EP0345309A1 - Filtre electrostatique pour la separation continue de particules solides ou fluides en suspension dans un courant de gaz - Google Patents

Filtre electrostatique pour la separation continue de particules solides ou fluides en suspension dans un courant de gaz

Info

Publication number
EP0345309A1
EP0345309A1 EP88909507A EP88909507A EP0345309A1 EP 0345309 A1 EP0345309 A1 EP 0345309A1 EP 88909507 A EP88909507 A EP 88909507A EP 88909507 A EP88909507 A EP 88909507A EP 0345309 A1 EP0345309 A1 EP 0345309A1
Authority
EP
European Patent Office
Prior art keywords
electrode
separating
electrodes
gas stream
flow
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
EP88909507A
Other languages
German (de)
English (en)
Other versions
EP0345309B1 (fr
Inventor
Harald Jodeit
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.)
ABB Asea Brown Boveri Ltd
ABB AB
Original Assignee
ABB Asea Brown Boveri Ltd
Asea Brown Boveri AB
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 ABB Asea Brown Boveri Ltd, Asea Brown Boveri AB filed Critical ABB Asea Brown Boveri Ltd
Priority to AT88909507T priority Critical patent/ATE74801T1/de
Publication of EP0345309A1 publication Critical patent/EP0345309A1/fr
Application granted granted Critical
Publication of EP0345309B1 publication Critical patent/EP0345309B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/66—Applications of electricity supply techniques
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02—Plant or installations having external electricity supply
    • B03C3/04—Plant or installations having external electricity supply dry type
    • B03C3/10—Plant or installations having external electricity supply dry type characterised by presence of electrodes moving during separating action

Definitions

  • Electrostatic filters for separating solid and liquid particles are widely used in the metallurgical and chemical industries as well as in power plants. Dust separation and gas cleaning have become increasingly important, particularly in connection with environmental protection regulations.
  • the invention relates to the further development, improvement and simplification of electrostatic dust separation and to the reduction of the associated apparatus.
  • an electrostatic filter for the continuous separation of solid or liquid particles suspended in a gas stream, with a rectangular cross-section in a channel guiding the gas stream at least one spray electrode acting as an ion source and utilizing the corona effect is arranged in the form of a plurality of peaks placed in the flow direction and at least one transverse, movable flat separator designed as an endless perforated conveyor belt or traveling grille, such that the spray electrode and the separating electrode are penetrated essentially vertically by the gas stream laden with particles and the electric fields accelerating the charged particles lie essentially in the direction of flow.
  • Dust separation is improved by moving separation electrodes with continuous cleaning.
  • electrically conductive metal strips or metal plates fastened to chains which in many cases also serve as lateral delimitation of the flow channel, are generally moved in a "cross flow" perpendicular to the direction of flow.
  • These movable separation electrodes are usually cleaned with the help of rotating brushes.
  • the construction of the device should be simple and inexpensive and should be characterized by low energy consumption and low maintenance requirements. You should fine the ⁇ special capture and fine dust particles to be suitable and independent of the carrier gas.
  • This object is achieved in that, in the electrostatic filter mentioned at the outset, in the direction of flow, after the separating electrode, in the space between the planes its supply side and the level of its return side and / or in the space after the level of its return side at least one control unit located in the same name as the spray electrode, in the form of rods lying in a plane parallel to the separating electrode, or in the form of a Grid or grid is arranged.
  • FIG. 1 schematically shows the basic structure of the basic embodiment of an electric lecturer with only one row of control electrodes in the space between two separating electrodes
  • FIG. 2 schematically shows the basic structure of an embodiment of an electrofilter with only one row of control electrodes in the space after the second separating electrode
  • FIG. 3 schematically shows the basic structure of an embodiment of an electrostatic filter with a number of control electrodes in the space between two reading electrodes and a number of control electrodes in the space after the second reading.
  • Fig. 4 shows schematically the construction of an embodiment of an ELektro ⁇ filter with several spray electrodes, several rows of control electrodes and rotating, zigzag, multi-acting band-shaped separating electrode.
  • Fig. 5 shows schematically the structure of an embodiment of an ELektro ⁇ filter with several spray electrodes, several rows of control electrodes and a plurality of circumferential, parallel ribbon-shaped separation electrodes,
  • FIG. 6 shows the basic structure (longitudinal section) of an embodiment of an electrofilter with a peripheral separating electrode and only one row of control electrodes
  • FIG. 7 shows the basic structure (longitudinal section) - an embodiment of an electrofilter with a peripheral separating electrode and three rows of control electrodes.
  • 1 schematically shows the basic structure of the basic design of an electrofilter with only one row of control electrodes in the space between two separating electrodes.
  • 1 is the gas stream loaded with particles, which perpendicularly passes through the electrodes arranged in parallel planes transverse to the direction of flow.
  • 3 is a usually negatively charged (sign) spray electrode, the tips 4 of which use the corona effect serve as ion sources.
  • 5 are the separating electrodes, which are basically designed as perforated sheets, nets or grids, and are normally kept at zero potential (sign 0). In the present case, there is mechanically a single, continuous, continuous separating electrode designed as a broken band.
  • 6 is the control electrode formed as round rods, which is at the same potential as the spray electrode 3.
  • This electrode arrangement requires an accelerating electric field 7 located in the direction of flow between the spray electrode 3 and the outer feed side (indicated by the left-hand arrow ) of the separating electrode 5. This is the case between the control lect 6 and the inner feed side of the separator 5 the accelerating electric field directed 8. The accelerating electric field between the control electrode 6 and the inner return side (indicated by the right-hand arrow) of the separating electrode 5 is again in the direction of flow.
  • the charged particles which in the present case have a negative charge (sign) are given multiple opportunities to deposit on one and / or the other side of the separating electrode 5. This is represented by the trajectories 10 of the charged particles. Accordingly, for example, a particle is repelled by the electric field 8 on the inner feed side of the separating electrode 5 against the direction of flow.
  • FIG. 2 shows schematically the basic structure of an embodiment of an electrofilter with only one row of control electrodes in the room after the second separating electrode.
  • 1 is the gas flow .
  • m 3 the spray electrode provided with tips 4, 5 the separator formed as a continuous openwork band and 6 the control electrode in the form of parallel rods.
  • the Fe Ldverh- ⁇ Ltm " sse in the space between the spray electrode 4 and the outer feed side of the separating electrode 5 are the same as in Fig. 1 (accelerating electrical field 7).
  • the separating electrode is dominated by the electric field NuLL (sign 0), which becomes in the space between the external control electrode 6 (negative potential: sign -) and the outer return side of the separating electrode 5 (potential zero: sign 0) against the direction of flow accelerating electrical field 15.
  • the trajectories 10 reflect the migration of the charged particles (sign -) onto the separating electrode 5. For example, a particleL is deflected under the influence of the electrical field 15 and against the direction of flow knocked back on the outer return side of the separating electrode 5.
  • FIGS. 1 and 2 schematically shows the basic structure of an embodiment of an electrofilter with a row of control electrodes in the space between two separation electrodes and one Row of control electrodes shown in the room after the second Abscheide ⁇ electrode. It is essentially a superposition of the electrode arrangements of FIGS. 1 and 2.
  • the accelerating electric fields 7 and 9 are directed in the direction of flow, the fields 8 and 15 are directed against the direction of flow. Accordingly, there are 4 different possibilities for the migration of the negatively charged particles (sign) to the separating electrodes 5. All reference numerals correspond to those in FIGS. 1 and 2.
  • FIG. 4 schematically shows the structure of an embodiment of an electrostatic filter with a plurality of spray electrodes, a plurality of rows of control electrodes and a circumferential, zigzag-guided, multi-acting band-shaped separation electrode.
  • the gas stream 1 passes vertically through several electrode groups arranged in parallel planes.
  • the Abschei deelektrode 5 is designed as an endless openwork band, which-more than between a spray electrode 3 with tips 4 and a number of control electrodes 6, respectively. between two rows of control electrodes 6.
  • the belt is guided over drums 11 acting as deflection rollers. All spray electrodes 4 and all control electrodes 6 are at negative potential (sign -), while the multi-acting deposition electrode 5 is at zero potential (sign 0).
  • the spray electrodes 4 are on the negative pole of a direct high-voltage source 16 (voltage U 1 ), while the control electrodes 6 are on the negative pole of a second direct high-voltage source 17 (voltage U ? ).
  • the positive poles of both high-voltage sources are connected to the separating electrode 5 and are grounded together (sign 0).
  • the potential connections between the high-voltage sources and the electrodes are only shown in the upper part of the figure.
  • Such a cascade connection of a plurality of electrode groups lying one behind the other in the direction of flow improves the degree of separation, particularly in the case of very fine dust.
  • FIG. 5 schematically shows the construction of an embodiment of an electrostatic filter with a plurality of spray electrodes, a plurality of rows of control electrodes and a plurality of circumferential, parallel band-shaped separation electrodes.
  • the construction is similar to that of FIG. 4, with the difference that here 3 separate, i Openwork tapes guided essentially in the same way are used as deposition electrodes 5.
  • the arrangement of the spray electrodes 3 and the control electrodes 6 is similar to that of Fig. 4.
  • the potential relationships are basically the same. The voltage coupling has not been shown. Otherwise, the reference numerals are the same as in FIG. 4.
  • FIG. 6 shows the basic structure (longitudinal step) of an embodiment of an electrofilter with a rotating separating electrode and only one row of control electrodes.
  • 1 is the gas stream loaded with particles and guided vertically downwards in a channel 2. It passes through the plane of the spray electrode 3 vertically.
  • Whose tips 4 are arranged on a (for example square, rectangular or hexagonal) grid and point in the direction of flow.
  • 5 is the circumferential endless deposition electrode (for example designed as a broken band). The dust particles deposited on it are indicated as dots.
  • the drums 11, which are accommodated in lateral chambers, are provided as deflection rollers for the separating electrode 5 outside the channel wall 2. The direction of movement is indicated by arrows.
  • the Lekt rode 5 deposited on the separator dust is removed by bilateral wipers (scraper) 12 and also bilateral rotating re cleaning bushes 13 removed. With 14 de rabaustrag is indicated, but this is usually done in practice perpendicular to the plane of the drawing.
  • the control electrode which is designed in the form of parallel rods, is located between the supply side and the return side of the separating electrode 5. 6. Between the negatively charged tips 4 in the present case, which act as ion sources (co- rona effect ) , and the accelerating electric field 7 is built up on the outer supply side of the separating electrode 5, which is at zero potential. It is directed in the direction of flow.
  • An accelerating electric field 8 directed against the direction of flow is spanned between the negatively charged control electrode 6 and the inner feed side of the separating electrode 5. Between the control electrode 6 and the inner return side of the separating electrode 5 there is the accelerating electric field 9 directed in the direction of flow.
  • the trajectories 10 indicate the migration paths of the charged particles.
  • the active components 2, 3, 4, 5, 6, 11, 12 and 13 are usually made of rustproof or corrosion-resistant Cr or Cr / Ni steel.
  • FIG. 7 shows the basic structure (longitudinal section) of an embodiment of an electrofilter with a circumferential separating electrode and three rows of control electrodes.
  • the basic concept is similar to that of Fig. 6, with the reference numerals corresponding exactly.
  • the gas stream 1 loaded with particles was guided vertically from top to bottom.
  • the already expanded channel 2 consisted of a sheet made of corrosion-resistant 18 Cr / 8 Ni steel and
  • the spray electrode 3 also made of Cr / Ni steel, had tips 4 of 20 mm length arranged on a square grid ( in the direction of flow) and 0.8 mm rounding radius.
  • the tips 4 also made of corrosion-resistant Cr / Ni steel and had ⁇ a mutual spacing in two main 'chtungen of 100 mm.
  • the circumferential endless separating electrode 5 was designed in the form of 3, viewed perpendicular to the plane of the drawing, side by side (one behind the other) arranged, parallel and synchronously guided openwork steel bands.
  • the strips had a thickness of 0.5 mm and consisted of a corrosion-resistant type 18/8 Cr / Ni steel alloyed with special additives, but with a high plug-in limit, in the cold-rolled, almost spring-hard condition.
  • Each band had slots arranged in the direction of movement in the form of oblong holes of 5 mm width and 56 mm length rounded on the narrow sides.
  • the center distance (pitch) of the slots in the longitudinal direction (moving direction) was 119 mm, that in Quer ⁇ 'rect 10 mm. Adjacent rows of slots were offset by half a division in the longitudinal direction.
  • the strips ran over drums 11 made of Cr / Ni steel, which had a diameter of 250 mm. One of the drums 11 was driven by an electric motor via a gear.
  • the conveying speed was adjustable between approx. 1.5 mm / s and 85 mm / s, which corresponded to 1 revolution / h or 60 revolutions / h.
  • the distance from the tape surface to the tips 4 was 70 mm.
  • the control electrodes 6 were rods made of Cr / Ni steel with a diameter of 10 mm and a horizontal center distance (pitch) from one another.
  • the vertical distance between the centers of the bars from the adjacent strip surface was 75 mm each, the vertical distance between the centers of the bars below them was 100 mm.
  • the wipers (scraper) 12 and the rotating cleaning brushes 13 were also made of corrosion-resistant Cr / Ni steel.
  • the plant was operated with a gas stream 1 loaded with quartz dust.
  • the negative pole of a high-voltage source was placed.
  • the positive pole was placed on the separating electrode 5 and at the same time grounded (potential 0).
  • the control electrodes 6 negative pole of another equilibrium high-voltage source, while its positive pole was connected to earth.
  • Control electrode / separation electrode
  • the invention is not limited to the exemplary embodiment.
  • the separating electrode 5 is designed as a perforated conveyor belt or traveling grating, the control electrode 6 in the form of bars, grids or grids.
  • the multiple separating electrode 5 is designed as conveyor belts which are located one behind the other in the flow direction and move in the same or opposite directions.
  • the potential of the control electrodes 6 is generally matched to that of the spray electrode. Its absolute value is preferably set higher than that of the spray electrode 3. Otherwise, reference is made to the embodiment variants of FIGS. 1 to 6.

Landscapes

  • Electrostatic Separation (AREA)
  • Filtering Materials (AREA)

Abstract

Le filtre électrostatique pour la séparation continue de particules solides ou fluides dans un courant de gaz dans un canal (2) comporte une série d'électrodes de dispersion (3) disposées transversalement au courant face à des électrodes de séparation (5) en mouvement continu sur des tambours (11). Le nettoyage de ces électrodes est effectué au moyen de racloirs (12) et de brosses rotatives (13). Une série d'électrodes de commande (6) sont disposées en plusieurs rangées parallèles aux électrodes de séparation. Les électrodes de commande (6) se trouvent à l'intérieur et/ou à l'extérieur des côtés d'entrée et de sortie des électrodes de séparation (5) et sont portées à un potentiel de même polarité que les électrodes de dispersion (3). Les particules s'accumulent sur tous les côtés des électrodes de séparation (5) ce qui conduit à un rendement élevé.
EP88909507A 1987-11-27 1988-11-17 Filtre electrostatique pour la separation continue de particules solides ou fluides en suspension dans un courant de gaz Expired - Lifetime EP0345309B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT88909507T ATE74801T1 (de) 1987-11-27 1988-11-17 Elektrostatisches filter fuer die kontinuierliche abscheidung von in einem gasstrom suspendierten festen oder fluessigen partikeln.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH4637/87 1987-11-27
CH4637/87A CH673411A5 (fr) 1987-11-27 1987-11-27

Publications (2)

Publication Number Publication Date
EP0345309A1 true EP0345309A1 (fr) 1989-12-13
EP0345309B1 EP0345309B1 (fr) 1992-04-15

Family

ID=4279851

Family Applications (1)

Application Number Title Priority Date Filing Date
EP88909507A Expired - Lifetime EP0345309B1 (fr) 1987-11-27 1988-11-17 Filtre electrostatique pour la separation continue de particules solides ou fluides en suspension dans un courant de gaz

Country Status (6)

Country Link
EP (1) EP0345309B1 (fr)
AT (1) ATE74801T1 (fr)
AU (1) AU2616288A (fr)
CH (1) CH673411A5 (fr)
DE (1) DE3870231D1 (fr)
WO (1) WO1989004724A1 (fr)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE8900214L (sv) * 1989-01-20 1990-07-21 Flaekt Ab Anordning foer rening av med faergpartiklar foerorenad ventilationsluft
EP0415486B1 (fr) * 1989-08-31 1994-03-16 METALLGESELLSCHAFT Aktiengesellschaft Procédé et appareil pour la purification électrostatique d'effluents de gaz nocifs et poussiéreux dans des séparateurs à plusieurs champs
AU776136B2 (en) * 2000-05-19 2004-08-26 Hitachi, Ltd. Moving electrode type electric dust collecting apparatus
GB0616916D0 (en) * 2006-08-26 2006-10-04 Secr Defence An electrostatic precipitator
DE102007036553A1 (de) * 2007-07-25 2009-02-05 Eisenmann Anlagenbau Gmbh & Co. Kg Vorrichtung zum Abscheiden von Lack-Overspray
CN104826737A (zh) * 2015-05-26 2015-08-12 济宁德山峻明机械设备有限公司 一种回流式静电除尘装置

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE636744A (fr) * 1962-08-29
US3740927A (en) * 1969-10-24 1973-06-26 American Standard Inc Electrostatic precipitator
US3650092A (en) * 1970-08-17 1972-03-21 Gourdine Systems Inc Electrogasdynamic precipitator utilizing retarding fields
DE3418112A1 (de) * 1984-05-16 1985-11-21 Brown, Boveri & Cie Ag, 6800 Mannheim Entstaubungsvorrichtung

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO8904724A1 *

Also Published As

Publication number Publication date
EP0345309B1 (fr) 1992-04-15
WO1989004724A1 (fr) 1989-06-01
ATE74801T1 (de) 1992-05-15
AU2616288A (en) 1989-06-14
DE3870231D1 (de) 1992-05-21
CH673411A5 (fr) 1990-03-15

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