EP4000738A1 - Filtre de nettoyage d'un flux gazeux - Google Patents

Filtre de nettoyage d'un flux gazeux Download PDF

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Publication number
EP4000738A1
EP4000738A1 EP20207187.4A EP20207187A EP4000738A1 EP 4000738 A1 EP4000738 A1 EP 4000738A1 EP 20207187 A EP20207187 A EP 20207187A EP 4000738 A1 EP4000738 A1 EP 4000738A1
Authority
EP
European Patent Office
Prior art keywords
ionization
electrode
plate
counter
electrode plate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP20207187.4A
Other languages
German (de)
English (en)
Other versions
EP4000738B1 (fr
Inventor
Harald Hentschel
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.)
Isi Industrieprodukte GmbH
Original Assignee
Isi Industrieprodukte GmbH
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 Isi Industrieprodukte GmbH filed Critical Isi Industrieprodukte GmbH
Priority to EP20207187.4A priority Critical patent/EP4000738B1/fr
Publication of EP4000738A1 publication Critical patent/EP4000738A1/fr
Application granted granted Critical
Publication of EP4000738B1 publication Critical patent/EP4000738B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • 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
    • B03C3/04Plant or installations having external electricity supply dry type
    • B03C3/12Plant or installations having external electricity supply dry type characterised by separation of ionising and collecting stations
    • 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
    • B03C3/04Plant or installations having external electricity supply dry type
    • B03C3/06Plant or installations having external electricity supply dry type characterised by presence of stationary tube electrodes
    • 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
    • B03C3/04Plant or installations having external electricity supply dry type
    • B03C3/08Plant or installations having external electricity supply dry type characterised by presence of stationary flat electrodes arranged with their flat surfaces parallel to the gas stream
    • 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
    • B03C3/36Controlling flow of gases or vapour
    • B03C3/361Controlling flow of gases or vapour by static mechanical means, e.g. deflector
    • B03C3/366Controlling flow of gases or vapour by static mechanical means, e.g. deflector located in the filter, e.g. special shape of the electrodes
    • 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
    • B03C3/40Electrode constructions
    • B03C3/41Ionising-electrodes
    • 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
    • B03C3/40Electrode constructions
    • B03C3/45Collecting-electrodes
    • B03C3/47Collecting-electrodes flat, e.g. plates, discs, gratings
    • 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
    • B03C2201/00Details of magnetic or electrostatic separation
    • B03C2201/04Ionising electrode being a wire

Definitions

  • the invention relates to an electrostatic filter with an ionization unit and a separation unit for cleaning a gas flow.
  • the electrode plate has a front edge and a rear edge, viewed in the direction of flow, which are positioned in front of the ionization element, viewed in the direction of flow.
  • the rear edge of the electrode plate is also arranged in front of the ionization element. The rear edge is located in the inflow direction in front of a plane in which the ionization element is located and which extends perpendicularly to the inflow direction.
  • a voltage can be applied between the ionization element and the electrode plate, so that an electric field is created.
  • the particles transported in the gas flow are ionized by the electric field.
  • Ionization means that the particles are electrically charged, so that each particle has an excess of electrons, for example.
  • the gas flow can be an air flow. In addition, it can also be other gaseous media or mixtures.
  • the gas flow contains particles that are transported along with it. Particles can be dirt or dust particles that arise in industrial processes such as metal-cutting shaping (e.g. turning and milling using coolants). The particles can also be fine dust or the finest particles, right down to microscopically small suspended matter or particles. A particle can also be a liquid substance. Accordingly, particles can also be droplets or aerosols. Droplets or aerosols can also be carriers of viruses or bacteria, so that the filter according to the invention can be used to filter viruses or bacteria. Ozone, which can form in the ionization unit, can advantageously be used to kill viruses or bacteria.
  • the filter can be used in extractors, air conditioners, room fans or ventilation systems.
  • An advantageous arrangement of ionization element and counter-electrode is realized by the invention.
  • the position of the electrode plate with its rear edge makes it possible for the ionization and the associated flow of electrons between the ionization element and counter-electrode to take place in front of the ionization element, viewed in the flow direction.
  • the sharp contour of the rear edge promotes the desired ionization.
  • an advantageous flow behavior of the gas flow can be adjusted by the electrode plate connected upstream of the ionization element.
  • the counter-electrode can be positioned in such a way that the particles are exposed to the ionization for a long time and thus an efficient ionization takes place.
  • the direction of the gas flow and the particles is preferably aligned and/or calmed by the electrode plate.
  • a turbulent gas flow can be converted into a directed gas flow by flowing around the electrode plate.
  • the gas flow and the particles preferably do not experience any turbulence.
  • the configuration can also prevent stagnation points.
  • Stagnation points are points at which flow-related particles are deposited because there is no air movement in the stagnation point.
  • a further advantage is the simple design of the counter-electrode on the basis of plates or metal sheets, as a result of which the filter can be manufactured at low cost.
  • the rear edge of the electrode plate runs parallel to the longitudinal axis of the ionization element.
  • a constant distance from the rear edge of the electrode plate can thus be set over the entire length of the ionization element. This enables continuous and efficient ionization to be achieved over the entire length of the ionization element.
  • the precipitation plates also have the additional function of specifying the direction of gas flow and particles through the plate.
  • the electrode plate and the precipitation plate can advantageously be matched to one another, for example by lying in one plane and thus providing a good flow profile.
  • the ozone that has formed on the ionization element can be transported away or broken down by the precipitation plates. Due to the design as a flat sheet, the precipitation plate is particularly easy to clean. It is also conceivable for the ozone and/or for particles which could not or could not be separated from the gas flow in the separation unit could be dismantled to provide a downstream after-treatment. This can include the use of an activated carbon filter. Filter media made of glass fibers can also be used here.
  • the precipitation plate can have a front edge which is arranged behind the ionization element as seen in the direction of flow and whose distance from the ionization element preferably corresponds to the distance from the rear edge of the electrode plate of the counter-electrode to the ionization element.
  • the rear edge of the electrode plate of the counter-electrode and the front edge of the collecting electrode lie on the circumference of a circle whose center coincides with the longitudinal axis of the ionization element and whose radius corresponds to the distance.
  • the precipitation plate is therefore not only used to separate the particles from the gas flow, but can also contribute to the ionization of the particles.
  • the counter-electrode has at least two additional electrode plates, the ratio of one The distance between the two additional electrode plates and the distance between the ionization element and the rear edge of the electrode plate is 1.5 to 2.5, preferably 1.8 to 2.2. If the counter-electrode has more than two additional electrode plates, the distance described here is the distance between two adjacent additional electrode plates. It has been found that with the above ratio, a compact ionization unit with good efficiency can be implemented.
  • the separating unit 3 has three precipitation plates 9 and two intermediate plates 10 which are arranged between two adjacent precipitation plates.
  • the precipitation plates 9 and the intermediate plates 10 are in the figure 1 shown only partially and therefore in a shortened form.
  • the rear edges 14 of the electrode plates 7 can also lie in a common plane which is aligned parallel to the plane E. In this case, the individual rear edges 14 would not be at the same distance from the ionization element 4.
  • the electrode plates 7 and the additional electrode plates 8 are grounded, while a voltage is applied to the ionization element.
  • the precipitation plates are also grounded, with the intermediate plates also being subjected to a voltage.

Landscapes

  • Electrostatic Separation (AREA)
EP20207187.4A 2020-11-12 2020-11-12 Filtre de nettoyage d'un flux gazeux Active EP4000738B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP20207187.4A EP4000738B1 (fr) 2020-11-12 2020-11-12 Filtre de nettoyage d'un flux gazeux

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP20207187.4A EP4000738B1 (fr) 2020-11-12 2020-11-12 Filtre de nettoyage d'un flux gazeux

Publications (2)

Publication Number Publication Date
EP4000738A1 true EP4000738A1 (fr) 2022-05-25
EP4000738B1 EP4000738B1 (fr) 2022-11-02

Family

ID=73401387

Family Applications (1)

Application Number Title Priority Date Filing Date
EP20207187.4A Active EP4000738B1 (fr) 2020-11-12 2020-11-12 Filtre de nettoyage d'un flux gazeux

Country Status (1)

Country Link
EP (1) EP4000738B1 (fr)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1073901A (en) * 1964-09-14 1967-06-28 Hitachi Ltd Electrostatic precipitator
JPS60187357A (ja) * 1984-03-07 1985-09-24 Sanden Corp 空気清浄器
JPS60187358A (ja) * 1984-03-05 1985-09-24 Sanden Corp 空気清浄器
JPH0884939A (ja) * 1994-09-14 1996-04-02 Matsushita Electric Works Ltd 空気清浄器
EP2105205B1 (fr) 2008-03-28 2011-08-10 ISI-Industrie-Produkte GmbH Elément d'ionisation et filtre électrostatique
DE102017214495A1 (de) 2017-08-21 2019-02-21 BSH Hausgeräte GmbH Filtereinheit für Luftreinigungsvorrichtung und Luftreinigungsvorrichtung

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1073901A (en) * 1964-09-14 1967-06-28 Hitachi Ltd Electrostatic precipitator
JPS60187358A (ja) * 1984-03-05 1985-09-24 Sanden Corp 空気清浄器
JPS60187357A (ja) * 1984-03-07 1985-09-24 Sanden Corp 空気清浄器
JPH0884939A (ja) * 1994-09-14 1996-04-02 Matsushita Electric Works Ltd 空気清浄器
EP2105205B1 (fr) 2008-03-28 2011-08-10 ISI-Industrie-Produkte GmbH Elément d'ionisation et filtre électrostatique
DE102017214495A1 (de) 2017-08-21 2019-02-21 BSH Hausgeräte GmbH Filtereinheit für Luftreinigungsvorrichtung und Luftreinigungsvorrichtung

Also Published As

Publication number Publication date
EP4000738B1 (fr) 2022-11-02

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