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WO1992019380A1 - Separateur electrostatique a l'etat humide et procede d'utilisation - Google Patents

Separateur electrostatique a l'etat humide et procede d'utilisation Download PDF

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Publication number
WO1992019380A1
WO1992019380A1 PCT/US1992/002999 US9202999W WO9219380A1 WO 1992019380 A1 WO1992019380 A1 WO 1992019380A1 US 9202999 W US9202999 W US 9202999W WO 9219380 A1 WO9219380 A1 WO 9219380A1
Authority
WO
WIPO (PCT)
Prior art keywords
precipitator
discharge
electrode
mast
outer electrode
Prior art date
Application number
PCT/US1992/002999
Other languages
English (en)
Inventor
Shui-Chow Yung
Mark T. Herndon
Original Assignee
Calvert Environmental
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 Calvert Environmental filed Critical Calvert Environmental
Publication of WO1992019380A1 publication Critical patent/WO1992019380A1/fr

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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
    • B03C3/40—Electrode constructions
    • B03C3/41—Ionising-electrodes
    • 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
    • B03C3/06—Plant or installations having external electricity supply dry type characterised by presence of stationary tube electrodes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02—Plant or installations having external electricity supply
    • B03C3/16—Plant or installations having external electricity supply wet type
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/66—Applications of electricity supply techniques
    • B03C3/70—Applications of electricity supply techniques insulating in electric separators
    • 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
    • B03C2201/00—Details of magnetic or electrostatic separation
    • B03C2201/10—Ionising electrode with two or more serrated ends or sides

Definitions

  • the present invention relates generally to an electrostatic apparatus and method for removing particulates from fluid streams.
  • the invention more particularly relates to a new and improved wet electrostatic precipitator, and method of operating same, for more efficient and effective particle removal.
  • Electrostatic precipitators have been employed for removal of particulates in waste fluids.
  • the precipitators include concentric electrodes in the form of an electrically conductive rod or mast disposed within an electrically conductive collector tube. A high voltage discharge between the electrodes ionizes particles from the waste fluid.
  • the conventional electrostatic precipitators described above may be useful with regard to handling large volumes of waste gas.
  • the problem relates to the construction and configuration of the inner electrode.
  • the foregoing mentioned prior known electrodes employ various different projections extending along an inner electrode mast, in a spaced apart manner, relative to an outer collection tube. The spacing is critical, and enables the electrostatic discharge to occur between the electrodes.
  • the projections such as helical fins and discs, serve as a hinderance to the free flow of gas through the collection tubes. Additionally, such projections do not provide the highly desirable uniform electrostatic field to increase particle removal from the gas.
  • the inner electrode should not present an undue impedance to the flow of gas through the collection tube, and at the same time, present a highly uniform electrostatic field. Disclosure of Invention It is therefore a principal object of the present invention to provide an electrostatic precipitator and method of using it having high intensity ionization electrodes for providing a uniform electrostatic field for more efficient and effective particle removal. It is a further object of the present invention to provide such an electrostatic precipitator and method for greatly reducing impedance to the flow of fluid to be cleaned through the precipitator.
  • a wet electrostatic precipitator and method include the use of concentric electrodes, the inner one of which includes a discharge disc extending a short distance therefrom toward the outer electrode to reduce the impedance to waste gas fluid flow.
  • a relatively large number of discharge points on the outer periphery of the disc provides a large number of radially extending discharge paths to the outer electrode, in a very uniform manner.
  • a large number of individual discharge points are utilized to produce a uniform field distribution. The number of discharge points is precisely determined because if the disc were to have too many points, the disc would approach a smooth outer periphery and not be as effective in maintaining a uniform field. Too few points would lead to a condition of fewer individual discharges and less uniformity in the field.
  • FIG. 1 is an elevational, partially cut away diagrammatic view of the electrostatic precipitator of the present invention, the precipitator being illustrated in a waste gas treating system;
  • FIG. 2 is an enlarged sectional view of the system of FIG. 1, taken substantially on line 2-2 thereof;
  • FIG. 3 is a greatly enlarged plan view of a discharge disc of the circled portion of the precipitator of FIG. 2;
  • FIG. 4 is a fragmentary sectional view of another precipitator, which is also constructed according to the invention, and which is shown with only one pair of its concentric electrodes;
  • FIG. 4A is a fragmentary sectional view of another electrostatic precipitator, which is also constructed according to the present invention, and which is shown with only one pair of its concentric electrodes;
  • FIG. 5 is a fragmentary sectional view of still another form of a precipitator, which is also constructed according to the invention and which is shown with only one pair of its concentric electrodes;
  • FIG. 6 is a fragmentary sectional view of yet still another form of a precipitator, which is also constructed according to the invention and is shown with only one pair of its concentric electrodes;
  • FIG. 7 is a greatly enlarged view of the circled portion of the electrode of FIG. 3. Best Mode for Carrying Out the Invention Referring now the drawings, and more particularly to FIG. 1 thereof, there is shown a wet scrubbing system 10 having an inlet 11 in an upper portion 22 of a generally cylindrical housing 24 confining a wet electrostatic precipitator 20, which is constructed in accordance with the present invention. Waste gas enters the system 10 at an inlet 11, passes through a cylindrical conduit 13 into the upper portion 22 where the waste gas is saturated with a finely atomized spray of an additive, such as water, delivered by an atomizing nozzle 16 which is held in place by a nozzle plate 14, and which is shown diagrammatically to include a pair of opposed nozzles.
  • an additive such as water
  • the saturated gas then passes into the housing 24.
  • the electrostatic precipitator 20 produces an electrical f eld through which the saturated waste gas must pass.
  • particles in the waste gas become electrically charged.
  • the particles adhere to an oppositely charged electrodes of the precipitator and are thereby removed from the waste gas stream.
  • the waste gas now cleaned of the particles, passes through a demister DM, having an array of baffles, such as baffle 240, for removing moisture from the treated gas.
  • the clean gas generally follows a flowpath P into a cylindrical clean air conduit 26 connecting an outlet 28 to the interior of the housing 24.
  • water under pressure is delivered through the atomizing nozzle 16, to saturate the gas.
  • the water washes particle collecting surfaces, thereby sweeping away particles adhering thereto.
  • the water separated from the gas in the demister DM flows into a funnel shaped portion 48 and, as a sludge containing particles removed from the waste gas stream flows out through a port 33.
  • Water delivery may be continuous or intermittent, depending on particle loading.
  • the electrostatic precipitator 20 has a plurality of inner and outer concentric oppositely poled elongated electrodes, such as inner and outer electrodes 35A and 31, respectively, disposed within the interior of the housing 24 and extending in the direction of movement of the sprayed gas flowing therethrough.
  • a power supply P applies a high voltage to the inner electrodes, and the outer electrodes are grounded, to cause a corona discharge to occur between the concentric electrodes.
  • the outer electrodes are all similar to one another, and only the outer electrode 31 will now be described in greater detail.
  • the outer electrode 31 is in the form of an elongated collector tube.
  • the tube 31 is oriented so that the gas flow path through the system 10 is along the longitudinal axis of the electrode.
  • the tube 31 is mechanically and electrically supported between top and bottom plates 57 and 59.
  • the collector tube 31 collects charged particles during system 10 operation. It may have an internal diameter ranging from about 8 inches to about 12 inches. In a preferred system actually constructed, the collector tube 31 has an internal diameter of about 10 inches, and is about ten feet in length.
  • a bus bar 42 is disposed within the housing 24 and is electrically isolated from connection therewith by insulators, such as the insulator 43. Suspended from the bus bar 42 and electrically connected are the individual like inner electrodes, such as the inner electrode 35A.
  • the inner electrodes are each fixed in concentric alignment with the corresponding collector tubes, and extend from the bus bar 42 terminating at their bottom distal ends (not shown) spaced above the plate 59.
  • the high voltage power supply P is electrically connected to a power supply input 44 for delivery of negative electrical energy to the bus bar 42 to create an electrostatic field between the inner electrodes and the grounded outer electrode tubes. It has been determined that the system works well with a field strength of about 6KV/cm, for effective particle removal.
  • the ends of the bus bar 42 are positioned within a pair of similar insulator purge boxes 46 and 46A.
  • the insulator box 46 has the power supply input 44, and an inlet 47 through which heated dry air may be delivered into the hollow interior of the box 46 and out its outlet 47A connected in fluid communication with the interior of the housing 24, for purging the box 46 of moisture and for maintaining the bus bar 42 in a substantially dry state.
  • the other box 46A also is purged in a similar manner.
  • the system 10 is substantially self cleaning during the particle removal operation.
  • the system 10 may be adapted so that the surfaces of the electrodes can be cleaned of particles in an easy and convenient manner, without disassembly of the system.
  • water under pressure is delivered through a plurality of nozzles, such as a nozzle 34.
  • the nozzles, such as the nozzle 34 are connected in fluid communication with a manifold 37 disposed in the upper portion 22 of the housing 24 upstream of the precipitator 20.
  • An external connector 36 is adapted for receiving a water delivery line (not shown) for admitting water or other suitable cleaning liquid under pressure to the manifold 37.
  • the nozzles 34 direct the water, under pressure, downwardly through the interior of the housing 24 for cleaning the system by removing particles from the electrodes.
  • the electrode 35A is in the form of an electrically conductive elongated rod or discharge mast 32 axially aligned with, and centered disposed within, its collector tube 31.
  • Discharge discs 38, 39 and 41 are mounted on the mast electrode 32, in a spaced apart relationship along the top portion thereof. In the system actually constructed, the discs are spaced at approximately one foot intervals.
  • the discharge discs 38, 39 and 41 are electrically and mechanically connected to the mast 32 so that the plane of the disc is transverse to the longitudinal axis of the electrode 32.
  • Each discharge disc is thin, and in the constructed system, is approximately 1/8 inch thick.
  • the discs are preferably constructed of noncorrosive electrically conductive material such as stainless steel. It is recognized, of course, that materials such as zirconium and titanium are also suitable.
  • the disc has a large number of radially extending sharply pointed projections or points, such as the points 73 and 77 to enable an individual corona discharge to be established between the radial discharge points and the inner surface of the collector tube.
  • a uniformly distributed electrostatic field is established, due to the sharpness of the points and the relatively large number thereof for a given circumference of the disc.
  • the diameter of the disc is only somewhat greater than the diameter of the mast, to provide only a small impedance to the flowing wet gas therepast.
  • each discharge disc is able to not only provide a uniformly distributed electrostatic field, but also a low impedance to gas flow.
  • the precipitator is highly efficient and effective in its particle removing operation
  • Arcuate shaped interconnecting web portions such as the portion 75, are concave in shape, and join the discharge points along the peripheral edge of the disc.
  • each of the points such as the point 73, has a pair of curved opposite side edges 73A and 73B.
  • the side edges 73A and 73B form an included angle T of between 55° and 65", with a preferred range of 59° to 61" and a most preferred angle of 60°.
  • each of the side edges 73A and 73B has a radius of curvature ranging from about 0.009 inches to about 0.111 inches, with a preferred range of about 0.110 inches.
  • the disc 38 has a large number of points disposed along its periphery. In the constructed system, the disc has 50 points arrayed along the periphery of the disc 38.
  • the corona discharge thus produced is very stable and the electrostatic field is more efficient in particle removal. In addition, field fluctuations are significantly diminished.
  • the relative dimensions between the discharge disc 38 and the mast electrode 32 are found to be critical.
  • the discharge disc should be sufficiently small to present low impedance to the gas flow around it, yet capable of maintaining a high intensity uniform field. It has been found that in the discharge disc 38, as best seen in FIG.
  • a tip to tip diameter dimension D is between about 1.575 to about 1.825 times the rod diameter d with a preferred range of about 1.64 to about 1.76, and a most preferred dimension D being about 1.7 times the diameter d.
  • the disc 38 has a dimension D of approximately 3.4 inches, while the rod diameter d is approximately 2.0 inches.
  • the 1.7 ratio is critical. If, for example, - is too large, the disc presents too high an impedance to gas flow, and thus precipitator efficiency is reduced to an unacceptable level. Also, when the disc diameter is too large for a given diameter mast, sparks (and not the desired corona discharge) are established between the inner and outer electrodes, at too low a voltage. Also, in small diameter masts, relative to the size of the diameter of the disc, unwanted coronal discharges from the mast itself are produced, when, of course, it is desirable that the discharge emanate from the disc electrode. Such discharges or sparks are wasteful of electrical energy and, in addition, lead to an inefficient particle removal operation.
  • the disc/mast relationship _ - ⁇ "too small, inefficient system performance results because the electrostatic field between the disc tip and the tube wall is not readily established and maintained in a desired manner.
  • the electrode in the constructed system, has an inside diameter of ten inches.
  • a preferable mast diameter is about 2 inches for maintenance of a uniform electrostatic field.
  • the collector tube 31 has an internal diameter of about 10 inches, application of the formula reveals that a suitable distance S would be from about 3.0 inches to 3.6 inches with a preferred range being about 3.2 to about 3.4 inches and a most preferred distance about 3.3 inches.
  • the collector tube 31 and the mast 32 are made of suitable corrosion resistant, conductive materials such as stainless steel.
  • the precipitator 120 is generally similar to the precipitator 20, with the exception of the configuration of the collector electrode 131.
  • FIG. 4A there is shown for illustration purposes, only one of a pair of concentric electrodes 135 and 131, respectively.
  • the other like electrode pairs and the other portions of the precipitator 120 are not shown for sake of simplicity.
  • the inner electrode 135 is similar to the inner electrode 35A of FIG. 1, and includes a mast 132 having spaced apart discharge discs, such as the disc 138, disposed thereon.
  • the electrode 131 is generally rectangular in cross section throughout its length and is comprised of four walls 141-144.
  • the transverse cross sectional shape is preferably square. While the electrode 131 operates in a generally similar manner to the electrode 31 of FIG. 1, and is generally similar in particle removal function, the configuration of the walls 141-144 render the electrode 131 less expensive to manufacture than the cylindrically shaped electrode 31 of FIG. 1.
  • a mast electrode 132 having a discharge electrode 138 mounted thereon is centrally and coaxially positioned within the squared tubular collector electrode 131.
  • FIG. 4 there is shown another electrostatic precipitator 62C which is constructed according to the present invention.
  • the precipitator 62C is generally similar to the precipitator 20 of FIG. 1 in structure and particle removal function, except for the shape of the discharge discs. Thus, only a portion of the disc and the mast are illustrated.
  • the precipitator 62C includes an inner electrode E having a mast 55C and a discharge disc 38C.
  • a large number of discharge points 81 are arrayed along the peripheral edge of the discharge disc 38C.
  • the discharge points 81 are each defined by a generally curved side edge and a straight side edge to provide an asymmetrical discharge point.
  • a point 82 is defined by a curved side edge 83A and a generally straight side edge 83B.
  • the electrode disc 32 of FIG. 1 it is critical to have a large number of discharge points arrayed around the periphery of the disc.
  • the preferred number of points may be calculated according to the foregoing formula.
  • FIG. 5 there is shown yet another electrostatic precipitator 62D which is constructed according to the present invention.
  • the precipitator 62D is generally similar to the precipitator 20 of FIG. 1 in structure and particle removal function, except for the shape of the inner electrode discharge discs.
  • the precipitator 62D of FIG. 5 includes an inner electrode F having a mast electrode 55D and a discharge disc 38D.
  • the disc 38D includes a plurality of peripherally arrayed, radially extending points 86 disposed on the outer edge of the disc 38D. Each point is defined by a pair of generally straight, unequal length side edges forming a V shaped discharge point.
  • a point 86A includes a side edge 84, which is approximately twice the length of its other side edge 85.
  • the precipitator 62D and as discussed with regard to the disc electrode 32 of FIG. 1, it is desirable to have a large number of points arrayed around the periphery of the disc 38D.
  • the preferred number of points may be calculated according to the foregoing formula.
  • an electrostatic precipitator 62E is illustrated and is constructed according to the present invention.
  • the precipitator 62E is generally similar to the precipitator 20 of FIG. 1 in structure and particle removal function, except for the shape of the discharge disc.
  • the precipitator includes an inner electrode I having a mast electrode 55E and a discharge disc 38E.
  • the disc 38E includes a plurality of spike shaped discharge points, such as the discharge point 88, extending radially outwardly from the discharge disc 38E in a plane transverse to the axis of the mast electrode 55E.
  • the length 1 of the spike 86 is approximately equal to the width w of an annular hub H of the disc electrode 38E.
  • the electrostatic precipitator of the present invention has many significant advantages. In the first place, it produces a high intensity ionizing electrode configuration to concentrate the charging field in the zone between the disc and the collecting tube electrode. Thus, the performance of the system exceeds conventional designs and results in more efficient operation. Further, the disc configuration provides excellent collection of particulate matter over a broad spectrum of sizes. While particular embodiments of the present invention have been disclosed, it is to be understood that various different modifications are possible and are contemplated within the true spirit and scope of the appended claims. There is no intention, therefore, of limitations to the exact abstract or disclosure herein presented.

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  • Electrostatic Separation (AREA)

Abstract

Séparateur électrostatique à l'état humide (20) possédant un boîtier cylindrique (24), une entrée située dans une partie supérieure (22), une buse de pulvérisation, des électrodes concentriques intérieure et extérieure (35A, 31), l'électrode extérieure (31) se présentant sous la forme d'un tube collecteur supporté par des plaques supérieure et inférieure (57, 59). Les électrodes intérieures (35A) sont supportées par une barre collectrice (42) reliée à une source d'énergie (P). Une sortie (28) est reliée à l'intérieur du boîitier (24).
PCT/US1992/002999 1991-04-24 1992-04-10 Separateur electrostatique a l'etat humide et procede d'utilisation WO1992019380A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US69067291A 1991-04-24 1991-04-24
US690,672 1991-04-24

Publications (1)

Publication Number Publication Date
WO1992019380A1 true WO1992019380A1 (fr) 1992-11-12

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PCT/US1992/002999 WO1992019380A1 (fr) 1991-04-24 1992-04-10 Separateur electrostatique a l'etat humide et procede d'utilisation

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WO (1) WO1992019380A1 (fr)

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002085524A1 (fr) * 2001-04-24 2002-10-31 Koenig Ag Dispositif et procede pour epurer des rejets gazeux charges de polluants
WO2005007295A1 (fr) 2003-07-18 2005-01-27 Turbosonic Inc. Hotte d'elimination de gouttelettes
WO2005097297A1 (fr) * 2004-04-09 2005-10-20 Turbosonic Inc. Controle de pollution dans un sechoir de produits en bois
WO2006086886A1 (fr) 2005-02-18 2006-08-24 Turbosonic Inc. Conception d'electrodes en pylone
FR2983093A1 (fr) * 2011-11-28 2013-05-31 Commissariat Energie Atomique Dispositif de collecte electrostatique de particules en suspension dans un milieu gazeux
CN103203284A (zh) * 2013-04-07 2013-07-17 熊天渝 湿式静电除尘器
US9387487B2 (en) 2011-03-28 2016-07-12 Megtec Turbosonic Inc. Erosion-resistant conductive composite material collecting electrode for WESP
CN107213988A (zh) * 2017-06-09 2017-09-29 哈尔滨恒昇电站设备有限公司 带尖角板式芒刺放电功率可控的阴极线及其制备方法
US20180200671A1 (en) * 2017-01-13 2018-07-19 EnviroEnergy Solutions, Inc. WET ELECTROSTATIC GAS CLEANING SYSTEM WITH NON-THERMAL PLASMA FOR NOx REDUCTION IN EXHAUST
US10239016B2 (en) 2016-12-07 2019-03-26 Nuorganics LLC Systems and methods for nitrogen recovery from a gas stream
US10513466B2 (en) 2017-01-16 2019-12-24 Nuorganics LLC System and method for recovering nitrogenous compounds from a gas stream
EP3504007A4 (fr) * 2016-08-26 2020-04-22 Plasma Shield Pty Ltd Appareil de purification de gaz
US10744456B2 (en) * 2017-01-13 2020-08-18 EnviroEnergy Solutions, Inc. Wet electrostatic gas cleaning system with non-thermal plasma for NOx reduction in exhaust
US11027289B2 (en) 2011-12-09 2021-06-08 Durr Systems Inc. Wet electrostatic precipitator system components

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4194888A (en) * 1976-09-24 1980-03-25 Air Pollution Systems, Inc. Electrostatic precipitator
US4247307A (en) * 1979-09-21 1981-01-27 Union Carbide Corporation High intensity ionization-wet collection method and apparatus
US4389225A (en) * 1981-03-26 1983-06-21 Peabody Process Systems, Inc. Electrostatic precipitator having high strength discharge electrode

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4194888A (en) * 1976-09-24 1980-03-25 Air Pollution Systems, Inc. Electrostatic precipitator
US4247307A (en) * 1979-09-21 1981-01-27 Union Carbide Corporation High intensity ionization-wet collection method and apparatus
US4389225A (en) * 1981-03-26 1983-06-21 Peabody Process Systems, Inc. Electrostatic precipitator having high strength discharge electrode

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002085524A1 (fr) * 2001-04-24 2002-10-31 Koenig Ag Dispositif et procede pour epurer des rejets gazeux charges de polluants
WO2005007295A1 (fr) 2003-07-18 2005-01-27 Turbosonic Inc. Hotte d'elimination de gouttelettes
US7160348B2 (en) 2003-07-18 2007-01-09 Turbosonic Inc. Mist elimination hood
US7402196B2 (en) 2003-07-18 2008-07-22 Turbosonic Inc. Mist elimination hood
WO2005097297A1 (fr) * 2004-04-09 2005-10-20 Turbosonic Inc. Controle de pollution dans un sechoir de produits en bois
US7160358B2 (en) * 2004-04-09 2007-01-09 Turbosonic Inc. Pollution control in wood products dryer
WO2006086886A1 (fr) 2005-02-18 2006-08-24 Turbosonic Inc. Conception d'electrodes en pylone
EP1850965A4 (fr) * 2005-02-18 2011-02-23 Turbosonic Inc Conception d'electrodes en pylone
US8092576B2 (en) 2005-02-18 2012-01-10 Turbosonic Inc. Mast electrode design
US9387487B2 (en) 2011-03-28 2016-07-12 Megtec Turbosonic Inc. Erosion-resistant conductive composite material collecting electrode for WESP
FR2983093A1 (fr) * 2011-11-28 2013-05-31 Commissariat Energie Atomique Dispositif de collecte electrostatique de particules en suspension dans un milieu gazeux
US11027289B2 (en) 2011-12-09 2021-06-08 Durr Systems Inc. Wet electrostatic precipitator system components
CN103203284A (zh) * 2013-04-07 2013-07-17 熊天渝 湿式静电除尘器
EP3504007A4 (fr) * 2016-08-26 2020-04-22 Plasma Shield Pty Ltd Appareil de purification de gaz
US10744515B2 (en) 2016-08-26 2020-08-18 Plasma Shield Pty Ltd Gas purifying apparatus
US10239016B2 (en) 2016-12-07 2019-03-26 Nuorganics LLC Systems and methods for nitrogen recovery from a gas stream
US20180200671A1 (en) * 2017-01-13 2018-07-19 EnviroEnergy Solutions, Inc. WET ELECTROSTATIC GAS CLEANING SYSTEM WITH NON-THERMAL PLASMA FOR NOx REDUCTION IN EXHAUST
US10744456B2 (en) * 2017-01-13 2020-08-18 EnviroEnergy Solutions, Inc. Wet electrostatic gas cleaning system with non-thermal plasma for NOx reduction in exhaust
US10513466B2 (en) 2017-01-16 2019-12-24 Nuorganics LLC System and method for recovering nitrogenous compounds from a gas stream
US10934223B2 (en) 2017-01-16 2021-03-02 Nuorganics LLC System and method for recovering nitrogenous compounds from a gas stream
CN107213988A (zh) * 2017-06-09 2017-09-29 哈尔滨恒昇电站设备有限公司 带尖角板式芒刺放电功率可控的阴极线及其制备方法

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