzle and the counter electrode, the first distance from the jetting position of the droplet in the nozzle to the intersection of the plane including the counter electrode and the center line of the cone is r (millimeter), and the intersection is When the second distance that is the minimum distance between the counter electrode and the counter electrode is a 0 (millimeter), and the ejection angle at which the nozzle ejects the droplet is θ (degrees), the following equation (1)
r <a 0 / tan (θ / 2) (1)
It is represented by.

 上記(2)の構成によれば、上記の式(1)を満たす場合には、対向電極が囲む開口において、ノズルから円錐状に噴射される液滴を、対向電極よりも内側の領域を通過させることができる。これにより、対向電極が液滴で濡れてしまうことを抑制でき、ノズルと対向電極との間で漏洩電流が流れることを抑制できる。 According to the configuration of the above (2), when the above equation (1) is satisfied, the droplets ejected in a conical shape from the nozzle pass through the region inside the counter electrode in the opening surrounded by the counter electrode. Can be made. As a result, it is possible to prevent the counter electrode from getting wet with droplets, and it is possible to suppress the flow of leakage current between the nozzle and the counter electrode.

(3)幾つかの実施形態では、上記(2)の構成において、
 前記第1距離は、5ミリメートル以上200ミリメートル以下であり、
 前記第2距離は、5ミリメートル以上50ミリメートル以下である。
(3) In some embodiments, in the configuration of (2) above,
The first distance is 5 mm or more and 200 mm or less,
The second distance is 5 mm or more and 50 mm or less.

 上記(3)の構成によれば、第1距離及び第2距離を上記範囲内に設定することで、対向電極に印加された高電圧によってノズルにおける液滴の噴射位置、すなわちノズルの先端において形成される電界の強度を十分に高めることができる。 According to the configuration of (3), by setting the first distance and the second distance within the above range, the high voltage applied to the counter electrode forms the droplet at the nozzle ejection position, that is, at the nozzle tip. The strength of the applied electric field can be sufficiently increased.

(4)幾つかの実施形態では、上記(2)又は(3)の構成において、前記ノズルの前記噴射角度は、30度以上100度以下である。 (4) In some embodiments, in the configuration of (2) or (3), the ejection angle of the nozzle is 30 degrees or more and 100 degrees or less.

 噴霧角度が大きくなると、対向電極が液滴で濡れ易くなってしまう。そのため、電流の漏洩が起こり易くなり、液滴の帯電に必要な電界強度の確保が難しくなってしまう。
 その点、上記(4)の構成によれば、ノズルの噴射角度を30度以上100度以下とすることで、対向電極が液滴で濡れることを抑制でき、液滴の帯電に必要な電界強度を確保できる。
When the spray angle is large, the counter electrode is easily wet with the liquid droplets. Therefore, current leakage is likely to occur, and it becomes difficult to secure the electric field strength necessary for charging the droplets.
On the other hand, according to the configuration of (4), by setting the ejection angle of the nozzle to 30 degrees or more and 100 degrees or less, wetting of the counter electrode with droplets can be suppressed, and the electric field strength required for charging the droplets can be reduced. Can be secured.

(5)幾つかの実施形態では、上記(1)乃至(4)の何れかの構成において、前記少なくとも1つのノズルは、液滴径がザウタ平均径で10マイクロメートル以上300マイクロメートル以下となる前記液滴を噴射可能に構成されている。 (5) In some embodiments, in any one of the configurations (1) to (4), the at least one nozzle has a droplet diameter of 10 μm or more and 300 μm or less in terms of Sauter average diameter. The droplets can be ejected.

 発明者らが鋭意検討した結果、液滴径が大きくなると、大気中の微粒子の除去効果が低下する傾向となることが見出されている。
 その点、上記(5)の構成によって、液滴径をザウタ平均径で10マイクロメートル以上300マイクロメートル以下とすることで、大気中の微粒子を液滴で効果的に捕集できる。
As a result of diligent studies by the inventors, it has been found that the effect of removing fine particles in the atmosphere tends to decrease as the droplet size increases.
On the other hand, with the configuration of (5) above, by setting the droplet diameter to 10 μm or more and 300 μm or less in terms of Sauter mean diameter, it is possible to effectively collect fine particles in the atmosphere with the droplets.

(6)幾つかの実施形態では、上記(1)乃至(5)の何れかの構成において、
 前記吹出し部を有し、前記液滴を含む空気を送風するための送風機をさらに備え、
 前記ノズル及び前記電極部は、前記送風機の筐体に取り付けられている。
(6) In some embodiments, in any of the configurations of (1) to (5) above,
And a blower for blowing the air containing the droplets,
The nozzle and the electrode unit are attached to the housing of the blower.

 上記(6)の構成によれば、送風機から送風された空気によって液滴を比較的広い空間に拡散させることができるので、比較的広い空間の除塵を行うことができる。また、上記(6)の構成によれば、ノズル及び電極部を送風機の筐体に取り付けることで、送風機からの送風によって効果的に液滴を拡散させることができる位置にノズル及び電極部を設置することが容易となる。 According to the above configuration (6), the air blown from the blower can diffuse the droplets into a relatively wide space, so that dust can be removed in a relatively wide space. Further, according to the configuration of (6) above, by mounting the nozzle and the electrode portion on the housing of the blower, the nozzle and the electrode portion are installed at positions where the droplets can be effectively diffused by the air blown from the blower. It becomes easy to do.

(7)幾つかの実施形態では、上記(1)乃至(6)の何れかの構成において、
 絶縁材によって構成され、前記電極部を支持する支持部と、
 前記支持部に向かって気体を噴射可能に構成された掃気用ノズルと、
をさらに備える。
(7) In some embodiments, in any of the configurations of (1) to (6) above,
A support portion configured by an insulating material and supporting the electrode portion,
A scavenging nozzle configured to inject a gas toward the support portion,
Is further provided.

 支持部が液滴で濡れてしまうと、対向電極に印加された高電圧の電流が漏洩電流として液滴で濡れた支持部を介して接地側に流れてしまうおそれがある。その点、上記(7)の構成によれば、掃気用ノズルから支持部に向かって気体を噴射することで、液滴が支持部に付着することを抑制して、漏洩電流の発生を抑制できる。 If the supporting part gets wet with the droplet, the high-voltage current applied to the counter electrode may flow as a leakage current to the ground side via the supporting part wet with the droplet. On the other hand, according to the configuration of (7) above, by injecting gas from the scavenging nozzle toward the support portion, it is possible to suppress liquid droplets from adhering to the support portion and suppress the generation of leakage current. .

(8)幾つかの実施形態では、上記(1)乃至(7)の何れかの構成において、
 撥水性の絶縁材によって構成されるか、又は、絶縁材によって構成されていて表面に撥水処理が施されている、前記電極部を支持する支持部をさらに備える。
(8) In some embodiments, in any of the configurations of (1) to (7) above,
It further comprises a support portion configured to be formed of a water-repellent insulating material, or formed of an insulating material and having a surface subjected to a water-repellent treatment, for supporting the electrode portion.

 上述したように、支持部が液滴で濡れてしまうと、対向電極に印加された高電圧の電流が漏洩電流として液滴で濡れた支持部を介して接地側に流れてしまうおそれがある。その点、上記(8)の構成によれば、液滴が支持部に接触しても、その撥水性によって液滴が支持部に付着することを抑制できる。また、液滴が支持部に接触しても、支持部の表面の全体が液体で濡れてしまうことを抑制できる。これにより、漏洩電流の発生を抑制できる。 As described above, if the supporting part gets wet with the liquid droplets, the high-voltage current applied to the counter electrode may flow as a leakage current to the ground side through the supporting part wet with the liquid droplets. On the other hand, according to the configuration of (8), even if the droplet contacts the supporting portion, the water repellency can prevent the droplet from adhering to the supporting portion. Further, even if the droplet contacts the supporting portion, it is possible to prevent the entire surface of the supporting portion from getting wet with the liquid. Thereby, the generation of leakage current can be suppressed.

(9)幾つかの実施形態では、上記(1)乃至(8)の何れかの構成において、
 前記吹出し部を有し、前記液滴を含む空気を送風するための送風機をさらに備え、
 前記ノズルは、前記送風機が送風する空気の流れに関して前記送風機の下流側に複数設けられている。
(9) In some embodiments, in any of the configurations of (1) to (8) above,
And a blower for blowing the air containing the droplets,
A plurality of nozzles are provided on the downstream side of the blower with respect to the flow of air blown by the blower.

 上記(9)の構成によれば、複数のノズルから液滴を噴射することで、送風機からの送風される空気の流れに液滴を均一に付与できる。 According to the above configuration (9), the droplets can be uniformly applied to the flow of air blown from the blower by ejecting the droplets from the plurality of nozzles.

(10)幾つかの実施形態では、上記(1)乃至(9)の何れかの構成において、
 前記吹出し部を有し、前記液滴を含む空気を送風するための送風機と、
 前記送風機からの空気の送風方向を変更可能に構成された方向変更装置と、
をさらに備える。
(10) In some embodiments, in any of the configurations of (1) to (9) above,
An air blower for blowing air containing the droplets, the blower having the blowing portion;
A direction changing device configured to change the blowing direction of air from the blower,
Is further provided.

 上記(10)の構成によれば、方向変更装置によって送風機からの空気の送風方向を変更することで、除塵装置の配置位置を起点とした、液滴を散布する方向を容易に変更できる。 According to the configuration of (10) above, by changing the blowing direction of the air from the blower with the direction changing device, it is possible to easily change the direction in which the droplets are scattered, starting from the arrangement position of the dust removing device.

(11)幾つかの実施形態では、上記(1)乃至(10)の何れかの構成において、
 前記吹出し部を有し、前記液滴を含む空気を送風するための送風機と、
 前記送風機からの空気の送風方向を変更可能に構成された方向変更装置と、
をさらに備え、
 前記方向変更装置は、少なくとも水平方向よりも上側に送風できるように前記送風方向を設定可能に構成されている。
(11) In some embodiments, in any of the configurations of (1) to (10) above,
An air blower for blowing air containing the droplets, the blower having the blowing portion;
A direction changing device configured to change the blowing direction of air from the blower,
Further equipped with,
The direction changing device is configured to be able to set the air blowing direction so that the air can be blown at least above the horizontal direction.

 上記(11)の構成によれば、例えば床面等の低い位置に配置した除塵装置によって、床面よりも上の空間で浮遊する微粒子を捕集することができる。 According to the configuration of (11) above, it is possible to collect fine particles floating in the space above the floor surface by the dust removing device arranged at a low position such as the floor surface.

(12)幾つかの実施形態では、上記(10)又は(11)の構成において、前記方向変更装置は、0度以上の仰角で上側に向かって送風できるように前記送風方向を設定可能に構成されている。 (12) In some embodiments, in the configuration of (10) or (11), the direction changing device is capable of setting the air blowing direction so that air can be blown upward at an elevation angle of 0 degrees or more. Has been done.

 上記(12)の構成によれば、時間の経過とともに落下する液滴を除塵装置から離れた位置に効果的に散布できる。 According to the configuration of (12) above, it is possible to effectively disperse the liquid droplets that drop with the passage of time at a position away from the dust removing device.

(13)幾つかの実施形態では、上記(10)乃至(12)の何れかの構成において、前記方向変更装置は、前記少なくとも1つのノズルからの前記液滴の噴射方向を前記送風機からの空気の送風方向と同じ方向に変更可能に構成されている。 (13) In some embodiments, in the configuration according to any one of the above (10) to (12), the direction changing device sets an ejection direction of the droplet from the at least one nozzle to an air from the blower. It is configured to be changeable in the same direction as the air blowing direction of.

 上記(13)の構成によれば、ノズルからの液滴の噴射方向を送風機からの空気の送風方向と同じ方向に変更できるので、送風機からの送風される空気の流れに液滴を効率よく付与できる。 According to the configuration of (13) above, since the jetting direction of the droplets from the nozzle can be changed to the same blowing direction of the air from the blower, the droplets can be efficiently applied to the flow of air blown from the blower. it can.

 本発明の少なくとも一実施形態によれば、比較的広い空間において空気中に浮遊する微粒子を除去できる。 According to at least one embodiment of the present invention, it is possible to remove fine particles suspended in the air in a relatively large space.

幾つかの実施形態に係る除塵装置の外観を模式的に示した斜視図である。It is a perspective view which showed typically the external appearance of the dust remover concerning some embodiments. 幾つかの実施形態に係る除塵装置を送風機の送風方向の下流側から見た図であり、要部について示している。It is the figure which looked at the dust remover concerning some embodiments from the lower stream side of the blower's ventilation direction, and shows the important section. 幾つかの実施形態に係る除塵装置の側面図であり、要部の構成を模式的に示している。It is a side view of the dust remover concerning some embodiments, and shows the composition of the important section typically. 液滴を帯電させるメカニズムについて説明するための模式的な図である。It is a schematic diagram for explaining a mechanism for charging a droplet. ノズルと対向電極との位置関係を説明するための図である。It is a figure for demonstrating the positional relationship between a nozzle and a counter electrode. 第1距離についてさらに説明するための図である。It is a figure for further explaining the 1st distance. 他の実施形態に係る除塵装置を送風機の送風方向の下流側から見た図であり、要部について示している。It is the figure which looked at the dust remover concerning other embodiments from the lower stream side of the blower's ventilation direction, and shows the important section.

 以下、添付図面を参照して本発明の幾つかの実施形態について説明する。ただし、実施形態として記載されている又は図面に示されている構成部品の寸法、材質、形状、その相対的配置等は、本発明の範囲をこれに限定する趣旨ではなく、単なる説明例にすぎない。
 例えば、「ある方向に」、「ある方向に沿って」、「平行」、「直交」、「中心」、「同心」或いは「同軸」等の相対的或いは絶対的な配置を表す表現は、厳密にそのような配置を表すのみならず、公差、若しくは、同じ機能が得られる程度の角度や距離をもって相対的に変位している状態も表すものとする。
 例えば、「同一」、「等しい」及び「均質」等の物事が等しい状態であることを表す表現は、厳密に等しい状態を表すのみならず、公差、若しくは、同じ機能が得られる程度の差が存在している状態も表すものとする。
 例えば、四角形状や円筒形状等の形状を表す表現は、幾何学的に厳密な意味での四角形状や円筒形状等の形状を表すのみならず、同じ効果が得られる範囲で、凹凸部や面取り部等を含む形状も表すものとする。
 一方、一の構成要素を「備える」、「具える」、「具備する」、「含む」、又は、「有する」という表現は、他の構成要素の存在を除外する排他的な表現ではない。
Hereinafter, some embodiments of the present invention will be described with reference to the accompanying drawings. However, the dimensions, materials, shapes, relative positions, and the like of the components described as the embodiments or shown in the drawings are not intended to limit the scope of the present invention thereto, but are merely illustrative examples. Absent.
For example, expressions that represent relative or absolute arrangements such as “in a certain direction”, “along a certain direction”, “parallel”, “orthogonal”, “center”, “concentric”, or “coaxial” are strict. In addition to representing such an arrangement, it also represents a state in which the components are relatively displaced by a tolerance or an angle or a distance at which the same function can be obtained.
For example, expressions such as "identical", "equal", and "homogeneous" that indicate that they are in the same state are not limited to strict equality, but also include tolerances or differences in the degree to which the same function is obtained. It also represents the existing state.
For example, the representation of a shape such as a quadrangle or a cylindrical shape does not only represent a shape such as a quadrangle or a cylindrical shape in a geometrically strict sense, but also an uneven portion or a chamfer within a range in which the same effect can be obtained. The shape including parts and the like is also shown.
On the other hand, the expressions “comprising”, “comprising”, “comprising”, “including”, or “having” one element are not exclusive expressions excluding the existence of other elements.

 図1は、幾つかの実施形態に係る除塵装置の外観を模式的に示した斜視図である。図2は、幾つかの実施形態に係る除塵装置を後述する送風機の送風方向の下流側から見た図であり、要部について示している。図3は、幾つかの実施形態に係る除塵装置の側面図であり、要部の構成を模式的に示している。 FIG. 1 is a perspective view schematically showing the appearance of a dust remover according to some embodiments. FIG. 2 is a view of a dust removing device according to some embodiments as seen from a downstream side in a blowing direction of a blower described later, and shows a main part. FIG. 3 is a side view of the dust remover according to some embodiments, and schematically shows the configuration of the main part.

 幾つかの実施形態に係る除塵装置1は、送風機10と、ノズル20と、電極部30と、高電圧発生装置40とを備えている。
 幾つかの実施形態に係る送風機10は、後述するノズル20が噴射した液滴2(図3参照)を含む空気を送風するための送風機である。幾つかの実施形態に係る送風機10は、例えば円筒形を有する筐体11の内部に不図示のモータの駆動力によって回転するインペラ12を備えており、インペラ12の回転によって円筒形の筐体11の一方端から空気を吸い込み、図3における矢印Cで示すように図示左方から右方に向かって吸い込んだ空気を送風し、他方端の吹出し部13から排出する。
The dust remover 1 according to some embodiments includes a blower 10, a nozzle 20, an electrode unit 30, and a high voltage generator 40.
A blower 10 according to some embodiments is a blower for blowing air including droplets 2 (see FIG. 3) ejected by a nozzle 20 described later. The blower 10 according to some embodiments includes an impeller 12 that is rotated by a driving force of a motor (not shown) inside a casing 11 having a cylindrical shape, for example, and the cylindrical casing 11 is rotated by the rotation of the impeller 12. Air is sucked in from one end and blown in from the left side to the right side in the drawing as shown by an arrow C in FIG. 3, and is discharged from the blowing section 13 at the other end.

 幾つかの実施形態に係るノズル20は、供給ポンプ29から供給された液体を液滴として噴射可能なノズルであり、一般的に、スプレーノズルとも呼ばれる。幾つかの実施形態では、ノズル20に供給される液体は、例えば水である。
 幾つかの実施形態では、ノズル20は、供給配管22に取り付けられて、送風空気の吹出し部13に配置されている。より具体的には、ノズル20は、送風機10の筐体11の他方端の吹出し部13から送風方向の下流側に離間した位置に配置されている。なお、供給配管22は、配管取付部24によって送風機10の筐体11に取り付けられている。
 幾つかの実施形態では、ノズル20は、複数設けられている。図1、図2に示す例では、ノズル20が8つ設けられているが、ノズル20の数は、1つ以上であればよい。
 幾つかの実施形態では、ノズル20は、送風機10の送風方向の下流側に向かって液滴を噴射する。
The nozzle 20 according to some embodiments is a nozzle capable of ejecting the liquid supplied from the supply pump 29 as droplets, and is generally also called a spray nozzle. In some embodiments, the liquid supplied to the nozzle 20 is water, for example.
In some embodiments, the nozzle 20 is attached to the supply pipe 22 and arranged in the blowout air blower 13. More specifically, the nozzle 20 is arranged at a position separated from the blowout portion 13 at the other end of the housing 11 of the blower 10 on the downstream side in the blowing direction. The supply pipe 22 is attached to the housing 11 of the blower 10 by the pipe attachment portion 24.
In some embodiments, multiple nozzles 20 are provided. In the example shown in FIGS. 1 and 2, eight nozzles 20 are provided, but the number of nozzles 20 may be one or more.
In some embodiments, the nozzle 20 ejects droplets toward the downstream side of the blower 10 in the blowing direction.

 幾つかの実施形態に係るノズル20は、液滴2を円錐状に噴射するように構成されている。
 幾つかの実施形態に係るノズル20は、液滴径がザウタ平均径で10(μm)以上300(μm)以下となる液滴を噴射可能に構成されている。
 また、幾つかの実施形態に係るノズル20の噴射角度θは、30度以上100度以下である。液滴径、及び噴霧角度θについては、後で詳述する。
The nozzle 20 according to some embodiments is configured to eject the droplet 2 in a conical shape.
The nozzle 20 according to some embodiments is configured to be capable of ejecting a droplet having a droplet diameter of 10 (μm) or more and 300 (μm) or less in average Sauter diameter.
Further, the ejection angle θ of the nozzle 20 according to some embodiments is 30 degrees or more and 100 degrees or less. The droplet diameter and the spray angle θ will be described in detail later.

 幾つかの実施形態に係るノズル20は、接地9に接続されている。具体的には、幾つかの実施形態に係るノズル20は、例えば、供給配管22を接地9に接続することで、供給配管22を介して接地9に接続される。なお、ノズル20及び供給配管22は、金属などの導電性の部材によって形成されている。 The nozzle 20 according to some embodiments is connected to the ground 9. Specifically, the nozzle 20 according to some embodiments is connected to the ground 9 via the supply pipe 22, for example, by connecting the supply pipe 22 to the ground 9. The nozzle 20 and the supply pipe 22 are formed of a conductive member such as metal.

 幾つかの実施形態に係る電極部30は、複数の対向電極31と、これら複数の対向電極を支持する電極支持部材35とを含む。幾つかの実施形態に係る対向電極31のそれぞれは、開口33の周囲を囲む形状を有する。幾つかの実施形態に係る対向電極31のそれぞれは、例えば円環形状を有する。なお、対向電極31のそれぞれは、例えば楕円環形状を有していてもよく、開口33の周囲を囲む矩形状等の多角形状を有していてもよい。対向電極31は、それぞれの大きさが同じであってもよく、異なっていてもよい。対向電極31は、それぞれ同じ形状であってもよく、異なる形状であってもよい。
 また、対向電極31のそれぞれは、必ずしも閉じた形状でなくてもよく、例えば、開口33の周囲を少なくとも半周以上囲む形状を有していればよい。
The electrode unit 30 according to some embodiments includes a plurality of counter electrodes 31 and an electrode support member 35 that supports the plurality of counter electrodes. Each of the counter electrodes 31 according to some embodiments has a shape surrounding the periphery of the opening 33. Each of the counter electrodes 31 according to some embodiments has, for example, an annular shape. Each of the counter electrodes 31 may have, for example, an elliptical ring shape, or may have a polygonal shape such as a rectangular shape surrounding the periphery of the opening 33. The counter electrodes 31 may have the same size or different sizes. The counter electrodes 31 may have the same shape or different shapes.
Further, each of the counter electrodes 31 does not necessarily have to have a closed shape, and may have, for example, a shape that surrounds the periphery of the opening 33 for at least a half circumference or more.

 幾つかの実施形態に係る電極部30では、1つのノズル20に対して、1つの対向電極が設けられている。
 幾つかの実施形態に係る電極部30は、複数の対向電極31が電極支持部材35によって支持されている。
 幾つかの実施形態に係る電極部30は、ノズル20が液滴を噴射する方向に対向電極31がノズル20から離間して配置され、絶縁材によって構成された支持部51によって支持されている。具体的には、送風機10の筐体11の他方端に設けられた取付部15に柱状の支持部51の一端が固定され、支持部51の他端に電極部30の電極支持部材35が固定されている。
In the electrode unit 30 according to some embodiments, one counter electrode is provided for one nozzle 20.
In the electrode unit 30 according to some embodiments, a plurality of counter electrodes 31 are supported by an electrode support member 35.
In the electrode unit 30 according to some embodiments, the counter electrode 31 is arranged apart from the nozzle 20 in the direction in which the nozzle 20 ejects droplets, and is supported by the support unit 51 made of an insulating material. Specifically, one end of the columnar support portion 51 is fixed to the mounting portion 15 provided at the other end of the casing 11 of the blower 10, and the electrode support member 35 of the electrode portion 30 is fixed to the other end of the support portion 51. Has been done.

 幾つかの実施形態に係る高電圧発生装置40は、例えば1キロボルト以上の高電圧を発生することができる装置である。幾つかの実施形態に係る高電圧発生装置40は、接地端子42が接地9に接続され、出力端子41に接続された対向電極31(電極部30)に高電圧を印加することができる。 The high voltage generator 40 according to some embodiments is a device capable of generating a high voltage of, for example, 1 kilovolt or more. In the high voltage generator 40 according to some embodiments, the ground terminal 42 is connected to the ground 9, and a high voltage can be applied to the counter electrode 31 (electrode portion 30) connected to the output terminal 41.

 幾つかの実施形態に係る除塵装置1では、送風機10は、図1における矢印Aで示すように、送風機支持部61によって俯仰可能に支持されている。また、幾つかの実施形態に係る除塵装置1では、送風機10は、図1における矢印Bで示すように、旋回装置65によって、中心軸CLを中心として回転可能とされている。すなわち、送風機10は、床面等の旋回装置65の載置面と平行な平面内で回転可能である。
 すなわち、幾つかの実施形態に係る除塵装置1では、送風機からの空気の送風方向を変更可能に構成された方向変更装置60が、送風機支持部61と旋回装置65とを含んでいる。
In the dust remover 1 according to some embodiments, the blower 10 is supported by the blower support portion 61 so as to be able to rise and fall, as indicated by an arrow A in FIG. 1. In the dust remover 1 according to some embodiments, the blower 10 is rotatable about the central axis CL by the turning device 65 as shown by an arrow B in FIG. 1. That is, the blower 10 can rotate in a plane parallel to the mounting surface of the turning device 65, such as the floor.
That is, in the dust removing device 1 according to some embodiments, the direction changing device 60 configured to change the blowing direction of the air from the blower includes the blower support portion 61 and the turning device 65.

 このように構成される幾つかの実施形態に係る除塵装置1では、供給ポンプ29から供給された液体(水)を、複数のノズル20によって液滴として噴霧可能である。そして、幾つかの実施形態に係る除塵装置1では、高電圧発生装置40で発生された高電圧を対向電極31に印加することで、ノズル20から噴霧される液滴2を対向電極31に印加された電圧の極性とは逆の極性に帯電させることができる。
 また、幾つかの実施形態に係る除塵装置1では、例えば体育館や屋内競技場のような比較的広い空間や、屋外において、帯電した液滴2を送風機10からの送風によって周囲に拡散させることができる。
 帯電した液滴2は、空気中の微粉末を静電気力によって捕集することができる。液滴2に捕集された微粉末は、液滴2と共に地上に落下する。これにより、例えば体育館や屋内競技場のような比較的広い空間や、屋外において、大気中の微粒子を帯電させた液滴2で効率的に捕集して除去できる。
In the dust remover 1 according to some embodiments configured as described above, the liquid (water) supplied from the supply pump 29 can be sprayed as droplets by the plurality of nozzles 20. Then, in the dust removing device 1 according to some embodiments, by applying the high voltage generated by the high voltage generating device 40 to the counter electrode 31, the droplet 2 sprayed from the nozzle 20 is applied to the counter electrode 31. It can be charged to the opposite polarity of the applied voltage.
Further, in the dust removing device 1 according to some embodiments, it is possible to diffuse the charged droplets 2 to the surroundings by blowing air from the blower 10 in a relatively large space such as a gymnasium or an indoor stadium or outdoors. it can.
The charged droplets 2 can collect fine powder in the air by electrostatic force. The fine powder collected in the droplet 2 falls on the ground together with the droplet 2. Thus, for example, in a relatively large space such as a gymnasium or an indoor arena, or outdoors, fine particles in the atmosphere can be efficiently collected and removed by the charged droplets 2.

(液滴2の帯電メカニズムについて)
 ここで、幾つかの実施形態に係る除塵装置1において、液滴2を帯電させるメカニズムについて説明する。図4は、液滴2を帯電させるメカニズムについて説明するための模式的な図である。
 対向電極31に高電圧発生装置40からの高電圧が印加されると、対向電極31と、接地9に接続されているノズル20との電位差によって形成される電界によって、ノズル20から噴射される液滴2が誘電分極する。
 例えば、対向電極31に高電圧発生装置40からの負の高電圧が印加されると、ノズル20から噴射される直前の液滴2では、対向電極31に近い領域が正に帯電し、対向電極31から遠い領域が負に帯電する。対向電極31から遠い領域で誘起された分極電荷は、導電性のノズル20及び供給配管22を介してアース(接地9)に流れる。
 これにより、ノズル20から噴射された液滴2は、正に帯電する。
 このように、幾つかの実施形態に係る除塵装置1では、誘電分極によって、ノズル20から噴霧される液滴2を対向電極31に印加された電圧の極性とは逆の極性に帯電させることができる。
(Regarding the charging mechanism of the droplet 2)
Here, the mechanism of charging the droplet 2 in the dust removing device 1 according to some embodiments will be described. FIG. 4 is a schematic diagram for explaining the mechanism of charging the droplet 2.
When a high voltage from the high voltage generator 40 is applied to the counter electrode 31, the liquid ejected from the nozzle 20 is generated by the electric field formed by the potential difference between the counter electrode 31 and the nozzle 20 connected to the ground 9. The drop 2 is dielectrically polarized.
For example, when a negative high voltage is applied to the counter electrode 31 from the high voltage generator 40, in the droplet 2 immediately before being ejected from the nozzle 20, a region near the counter electrode 31 is positively charged, and the counter electrode 31 is charged. Areas far from 31 are negatively charged. The polarization charge induced in the region far from the counter electrode 31 flows to the ground (ground 9) through the conductive nozzle 20 and the supply pipe 22.
As a result, the droplet 2 ejected from the nozzle 20 is positively charged.
As described above, in the dust remover 1 according to some embodiments, it is possible to charge the droplet 2 sprayed from the nozzle 20 to a polarity opposite to the polarity of the voltage applied to the counter electrode 31 by dielectric polarization. it can.

(液滴2の発生量について)
 例えば静電霧化によって液体から微細な液滴を生成する場合、その原理上、比較的多量の液滴を発生させることが困難である。そのため、例えば静電霧化によって液体から微細な液滴を生成する場合には、例えば体育館や屋内競技場のような比較的広い空間や、屋外において大気中の微粒子を帯電させた液滴で効率的に捕集して除去することが困難である。その点、幾つかの実施形態では、ノズル20によって比較的多量の液滴2を生成できる。
(Regarding amount of generated droplet 2)
For example, when minute droplets are generated from a liquid by electrostatic atomization, it is difficult to generate a relatively large number of droplets in principle. Therefore, for example, in the case of producing fine droplets from a liquid by electrostatic atomization, for example, in a relatively large space such as a gymnasium or an indoor stadium, or outdoors, droplets obtained by charging fine particles in the atmosphere can be efficiently used. Difficult to collect and remove. In that regard, in some embodiments, a relatively large amount of droplets 2 can be produced by the nozzle 20.

 したがって、幾つかの実施形態に係る除塵装置1では、ノズル20と、電極部30と、高電圧発生装置40とを備えるので、ノズル20によって生成された比較的多量の液滴2を、誘電分極によって帯電させることができる。
 幾つかの実施形態に係る除塵装置1では、誘電分極によって液滴2を帯電させるという原理から、液滴2を帯電させるために対向電極31に電流を流す必要はない。
 したがって、幾つかの実施形態に係る除塵装置1では、高電圧発生装置40から全ての対向電極31へ流れる電流の合計値は、ノズル20と対向電極31との間で漏洩電流が流れていない場合に、例えば0.1(mA)未満に抑制することも可能である。
Therefore, since the dust remover 1 according to some embodiments includes the nozzle 20, the electrode unit 30, and the high-voltage generator 40, a relatively large amount of the droplet 2 generated by the nozzle 20 is subjected to dielectric polarization. Can be charged by.
In the dust remover 1 according to some embodiments, it is not necessary to apply a current to the counter electrode 31 to charge the droplet 2 because of the principle of charging the droplet 2 by dielectric polarization.
Therefore, in the dust remover 1 according to some embodiments, the total value of the currents flowing from the high voltage generator 40 to all the counter electrodes 31 is the same as when the leakage current does not flow between the nozzle 20 and the counter electrode 31. In addition, it is possible to suppress it to less than 0.1 (mA), for example.

 また、幾つかの実施形態に係る除塵装置1では、誘電分極によって液滴2を帯電させるという原理から、液滴2の噴射量を増やしても、液滴1つあたりの誘電分極による電荷量は減らない。
 したがって、幾つかの実施形態に係る除塵装置1によれば、出力電力が比較的小さい高電圧発生装置40によって、大気中の微粒子を捕集するのに効果的な電荷量で比較的多量の液滴2を帯電させることができる。これにより、例えば体育館や屋内競技場のような比較的広い空間や、屋外において大気中の微粒子を帯電させた液滴2で効率的に捕集して除去できる。
 また、幾つかの実施形態に係る除塵装置1によれば、上述したように、液滴2を帯電させるために対向電極31に電流を流す必要はないので、大出力の高電圧発生装置40が不要であり、高電圧発生装置40のコストを抑制できる。
In addition, in the dust remover 1 according to some embodiments, even if the injection amount of the droplet 2 is increased, the charge amount due to the dielectric polarization per droplet does not change from the principle of charging the droplet 2 by dielectric polarization. It does not decrease.
Therefore, according to the dust remover 1 according to some embodiments, the high voltage generator 40 having a relatively low output power causes a relatively large amount of liquid with an effective charge amount for collecting fine particles in the atmosphere. The drop 2 can be charged. As a result, the particles 2 in the atmosphere can be efficiently collected and removed by the charged droplets 2 in a relatively large space such as a gymnasium or an indoor stadium or outdoors.
Further, according to the dust remover 1 according to some embodiments, as described above, since it is not necessary to pass a current through the counter electrode 31 to charge the droplet 2, the high-voltage high-voltage generator 40 has a large output. It is unnecessary, and the cost of the high voltage generator 40 can be suppressed.

 すなわち、上述したように、幾つかの実施形態に係る除塵装置1では、原理上、液滴2を帯電させるために対向電極31に電流を流す必要はない。したがって、ノズル20と対向電極31との間で漏洩電流が流れないように対向電極31(電極部30)の絶縁を確保することで、高電圧発生装置40から対向電極31へ流れる電流がほとんど発生しないようにすることができる。これにより、高電圧発生装置40の定格出力を下げることができ、高電圧発生装置40のコストをさらに抑制できる。 That is, as described above, in the dust removers 1 according to some embodiments, in principle, it is not necessary to apply a current to the counter electrode 31 to charge the droplet 2. Therefore, by ensuring the insulation of the counter electrode 31 (electrode portion 30) so that the leakage current does not flow between the nozzle 20 and the counter electrode 31, almost all the current flowing from the high voltage generator 40 to the counter electrode 31 is generated. You can choose not to. Thereby, the rated output of the high voltage generator 40 can be reduced, and the cost of the high voltage generator 40 can be further suppressed.

 図5は、ノズル20と対向電極31との位置関係を説明するための図である。以下、ノズル20と対向電極31との位置関係について説明する。
 幾つかの実施形態に係る除塵装置1では、上述したように、ノズル20は、液滴2を円錐状に噴射するように構成されている。そこで、ノズル20から噴射された液滴2が対向電極31に直接接触することを抑制するため、幾つかの実施形態に係る除塵装置1では、ノズル20と対向電極31との位置関係は、以下で説明する式(1)を満たす。
FIG. 5 is a diagram for explaining the positional relationship between the nozzle 20 and the counter electrode 31. Hereinafter, the positional relationship between the nozzle 20 and the counter electrode 31 will be described.
In the dust remover 1 according to some embodiments, as described above, the nozzle 20 is configured to eject the droplet 2 in a conical shape. Therefore, in order to prevent the liquid droplets 2 ejected from the nozzle 20 from directly contacting the counter electrode 31, in the dust removers 1 according to some embodiments, the positional relationship between the nozzle 20 and the counter electrode 31 is as follows. The formula (1) described in (3) is satisfied.

 すなわち、ノズル20における液滴2の噴射位置、すなわちノズル20の先端20aから対向電極31を含む平面と前記円錐の中心線との交点C1までの第1距離L1をr(ミリメートル)とし、交点C1と対向電極31との最小距離である第2距離L2をa(ミリメートル)とし、ノズル20が液滴2を噴射する噴射角度をθ(度)とすると、ノズル20と対向電極31との位置関係は、次式(1)で表される。
  r<a/tan(θ/2)・・・(1)
That is, the first distance L1 from the tip 20a of the nozzle 20, that is, the intersection C1 of the plane including the counter electrode 31 and the center line of the cone from the tip 20a of the nozzle 20 to r1 (millimeter), the intersection C1 The second distance L2, which is the minimum distance between the counter electrode 31 and the counter electrode 31, is a 0 (millimeter), and the ejection angle at which the nozzle 20 ejects the droplet 2 is θ (degrees). The relationship is expressed by the following equation (1).
r <a 0 / tan (θ / 2) (1)

 上記の式(1)を満たす場合には、対向電極31が囲む開口33において、ノズル20から円錐状に噴射される液滴2を、対向電極31よりも内側の領域を通過させることができる。これにより、対向電極31が液滴2で濡れてしまうことを抑制でき、ノズル20と対向電極31との間で漏洩電流が流れることを抑制できる。 When the above formula (1) is satisfied, the droplet 2 that is conically ejected from the nozzle 20 can pass through the region inside the counter electrode 31 in the opening 33 surrounded by the counter electrode 31. As a result, it is possible to prevent the counter electrode 31 from getting wet with the liquid droplet 2, and it is possible to prevent a leakage current from flowing between the nozzle 20 and the counter electrode 31.

 なお、ノズル20の噴射角度は、上述したように、30度以上100度以下であるとよい。
 すなわち、噴霧角度が大きくなると、対向電極31が液滴2で濡れ易くなってしまう。そのため、電流の漏洩が起こり易くなり、液滴の帯電に必要な電界強度の確保が難しくなってしまう。
 そこで、ノズル20の噴射角度を30度以上100度以下とすることで、対向電極31が液滴2で濡れることを抑制でき、液滴の帯電に必要な電界強度を確保できる。
The ejection angle of the nozzle 20 is preferably 30 degrees or more and 100 degrees or less, as described above.
That is, when the spray angle is large, the counter electrode 31 is likely to be wet with the droplet 2. Therefore, current leakage is likely to occur, and it becomes difficult to secure the electric field strength necessary for charging the droplets.
Therefore, by setting the ejection angle of the nozzle 20 to 30 degrees or more and 100 degrees or less, it is possible to prevent the counter electrode 31 from getting wet with the droplet 2 and to secure the electric field strength necessary for charging the droplet.

 なお、例えば、筐体11の内径が300(mm)程度であり、ノズル20を8個程度設ける場合には、交点C1と対向電極31との最小距離である第2距離L2を5(mm)以上50(mm)以下とするとよい。また、この場合には、ノズル20の先端20aから交点C1までの第1距離L1は、5(mm)以上200(mm)以下とするとよい。なお、対向電極31が円環形状を有している場合、第2距離L2は、対向電極31の内半径となる。 Note that, for example, when the housing 11 has an inner diameter of about 300 (mm) and about eight nozzles 20 are provided, the second distance L2, which is the minimum distance between the intersection C1 and the counter electrode 31, is 5 (mm). It is better to be 50 (mm) or less. In this case, the first distance L1 from the tip 20a of the nozzle 20 to the intersection C1 is preferably 5 (mm) or more and 200 (mm) or less. When the counter electrode 31 has an annular shape, the second distance L2 is the inner radius of the counter electrode 31.

(第1距離L1について)
 図6は、第1距離L1についてさらに説明するための図である。
 液滴2に誘起される分極電荷量が多いほど、液滴による大気中の微粉末の捕集効率が上がる。そのため、対向電極31に印加する電圧に対してノズル20の出口近傍(先端20a)に形成される電界強度ができるだけ大きくなるようにノズル20と対向電極31との位置関係を決めるのが良い。
(About the first distance L1)
FIG. 6 is a diagram for further explaining the first distance L1.
The greater the amount of polarization charge induced in the droplet 2, the more efficiently the droplet collects fine powder in the atmosphere. Therefore, it is preferable to determine the positional relationship between the nozzle 20 and the counter electrode 31 so that the electric field strength formed in the vicinity of the outlet (tip 20a) of the nozzle 20 with respect to the voltage applied to the counter electrode 31 is as large as possible.

 ノズル20の先端20aに形成される電界強度は概ね次式(2)で表され、対向電極31の内半径と外半径が決まると電界強度が極大値となるノズル20と対向電極31との垂直距離(第1距離L1)が決まる。
 E=-r/(a-a
  ×{1/(a+r0.5-1/(a +r0.5}×V・・・(2)
 ここで、aは対向電極31の外半径L3(m)であり、aは上述したように対向電極31の内半径L2(m)である。rは上述したようにノズル20の先端20aから交点C1までの第1距離L1(m)である。Vは対向電極への印加電圧(V)である。Eはノズル20の先端20aの電界強度(V/m)である。
The electric field strength formed at the tip 20a of the nozzle 20 is generally expressed by the following equation (2), and when the inner radius and the outer radius of the counter electrode 31 are determined, the electric field strength becomes a maximum value. The distance (first distance L1) is determined.
E = −r / (a−a 0 )
× {1 / (a 2 + r 2 ) 0.5 −1 / (a 0 2 + r 2 ) 0.5 } × V 0 (2)
Here, a is the outer radius L3 (m) of the counter electrode 31, and a 0 is the inner radius L2 (m) of the counter electrode 31 as described above. r is the first distance L1 (m) from the tip 20a of the nozzle 20 to the intersection C1 as described above. V 0 is a voltage (V) applied to the counter electrode. E is the electric field intensity (V / m) at the tip 20a of the nozzle 20.

 したがって、上記の式(2)に基づいて、5(mm)以上200(mm)以下の範囲内で電界強度Eができるだけ極大値に近くなるように第1距離L1を決めるのが良い。なお、印加電圧Vは、5(kV)以上80(kV)以下とするとよい。 Therefore, it is preferable to determine the first distance L1 so that the electric field strength E is as close to the maximum value as possible within the range of 5 (mm) or more and 200 (mm) or less based on the above equation (2). The applied voltage V 0 is preferably 5 (kV) or more and 80 (kV) or less.

 幾つかの実施形態に係る除塵装置1では、第1距離L1及び第2距離L2を上記範囲内に設定することで、対向電極31に印加された高電圧によってノズル20における液滴の噴射位置、すなわちノズル20の先端20aにおいて形成される電界の強度を十分に高めることができる。
 なお、第1距離L1が例えば電極部30の絶縁構造などとの関係で上記範囲内に入らない場合は、対向電極31の内半径や外半径を調整して、電界強度Eが、第1距離L1に対して極大になるようにするとよい。
In the dust remover 1 according to some embodiments, by setting the first distance L1 and the second distance L2 within the above range, the droplet ejection position in the nozzle 20 by the high voltage applied to the counter electrode 31, That is, the strength of the electric field formed at the tip 20a of the nozzle 20 can be sufficiently increased.
If the first distance L1 does not fall within the above range due to, for example, the insulating structure of the electrode portion 30, the inner radius and the outer radius of the counter electrode 31 are adjusted so that the electric field strength E becomes equal to the first distance. It is good to make it maximum with respect to L1.

(液滴径について)
 幾つかの実施形態に係るノズル20は、上述したように、液滴径がザウタ平均径で10(μm)以上300(μm)以下となる液滴を噴射可能に構成されている。
 発明者らが鋭意検討した結果、液滴径が大きくなると、大気中の微粒子の除去効果が低下する傾向となることが見出されている。また、液滴径が小さ過ぎると、液滴2が地上に到達する前に液滴2が蒸発してしまう。液滴2で捕集した微粒子が水に不溶の固体であれば、液滴2が地上に到達する前に液滴2が蒸発してしまうと、微粒子が再び大気中に拡散することとなってしまう。
 その点、幾つかの実施形態では、ノズル20から噴射される液滴2の液滴径をザウタ平均径で10(μm)以上300(μm)以下とすることで、大気中の微粒子を液滴で効果的に捕集できる。
(About droplet size)
As described above, the nozzle 20 according to some embodiments is configured to be capable of ejecting a liquid droplet having a Sauter mean diameter of 10 (μm) or more and 300 (μm) or less.
As a result of diligent studies by the inventors, it has been found that the effect of removing fine particles in the atmosphere tends to decrease as the droplet size increases. If the droplet diameter is too small, the droplet 2 will evaporate before the droplet 2 reaches the ground. If the fine particles collected by the droplet 2 are a solid insoluble in water, if the droplet 2 evaporates before the droplet 2 reaches the ground, the fine particles will diffuse into the atmosphere again. I will end up.
On the other hand, in some embodiments, by setting the droplet diameter of the droplet 2 ejected from the nozzle 20 to be not less than 10 (μm) and not more than 300 (μm) in terms of Sauter average diameter, the fine particles in the atmosphere are droplets. Can be effectively collected.

 幾つかの実施形態に係る除塵装置1では、送風機10を備えているので、送風機10から送風された空気によって液滴2を比較的広い空間に拡散させることができるので、比較的広い空間の除塵を行うことができる。
 また、幾つかの実施形態に係る除塵装置1では、ノズル20及び電極部30が送風機10の筐体11に取り付けられているので、送風機10からの送風によって効果的に液滴2を拡散させることができる位置にノズル20及び電極部30を設置することが容易となる。
Since the dust remover 1 according to some embodiments includes the blower 10, the droplets 2 can be diffused into a relatively wide space by the air blown from the blower 10, so that the dust in the relatively wide space is removed. It can be performed.
Further, in the dust remover 1 according to some embodiments, since the nozzle 20 and the electrode unit 30 are attached to the housing 11 of the blower 10, it is possible to effectively diffuse the droplets 2 by blowing air from the blower 10. It becomes easy to install the nozzle 20 and the electrode part 30 at a position where the above can be achieved.

 図7は、他の実施形態に係る除塵装置を送風機の送風方向の下流側から見た図であり、要部について示している。他の実施形態に係る除塵装置1では、上述した幾つかの実施形態に係る除塵装置1に対して、さらに掃気用ノズル71が設けられている。掃気用ノズル71は、電極部30を支持する支持部51に向かって気体を噴射可能に構成されたノズルである。図7に示した他の実施形態に係る除塵装置1では、掃気用ノズル71は、支持部51に対して、筐体11の径方向外側に配置されており、矢印bで示すように、筐体11の径方向外側から内側に向かって気体を噴出することができる。図7に示した他の実施形態に係る除塵装置1では、1つの支持部51に対して掃気用ノズル71が2つ配置されているが、少なくとも1つの掃気用ノズル71が配置されていればよい。 FIG. 7 is a view of a dust removing device according to another embodiment as viewed from the downstream side of the blower in the blowing direction, and shows the main part. In the dust remover 1 according to another embodiment, a scavenging nozzle 71 is further provided in addition to the dust removers 1 according to some of the above-described embodiments. The scavenging nozzle 71 is a nozzle configured to be able to inject gas toward the support portion 51 that supports the electrode portion 30. In the dust removing device 1 according to another embodiment shown in FIG. 7, the scavenging nozzle 71 is arranged on the outer side in the radial direction of the housing 11 with respect to the support portion 51, and as shown by an arrow b, the housing is shown. Gas can be ejected from the outside of the body 11 in the radial direction toward the inside. In the dust remover 1 according to another embodiment shown in FIG. 7, two scavenging nozzles 71 are arranged for one support portion 51, but if at least one scavenging nozzle 71 is arranged. Good.

 支持部51が液滴2で濡れてしまうと、対向電極31に印加された高電圧の電流が漏洩電流として液滴2で濡れた支持部51及び送風機10の筐体11を介して接地側に流れてしまうおそれがある。その点、図7に示した他の実施形態に係る除塵装置1によれば、掃気用ノズル71から支持部51に向かって気体を噴射することで、液滴2が支持部51に付着することを抑制して、漏洩電流の発生を抑制できる。
 なお、掃気用ノズル71は、全ての支持部51に対して設けてもよいし、送風機10の採り得る姿勢のうち、最も使用頻度が高い姿勢において濡れ易い支持部51に対してだけ設けてもよい。
When the support portion 51 gets wet with the droplet 2, the high-voltage current applied to the counter electrode 31 is leaked to the ground side via the support portion 51 wet with the droplet 2 and the housing 11 of the blower 10. It may flow. In that respect, according to the dust removing device 1 according to another embodiment shown in FIG. 7, the droplet 2 is attached to the support portion 51 by injecting gas from the scavenging nozzle 71 toward the support portion 51. It is possible to suppress the occurrence of leakage current.
Note that the scavenging nozzle 71 may be provided for all of the supporting portions 51, or may be provided only for the supporting portion 51 that is easily wetted in the most frequently used postures among the postures of the blower 10. Good.

 なお、図2及び図7に示した幾つかの実施形態において、支持部51は、撥水性の絶縁材によって構成されるか、又は、絶縁材によって構成されていて表面に撥水処理が施されているとよい。これにより、液滴2が支持部51に接触しても、その撥水性によって液滴2が支持部51に付着することを抑制できる。また、液滴2が支持部51に接触しても、支持部51の表面の全体が液体で濡れてしまうことを抑制できる。これにより、漏洩電流の発生を抑制できる。 In some of the embodiments shown in FIGS. 2 and 7, the support portion 51 is made of a water-repellent insulating material, or is made of an insulating material and the surface thereof is subjected to a water-repellent treatment. It is good to have Accordingly, even if the droplet 2 comes into contact with the support portion 51, it is possible to suppress the droplet 2 from adhering to the support portion 51 due to its water repellency. Further, even if the droplet 2 comes into contact with the support portion 51, it is possible to prevent the entire surface of the support portion 51 from getting wet with the liquid. Thereby, the generation of leakage current can be suppressed.

 幾つかの実施形態に係る除塵装置1では、ノズル20は、送風機10が送風する空気の流れに関して送風機の下流側に複数設けられている。
 これにより、複数のノズル20から液滴2を噴射することで、送風機10からの送風される空気の流れに液滴2を均一に付与できる。
 ここで、送風機10の吹出し部13から吹き出される送風空気の流速は、発明者らが鋭意検討した結果、5(m/sec)以上であるとよいことが分かった。なお、ノズル20からの液滴2の噴射速度がおおよそ5(m/sec)から10(m/sec)程度となるため、吹出し部13から吹き出される送風空気の流速は、ノズル20からの液滴2の噴射速度の0.5倍以上であるとよい。
In the dust remover 1 according to some embodiments, a plurality of nozzles 20 are provided on the downstream side of the blower with respect to the flow of air blown by the blower 10.
Accordingly, by ejecting the droplets 2 from the plurality of nozzles 20, the droplets 2 can be uniformly applied to the flow of air blown from the blower 10.
Here, as a result of intensive studies by the inventors, it has been found that the flow velocity of the blown air blown out from the blowout portion 13 of the blower 10 is preferably 5 (m / sec) or more. Since the ejection speed of the droplet 2 from the nozzle 20 is approximately 5 (m / sec) to 10 (m / sec), the flow velocity of the blown air blown out from the blowing portion 13 is equal to that of the liquid ejected from the nozzle 20. The ejection speed of the droplet 2 is preferably 0.5 times or more.

 幾つかの実施形態に係る除塵装置1では、送風機からの空気の送風方向を変更可能に構成された方向変更装置60を備えている。
 したがって、方向変更装置60によって送風機10からの空気の送風方向を変更することで、除塵装置1の配置位置を起点とした、液滴2を散布する方向を容易に変更できる。
The dust remover 1 according to some embodiments includes a direction changing device 60 configured to change the blowing direction of air from the blower.
Therefore, by changing the blowing direction of the air from the blower 10 by the direction changing device 60, it is possible to easily change the direction in which the droplets 2 are scattered, with the arrangement position of the dust removing device 1 as the starting point.

 幾つかの実施形態に係る除塵装置1において、方向変更装置60は、少なくとも水平方向よりも上側に送風できるように送風方向を設定可能に構成されているとよい。
 これにより、例えば床面等の低い位置に配置した除塵装置1によって、床面よりも上の空間で浮遊する微粒子を捕集することができる。
In the dust removing device 1 according to some embodiments, the direction changing device 60 may be configured to be able to set the air blowing direction so that the air can be blown at least above the horizontal direction.
Thereby, for example, the dust removing device 1 arranged at a low position on the floor or the like can collect fine particles floating in the space above the floor.

 幾つかの実施形態に係る除塵装置1において、方向変更装置60は、0度以上の仰角、より好ましくは、例えば30度以上の仰角で上側に向かって送風できるように送風方向を設定可能に構成されているとよい。
 これにより、時間の経過とともに落下する液滴2を除塵装置1から離れた位置に効果的に散布できる。
In the dust remover 1 according to some embodiments, the direction changing device 60 is configured to be able to set the air blowing direction so that the air can be blown upward at an elevation angle of 0 degrees or more, more preferably, an elevation angle of 30 degrees or more. It is good to have been.
This makes it possible to effectively disperse the droplets 2 that drop with the passage of time at a position away from the dust removing device 1.

 幾つかの実施形態に係る除塵装置1では、方向変更装置60は、ノズル20からの液滴2の噴射方向を送風機10からの空気の送風方向と同じ方向に変更可能に構成されている。すなわち、幾つかの実施形態に係る除塵装置1では、複数のノズル20が供給配管22及び配管取付部24を介して送風機10の筐体11に取り付けられている。そして、幾つかの実施形態に係る除塵装置1では、方向変更装置60が、送風機10の筐体11の姿勢を変更可能としている。
 したがって、ノズル20からの液滴2の噴射方向を送風機10からの空気の送風方向と同じ方向に変更できるので、送風機10からの送風される空気の流れに液滴2を効率よく付与できる。
In the dust removing device 1 according to some embodiments, the direction changing device 60 is configured to be able to change the ejection direction of the droplet 2 from the nozzle 20 to the same direction as the blowing direction of the air from the blower 10. That is, in the dust remover 1 according to some embodiments, the plurality of nozzles 20 are attached to the housing 11 of the blower 10 via the supply pipe 22 and the pipe attachment portion 24. In the dust removing device 1 according to some embodiments, the direction changing device 60 can change the posture of the housing 11 of the blower 10.
Therefore, the jetting direction of the droplet 2 from the nozzle 20 can be changed to the same blowing direction of the air from the blower 10, so that the droplet 2 can be efficiently applied to the flow of air blown from the blower 10.

(ノズル20と接地9との間に流れる電流の値について)
 なお、上述したように、幾つかの実施形態に係る除塵装置1では、誘電分極によって液滴2を帯電させるという原理から、液滴2を帯電させるために対向電極31に電流を流す必要はないが、ノズル20から噴射される直前の液滴2において対向電極31から遠い領域で誘起された分極電荷は、導電性のノズル20及び供給配管22を介してアース(接地9)に流れる。このように、ノズル20と接地9との間に流れる電流の値は、例えば、以下のようになる。
(About the value of the current flowing between the nozzle 20 and the ground 9)
As described above, in the dust removing devices 1 according to some embodiments, it is not necessary to apply a current to the counter electrode 31 in order to charge the droplet 2 because of the principle that the droplet 2 is charged by dielectric polarization. However, the polarization charge induced in the region far from the counter electrode 31 in the droplet 2 immediately before being ejected from the nozzle 20 flows to the ground (ground 9) via the conductive nozzle 20 and the supply pipe 22. Thus, the value of the current flowing between the nozzle 20 and the ground 9 is as follows, for example.

 なお、幾つかの実施形態に係る除塵装置1では、発明者らが鋭意検討した結果、以下の各パラメータに関し、その数値範囲が以下の範囲であるとよいことが分かった。
(a)液体の噴霧量は、微粒子を除去する領域1(m)あたり0.01(l/min)以上とするとよい。
(b)ノズル20の先端20aに形成される電界強度は、0.5(kV/cm)以上10(kV/cm)以下とするとよい。
(c)上述したように、液滴2の液滴径は、ザウタ平均径で10(μm)以上300(μm)以下とするとよい。
In addition, in the dust remover 1 according to some of the embodiments, as a result of intensive studies by the inventors, it was found that the numerical ranges of the following parameters should be within the following ranges.
(A) The spray amount of the liquid may be 0.01 (l / min) or more per region 1 (m 3 ) where the fine particles are removed.
(B) The electric field strength formed at the tip 20a of the nozzle 20 is preferably 0.5 (kV / cm) or more and 10 (kV / cm) or less.
(C) As described above, the droplet diameter of the droplet 2 is preferably 10 (μm) or more and 300 (μm) or less in terms of Sauter average diameter.

 上記の範囲を参照して、下記条件におけるノズル20と接地9との間に流れる電流の値の一例を試算する。なお、以下の1)~3)に挙げたパラメータの値は、ノズル20と接地9との間に流れる電流の値を算出するために適宜採用した値であり、本発明における各パラメータの値は、以下の各値に限定されることはない。
1)液体(水)の噴霧量:9(l/min)
2)ノズル20の先端20aに形成される電界強度:4.7(kV/cm)=4.7×10(V/m)
3)液滴径:80(μm)
4)水の比誘電率:75
5)水の密度:1000(kg/m
An example of the value of the current flowing between the nozzle 20 and the ground 9 under the following conditions will be calculated with reference to the above range. It should be noted that the values of the parameters listed in 1) to 3) below are values appropriately adopted to calculate the value of the current flowing between the nozzle 20 and the ground 9, and the values of the respective parameters in the present invention are , And is not limited to the following values.
1) Amount of liquid (water) sprayed: 9 (l / min)
2) Electric field intensity formed at the tip 20a of the nozzle 20: 4.7 (kV / cm) = 4.7 × 10 5 (V / m)
3) Droplet diameter: 80 (μm)
4) relative permittivity of water: 75
5) Water density: 1000 (kg / m 3 ).

 ノズル20と対向電極31との間で漏洩電流が流れていない場合には、ノズル20と接地9との間に流れる電流の値は、液滴2によって運ばれる単位時間あたりの電荷の量と等しい。そこで、以下のようにして、液滴2によって運ばれる単位時間あたりの電荷の量を求める。
 まず、単位時間あたりに噴霧される液滴2の個数Npは、次式(3)で求めることができる。
  Np=9/{4/3×π×(40×10-6×1000}
    =3.36×1010(個/min)    ・・・(3)
When no leakage current flows between the nozzle 20 and the counter electrode 31, the value of the current flowing between the nozzle 20 and the ground 9 is equal to the amount of charge carried by the droplet 2 per unit time. . Therefore, the amount of electric charge carried by the droplet 2 per unit time is obtained as follows.
First, the number Np of droplets 2 sprayed per unit time can be calculated by the following equation (3).
Np = 9 / {4/3 × π × (40 × 10 −6 ) 3 × 1000}
= 3.36 × 10 10 (pieces / min) (3)

 1個の液滴2が持つ電荷量Qpは、単位面積あたりの分極電荷量qと水滴の表面積sとの積(Qp=q×s)である。
 なお、液滴2を球と仮定したときの単位面積あたりの分極電荷量qは、次式(4)で表される。
   q=3×ε×E×(ε-1)/(ε+2)   ・・・(4)
 ここで、εは、真空の誘電率であり、ε=8.854×10-12(F/m)である。εは、液滴2(水)の比誘電率であり、上述したように、ε=75である。また、上述したように、Eは、ノズル20の先端20aに形成される電界強度であり、E=4.7×10(V/m)である。
 したがって、1個の液滴2が持つ電荷量Qpは、単位面積あたりの分極電荷量qと1個の液滴2の表面積sとの積であり、次式(5)のとおりとなる。
   Qp=q×s
     =3×ε×E×(ε-1)/(ε+2)×s
     =3×8.854×10-12×4.7×10
       ×(75-1)/(75+2)×4×π×(40×10-6
     =2.41×10-13(C)   ・・・(5)
The charge amount Qp possessed by one droplet 2 is the product of the polarization charge amount q per unit area and the surface area s of the water droplet (Qp = q × s).
The polarization charge amount q per unit area when the droplet 2 is assumed to be a sphere is expressed by the following equation (4).
q = 3 × ε 0 × E × (ε s −1) / (ε s +2) (4)
Here, ε 0 is the dielectric constant in vacuum, and ε 0 = 8.854 × 10 −12 (F / m). ε s is the relative permittivity of the droplet 2 (water), and as described above, ε s = 75. Further, as described above, E is the electric field strength formed at the tip 20a of the nozzle 20, and E = 4.7 × 10 5 (V / m).
Therefore, the charge amount Qp of one droplet 2 is the product of the polarization charge amount q per unit area and the surface area s of one droplet 2, and is given by the following equation (5).
Qp = q × s
= 3 × ε 0 × E × (ε s −1) / (ε s +2) × s
= 3 × 8.854 × 10 −12 × 4.7 × 10 5
× (75-1) / (75 + 2) × 4 × π × (40 × 10 −6 ) 2
= 2.41 × 10 −13 (C) (5)

 よって、単位時間あたりに噴霧される液滴2が持つ電荷量(Np×Qp)は、次式(6)のとおりとなる。
    Np×Qp=8.11×10-3(C/min)
         =1.35×10-4(C/sec)
         =0.135(mA)   ・・・(6)
Therefore, the amount of charge (Np × Qp) that the droplet 2 sprayed per unit time has is given by the following equation (6).
Np × Qp = 8.11 × 10 −3 (C / min)
= 1.35 × 10 -4 (C / sec)
= 0.135 (mA) (6)

 この電荷量(Np×Qp)は、噴霧量が9(l/min)の場合の値であるので、噴霧量1(l/min)あたりに換算すると0.015(mA)となる。 Since this charge amount (Np × Qp) is a value when the spray amount is 9 (l / min), it is 0.015 (mA) when converted per spray amount 1 (l / min).

 なお、この電流の値(0.015(mA))は、噴霧量1(l/min)で噴霧される液滴2によって運ばれる電荷量を電流として表したものである。また、液滴2は、送風機10から送風される送風空気によって大気中に拡散されるので、上述のようにして算出した電流値を送風機10の吹出し部13の開口面積で除すことで、送風機10の吹出し部13における液滴2を含んだ送風空気の見かけ上の電流密度を求めることができる。
 ここで、送風機10の吹出し部13の内径を例えば300(mm)と仮定すると、吹出し部13の開口面積Saは、Sa=0.15×0.15×π=0.07(m)となる。したがって、送風機10の吹出し部13における液滴2を含んだ送風空気の見かけ上の電流密度は、噴霧量1(l/min)あたり0.015/0.07=0.214(mA/m)となる。
The value of this current (0.015 (mA)) represents the amount of charge carried by the droplets 2 sprayed at a spray rate of 1 (l / min) as a current. Further, since the droplet 2 is diffused into the atmosphere by the blown air blown from the blower 10, the current value calculated as described above is divided by the opening area of the blowout portion 13 of the blower 10 to obtain the blower. It is possible to obtain the apparent current density of the blown air containing the droplets 2 in the blowing portion 13 of 10.
Here, assuming that the inner diameter of the blowout portion 13 of the blower 10 is, for example, 300 (mm), the opening area Sa of the blowout portion 13 is Sa = 0.15 × 0.15 × π = 0.07 (m 2 ). Become. Therefore, the apparent current density of the blown air containing the droplets 2 in the blowout portion 13 of the blower 10 is 0.015 / 0.07 = 0.214 (mA / m 2 ) per spray amount 1 (l / min). ).

 ノズル20と対向電極31との間で漏洩電流が流れていない場合には、上述したように、ノズル20と接地9との間に流れる電流の値は、液滴2によって運ばれる単位時間あたりの電荷の量と等しい。そのため、ノズル20と接地9との間に流れる電流の値を測定することで、液滴2によって運ばれる単位時間あたりの電荷の量を求めることができる。
 さらに、全てのノズル20に供給される液体の流量を測定することで、送風機10の吹出し部13における液滴2を含んだ送風空気の見かけ上の電流密度を、噴霧量1(l/min)あたりの値として求めることができる。
When the leakage current does not flow between the nozzle 20 and the counter electrode 31, the value of the current flowing between the nozzle 20 and the ground 9 is, as described above, per unit time carried by the droplet 2. Equal to the amount of charge. Therefore, by measuring the value of the current flowing between the nozzle 20 and the ground 9, the amount of charge carried by the droplet 2 per unit time can be obtained.
Furthermore, by measuring the flow rates of the liquids supplied to all the nozzles 20, the apparent current density of the blown air containing the droplets 2 in the blowout part 13 of the blower 10 can be calculated as the spray amount 1 (l / min). It can be obtained as a value around.

 幾つかの実施形態に係る除塵装置1では、上述した(a)~(c)に挙げたパラメータの値の範囲等も考慮すれば、送風機10の吹出し部13における液滴2を含んだ送風空気の見かけ上の電流密度は、噴霧量1(l/min)あたり0.3(mA/m)以下としてもよいと考えられる。すなわち、ノズル20と接地9との間を流れる電流は、ノズル20と対向電極31との間で漏洩電流が流れていない場合に、液滴2の噴射量1(l/min)あたり及び吹出し部13の開口面積1(m)あたりで、0.3(mA/(m・l/min)以下としてもよいと考えられる。 In the dust remover 1 according to some embodiments, in consideration of the range of the values of the parameters mentioned in (a) to (c) described above, the blown air containing the droplets 2 in the blowout unit 13 of the blower 10 is also taken into consideration. It is considered that the apparent current density may be 0.3 (mA / m 2 ) or less per spray amount 1 (l / min). That is, when the leakage current does not flow between the nozzle 20 and the counter electrode 31, the current flowing between the nozzle 20 and the ground 9 is about 1 (l / min) of the ejection amount of the droplet 2 and the blowing portion. It is considered that it may be 0.3 (mA / (m 2 · l / min) or less per opening area 1 (m 2 ) of 13.

 このように、ノズル20と対向電極31との間で漏洩電流が流れないように対向電極31の絶縁を確保することで、ノズル20と接地9との間を流れる電流が液滴の噴射量1(l/min)あたり及び吹出し部13の開口面積1(m)あたりで、0.3ミリアンペア/(mA/(m・l/min)以下であっても、例えば体育館や屋内競技場のような比較的広い空間や、屋外における大気中の微粒子を効果的に捕集できるように液滴を帯電できる。 In this manner, by ensuring the insulation of the counter electrode 31 so that the leakage current does not flow between the nozzle 20 and the counter electrode 31, the current flowing between the nozzle 20 and the ground 9 causes the droplet ejection amount 1 Even if it is 0.3 mA / (mA / (m 2 · l / min) or less per (l / min) and the opening area 1 (m 2 ) of the blowout portion 13, for example, in a gymnasium or an indoor stadium. The droplets can be charged so as to effectively collect fine particles in the atmosphere in such a relatively large space or outdoors.

(コロナ放電により液滴2に電荷を与える場合について)
 上述の説明では、誘電分極によって液滴2に電荷を与える場合について説明した。そこで、仮に、コロナ放電により液滴2に電荷を与える場合には、どのような放電条件が必要となるのか、以下で検討する。
 例えば、上述したように、液滴径が80(μm)である1つの液滴に、電荷量Qp=2.41×10-13(C)の電荷を与えることができる条件について検討する。
(In case of giving electric charge to the droplet 2 by corona discharge)
In the above description, the case where a charge is applied to the droplet 2 by dielectric polarization has been described. Therefore, it is examined below what kind of discharge conditions are required in the case of applying charges to the droplet 2 by corona discharge.
For example, as described above, a condition under which a charge of Qp = 2.41 × 10 −13 (C) can be given to one drop having a drop diameter of 80 (μm) will be examined.

 静電気学会編、「静電気ハンドブック」オーム社、昭和56年第1版第1刷、268頁―269頁によれば、電界帯電、及び、拡散帯電の式から計算すると、上述した電界強度(4.7(kV/cm))では、液滴径が80(μm)である1つの液滴に2.41×10-13(C)の電荷を与えることが困難であると考えられる。
 液滴径が80(μm)である1つの液滴に2.41×10-13(C)の電荷を与えるためには、さらに高い電界強度が必要であり、概ね、電界強度が5.5(kV/cm)であり、電流密度が10(mA/m)のエリアに、液滴を0.01(sec)程度滞留させることが必要である。なお、ノズルからの液滴の噴射速度が上述したようにおおよそ5(m/sec)から10(m/sec)程度であれば、コロナ放電を行うための一方の放電電極と他方の放電電極との間隔を50~100(mm)に設定し、一方の放電電極側から他方の放電電極側に向かって液滴を噴射することで、上記滞留時間を確保できる。
According to "Statician Handbook", Ohmsha, ed., Published by Ohmsha, ed., 1981, 1st edition, pp. 268-269, the above-mentioned electric field strength (4. 7 (kV / cm)), it is considered difficult to give 2.41 × 10 −13 (C) charges to one droplet having a droplet diameter of 80 (μm).
In order to give 2.41 × 10 −13 (C) charges to one droplet having a droplet diameter of 80 (μm), a higher electric field strength is required, and the electric field strength is generally 5.5. (KV / cm), and it is necessary to retain the droplets for about 0.01 (sec) in the area where the current density is 10 (mA / m 2 ). When the ejection speed of the liquid droplets from the nozzle is approximately 5 (m / sec) to 10 (m / sec) as described above, one discharge electrode for performing corona discharge and the other discharge electrode are used. The retention time can be secured by setting the interval of 50 to 100 (mm) and ejecting droplets from one discharge electrode side toward the other discharge electrode side.

 なお、液滴を噴霧する断面において上記の電流密度(10(mA/m))となることが必要である。例えば、上述した幾つかの実施形態に係る除塵装置1において、対向電極31をコロナ放電を行うための一方の放電電極に置き換え、吹き出し部13にコロナ放電を行うための他方の放電電極を配置した場合を想定する。この場合、放電電極間の領域のうち、少なくとも、吹出し部13を送風方向の下流側から見たときに吹出し部13が投影される領域において、上記の電流密度(10(mA/m))となることが必要である。上述したように、吹出し部13の内径を例えば300(mm)と仮定すると、吹出し部13の開口面積Saは0.07(m)となる。そのため、放電電極間に流れる電流値は、少なくとも、10(mA/m)×0.07(m)=0.7(mA)となる。 The current density (10 (mA / m 2 )) needs to be the above in the cross section where the droplets are sprayed. For example, in the dust remover 1 according to some of the above-described embodiments, the counter electrode 31 is replaced with one discharge electrode for performing corona discharge, and the other discharge electrode for performing corona discharge is arranged in the blowing portion 13. Imagine a case. In this case, the current density (10 (mA / m 2 )) is at least in the region between the discharge electrodes, in the region where the blowout portion 13 is projected when the blowout portion 13 is viewed from the downstream side in the blowing direction. It is necessary to be As described above, assuming that the inner diameter of the blowing portion 13 is 300 (mm), the opening area Sa of the blowing portion 13 is 0.07 (m 2 ). Therefore, the current value flowing between the discharge electrodes is at least 10 (mA / m 2 ) × 0.07 (m 2 ) = 0.7 (mA).

 本発明は上述した実施形態に限定されることはなく、上述した実施形態に変形を加えた形態や、これらの形態を適宜組み合わせた形態も含む。 The present invention is not limited to the above-described embodiments, and includes forms obtained by modifying the above-described embodiments, and forms obtained by appropriately combining these forms.

1 除塵装置
2 液滴
10 送風機
11 筐体
20 ノズル
30 電極部
31 対向電極
33 開口
40 高電圧発生装置
51 支持部
60 方向変更装置
71 掃気用ノズル
DESCRIPTION OF SYMBOLS 1 Dust remover 2 Droplet 10 Blower 11 Housing 20 Nozzle 30 Electrode part 31 Counter electrode 33 Opening 40 High voltage generator 51 Support part 60 Direction changing device 71 Scavenging nozzle

Claims (13)

 送風空気の吹出し部に配置され、供給された液体を液滴として噴射可能であり、接地に接続されている、少なくとも1つのノズルと、
 1つの開口の周囲を少なくとも半周以上囲む形状を有する対向電極を含み、前記ノズルの1つに対して1つの前記対向電極が設けられ、前記ノズルが液滴を噴射する方向に前記対向電極が前記ノズルから離間して配置される電極部と、
 接地端子が前記接地に接続され、出力端子に接続された前記対向電極に高電圧を印加するための高電圧発生装置と、
を備え、
 前記ノズルと前記接地との間を流れる電流は、前記ノズルと前記対向電極との間で漏洩電流が流れていない場合に、前記液滴の噴射量1リットル/分あたり及び前記吹出し部の開口面積1平方メートルあたりで、0.3ミリアンペア/(平方メートル・リットル/分)以下である
除塵装置。
At least one nozzle, which is arranged at the blowout part of the blown air, is capable of ejecting the supplied liquid as droplets, and is connected to the ground;
The counter electrode includes a counter electrode having a shape surrounding at least a half circumference of one opening, and one counter electrode is provided for one of the nozzles, and the counter electrode is arranged in a direction in which the nozzle ejects a droplet. An electrode portion arranged apart from the nozzle,
A high voltage generator for applying a high voltage to the counter electrode, which has a ground terminal connected to the ground and connected to an output terminal,
Equipped with
The current flowing between the nozzle and the ground is, when a leakage current does not flow between the nozzle and the counter electrode, per injection amount of the droplet of 1 liter / min and the opening area of the blowing portion. A dust remover with a rate of 0.3 milliamps / (square meter liter / minute) or less per square meter.
 前記ノズルは、前記液滴を円錐状に噴射するように構成され、
 前記ノズルと前記対向電極との関係は、前記ノズルにおける前記液滴の噴射位置から前記対向電極を含む平面と前記円錐の中心線との交点までの第1距離をr(ミリメートル)とし、前記交点と前記対向電極との最小距離である第2距離をa(ミリメートル)とし、前記ノズルが前記液滴を噴射する噴射角度をθ(度)とすると、次式(1)
  r<a/tan(θ/2)・・・(1)
で表される、
請求項1に記載の除塵装置。
The nozzle is configured to eject the droplet in a conical shape,
Regarding the relationship between the nozzle and the counter electrode, the first distance from the jetting position of the droplet in the nozzle to the intersection of the plane including the counter electrode and the center line of the cone is r (millimeter), and the intersection is When the second distance that is the minimum distance between the counter electrode and the counter electrode is a 0 (millimeter), and the ejection angle at which the nozzle ejects the droplet is θ (degrees), the following equation (1)
r <a 0 / tan (θ / 2) (1)
Represented by
The dust remover according to claim 1.
 前記第1距離は、5ミリメートル以上200ミリメートル以下であり、
 前記第2距離は、5ミリメートル以上50ミリメートル以下である、
請求項2に記載の除塵装置。
The first distance is 5 mm or more and 200 mm or less,
The second distance is 5 mm or more and 50 mm or less,
The dust remover according to claim 2.
 前記ノズルの前記噴射角度は、30度以上100度以下である、
請求項2又は3に記載の除塵装置。
The jet angle of the nozzle is 30 degrees or more and 100 degrees or less,
The dust remover according to claim 2 or 3.
 前記少なくとも1つのノズルは、液滴径がザウタ平均径で10マイクロメートル以上300マイクロメートル以下となる前記液滴を噴射可能に構成されている
請求項1乃至4の何れか一項に記載の除塵装置。
5. The dust remover according to claim 1, wherein the at least one nozzle is configured to be capable of ejecting the droplets having a droplet diameter of 10 μm or more and 300 μm or less in average Sauter diameter. apparatus.
 前記吹出し部を有し、前記液滴を含む空気を送風するための送風機をさらに備え、
 前記ノズル及び前記電極部は、前記送風機の筐体に取り付けられている
請求項1乃至5の何れか一項に記載の除塵装置。
And a blower for blowing the air containing the droplets,
The dust remover according to any one of claims 1 to 5, wherein the nozzle and the electrode portion are attached to a casing of the blower.
 絶縁材によって構成され、前記電極部を支持する支持部と、
 前記支持部に向かって気体を噴射可能に構成された掃気用ノズルと、
をさらに備える
請求項1乃至6の何れか一項に記載の除塵装置。
A support portion configured by an insulating material and supporting the electrode portion,
A scavenging nozzle configured to inject a gas toward the support portion,
The dust removing device according to claim 1, further comprising:
 撥水性の絶縁材によって構成されるか、又は、絶縁材によって構成されていて表面に撥水処理が施されている、前記電極部を支持する支持部をさらに備える
請求項1乃至7の何れか一項に記載の除塵装置。
8. A support part for supporting the electrode part, which is made of a water-repellent insulating material or is made of an insulating material and whose surface is subjected to a water-repellent treatment. The dust remover according to item 1.
 前記吹出し部を有し、前記液滴を含む空気を送風するための送風機をさらに備え、
 前記ノズルは、前記送風機が送風する空気の流れに関して前記送風機の下流側に複数設けられている
請求項1乃至8の何れか一項に記載の除塵装置。
And a blower for blowing the air containing the droplets,
The dust remover according to any one of claims 1 to 8, wherein a plurality of the nozzles are provided on a downstream side of the blower with respect to a flow of air blown by the blower.
 前記吹出し部を有し、前記液滴を含む空気を送風するための送風機と、
 前記送風機からの空気の送風方向を変更可能に構成された方向変更装置と、
をさらに備える
請求項1乃至9の何れか一項に記載の除塵装置。
An air blower for blowing air containing the droplets, the blower having the blowing portion;
A direction changing device configured to change the blowing direction of air from the blower,
The dust remover according to any one of claims 1 to 9, further comprising:
 前記吹出し部を有し、前記液滴を含む空気を送風するための送風機と、
 前記送風機からの空気の送風方向を変更可能に構成された方向変更装置と、
をさらに備え、
 前記方向変更装置は、少なくとも水平方向よりも上側に送風できるように前記送風方向を設定可能に構成されている
請求項1乃至10の何れか一項に記載の除塵装置。
An air blower for blowing air containing the droplets, the blower having the blowing portion;
A direction changing device configured to change the blowing direction of air from the blower,
Further equipped with,
The dust removing device according to claim 1, wherein the direction changing device is configured to be able to set the air blowing direction so as to blow air at least above a horizontal direction.
 前記方向変更装置は、0度以上の仰角で上側に向かって送風できるように前記送風方向を設定可能に構成されている
請求項10又は11に記載の除塵装置。
The dust removing device according to claim 10 or 11, wherein the direction changing device is configured to be able to set the air blowing direction so that air can be blown upward with an elevation angle of 0 degrees or more.
 前記方向変更装置は、前記少なくとも1つのノズルからの前記液滴の噴射方向を前記送風機からの空気の送風方向と同じ方向に変更可能に構成されている
請求項10乃至12の何れか一項に記載の除塵装置。
13. The direction changing device is configured to be capable of changing a jetting direction of the droplet from the at least one nozzle to the same direction as a blowing direction of air from the blower. The dust removing device described.
PCT/JP2019/041053 2018-10-26 2019-10-18 Dust removal device Ceased WO2020085231A1 (en)

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