WO2012139642A1 - Appareil d'élimination de matière particulaire dans un gaz - Google Patents

Appareil d'élimination de matière particulaire dans un gaz Download PDF

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Publication number
WO2012139642A1
WO2012139642A1 PCT/EP2011/055839 EP2011055839W WO2012139642A1 WO 2012139642 A1 WO2012139642 A1 WO 2012139642A1 EP 2011055839 W EP2011055839 W EP 2011055839W WO 2012139642 A1 WO2012139642 A1 WO 2012139642A1
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WO
WIPO (PCT)
Prior art keywords
electrode
additional
gas
ionization
particulate matter
Prior art date
Application number
PCT/EP2011/055839
Other languages
English (en)
Inventor
Thomas Hammer
Sridhar Gururaja Rao
Amit Kumar SINGH PARIHAR
Original Assignee
Siemens Aktiengesellschaft
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 Siemens Aktiengesellschaft filed Critical Siemens Aktiengesellschaft
Priority to PCT/EP2011/055839 priority Critical patent/WO2012139642A1/fr
Publication of WO2012139642A1 publication Critical patent/WO2012139642A1/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
    • B03C3/02—Plant or installations having external electricity supply
    • B03C3/04—Plant or installations having external electricity supply dry type
    • B03C3/14—Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
    • B03C3/15—Centrifugal forces
    • 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
    • B03C3/025—Combinations of electrostatic separators, e.g. in parallel or in series, stacked separators, dry-wet separator combinations
    • 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
    • B03C3/14—Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
    • 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
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/40—Electrode constructions
    • B03C3/45—Collecting-electrodes
    • B03C3/49—Collecting-electrodes tubular
    • 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
    • B03C3/86—Electrode-carrying means

Definitions

  • Apparatus for removal of particulate matter from a gas The present invention relates to removal of particulate mat ⁇ ter from a gas, and in particular, to an improvement in the use of centrifugal action and electrostatic force for parti ⁇ cle removal from a gas .
  • Fuel and flue gas generated from the thermo-chemical conver ⁇ sion processes mostly contain dust particles having a wide range of sizes. These gases should be free of dust particles either to meet the end application or to meet the environmental norms .
  • Cyclone separators are well-known devices for removing par ⁇ ticulates from a gas stream.
  • a stream of parti ⁇ cle-laden raw gas is introduced tangentially into a cyclonic separation zone so that the particles experience a centrifu- gal force in the ensuing swirling flow.
  • the particles are collected on the outer wall of the separation zone and a re ⁇ sultant clean gas exits from a central exhaust duct.
  • Cyclones are considered suitable for removing particles larger than 10 ym from a gas stream due to centrifugal force, which is re- sponsible for particle separation.
  • cyclones can be designed to remove sub-micron particles but the associated pressure drop would be prohibitively high resulting in considerable power consumption. Also, depending on the extent of dust loading i.e. concentration of dust particles, there is a possibility of choking at the entry of the cyclone. Hence, the best cyclone design is essentially a trade-off between performance i.e. collection efficiency and the allowable pressure drop.
  • pollu ⁇ tion control equipment including cyclone, scrubbers, electro ⁇ static precipitators (ESP) are generally employed. In this arrangement, the cyclone removes the larger particles from the gas to reduce load on the subsequent equipment like scrubber, ESP and filters where removal of the smaller parti ⁇ cles takes place.
  • the object of the present invention is to improve the parti ⁇ cle separation efficiency of an apparatus involving centrifu ⁇ gal action and electrostatic force.
  • the ionization zone As the ionization zone is provided at the inlet of the cas ⁇ ing, all the particulate matter in the contaminated gas is charged or ionized in the ionization zone. As all the par ⁇ ticulate matter is charged, the electric field generated in the separation zone forces the charged particulate matter to migrate towards the wall of the casing. Further the electric field assists in preventing re-entrainment of particles re ⁇ moved from the wall of the casing due to drag forces. Thus, the particulate matter is separated from the contained gas more efficiently to produce the partially clean gas.
  • the ionization electrode is disposed within the inlet of the casing, the compact design of the apparatus can be achieved.
  • the separation electrode comprises the outlet (23) , wherein the outlet (23) is electrically con ⁇ ductive.
  • the apparatus further comprises an feed-through arrangement (29) for passing the co ⁇ rona initiation electrical potential to the ionization zone, the feed-through arrangement being electrically insulated from the casing and being disposed in a third flow-path of the partially clean gas. This assists in insulting the feed- through arrangement in the third flow-path of the partially clean gas and thus prevent short circuit of the insulation as the deposition of particulate matter on the surface of the insulation is reduced.
  • the ionization zone comprises an ionization electrode for producing the corona dis- charge.
  • Ionization electrode comprises means for producing the corona discharge.
  • the ionization electrode is electrically connected to the feed-through arrangement. The feed-through arrangement provides the corona initiation elec ⁇ trical potential to the ionization electrode.
  • the ionization electrode comprises at least one rod and at least one sharp edged mem ⁇ ber electrically connected to the at least one rod. Sharp edges enable in producing efficient corona discharge and also reduce the electrical potential required for producing the corona discharge.
  • the separation electrode is electrically connected to the feed-through arrangement.
  • the electrical potential provided to the ionization electrode for producing the corona discharge can be provided to the separation electrode.
  • the ionization electrode is electrically connected to the separation electrode.
  • the ionization electrode can be electrically connected to the separation electrode and the corona initiation electrical potential can be passed on to the separation electrode.
  • the casing is electrically grounded and the electrical field is created between the ion ⁇ ized particulate matter and the casing, and the additional electric field is created between the separation electrode and the casing.
  • the casing being grounded enables in produc ⁇ ing the electrical field and the additional electrical field.
  • the apparatus further com- prises an additional electrode disposed inwardly in the out ⁇ let, the additional electrode extending out of the outlet such that an additional volume of the additional electrical field can be created. This assists in enhanced separation of charged particulate matter.
  • the additional electrode is electrically connected to the feed-through arrangement. This provides the electrical potential being provided for produc ⁇ ing the corona discharge to the additional electrode.
  • the additional electrode ex- tends into at least a portion of the separation zone. This enables in increasing the volume of the additional electrical field, and thus, prevents re-entrainment of the particulate matter more efficiently.
  • the apparatus further com ⁇ prises an additional ionization zone along the third flow- path of the partially clean gas for ionizing the particulate matter remaining in the partially cleaned gas by producing an additional corona discharge in the flow-path 25.
  • the particulate matter remaining in the partially clean gas can be charged electrically and thereafter removed at a subse ⁇ quent separation stage.
  • the additional ionization zone comprises a first portion of the additional electrode.
  • the additional corona discharge for ionizing or charging the particulate matter can be produced by the first portion of the additional electrode. Additionally, extending the first portion of the additional electrode into the additional ioni- zation zone enables in easy construction without the require ⁇ ment of an additional structure for producing the additional corona discharge.
  • the additional ionization zone comprises an additional ionization electrode 47 electri ⁇ cally connected to the feed-through arrangement 27 for pro ⁇ ducing the additional corona discharge in the flow-path 25.
  • FIG 2 illustrates an ionization electrode of an apparatus according to another embodiment
  • FIG 3 illustrates a top view of an apparatus according to an embodiment herein
  • FIG 4 illustrates an apparatus for removal of particulate matter from a gas according to another embodiment
  • FIG 5 illustrates an apparatus for removal of particulate matter from a gas according to yet another embodi- ment, wherein the apparatus comprises an additional ionization zone, illustrates an apparatus according to yet another embodiment herein, illustrates a second portion of a second electrode extending into an additional ionization zone ac ⁇ cording to an embodiment here, and illustrates an apparatus 10 according to yet an ⁇ other embodiment herein.
  • the illustrated apparatus 1 provides a compact solution combining a cyclone electrostatic precipitation to increase the overall particle collection efficiency with increased insulation by reducing precipitation of charged particulate matter on the insula ⁇ tors.
  • the apparatus 1 comprises a casing 3 having an inlet 5 for receiving a contaminated gas 7a that comprises particu ⁇ late matter.
  • the gas 7a to be cleaned may include a hot gas, such as an industrial flue gas, or a fuel gas, such as pro ⁇ ducer gas or synthetic gas, derived from biomass, coal or any other solid fossil fuel.
  • the particulate matter contained in the contaminated gas 7a may include, for example ash and dust particles in a wide range of sizes, including large sized particles (> 10 ym) , intermediate sized particles (> 1 ym) and small sized particles (sub-micron) .
  • the inlet 5 is designed to induce a swirl to the incoming particle-laden gas 7a as it is introduced tangentially into the casing 3.
  • the particulate matter con ⁇ tained in the contaminated gas 7a is ionized by an ioniza ⁇ tion zone 9 disposed along a first flow-path 11 of the con ⁇ taminated gas 7a.
  • the inlet 5 includes a duct, illustrated as the inlet duct 6a.
  • the ioni- zation zone 9 comprises means for charging or ionizing the particulate matter in the contaminated gas 7a.
  • an ionization electrode 13 is disposed inside the inlet duct 6 along the first flow-path 11.
  • the ionization electrode 13 is disposed such that a gap is maintained between the ionization electrode 13 and the wall 6a of the inlet duct 6 in the ionization zone 9.
  • the ionization electrode 13 can be disposed substan ⁇ tially coaxially and can be substantially centered in the ionization zone 9.
  • the ionization electrode 13 is connected to a high-voltage source, preferably of negative polarity, which is capable of providing a corona initiation electrical potential.
  • the ionization electrode 13 comprises a metallic rod.
  • the ionization electrode 13 may com ⁇ prise a plurality of metallic rods and additional electri- cally conductive members having sharp edges, such as thin sheets, being connected to one or more of these metallic rods, to aid in the production of a corona discharge.
  • the ionization electrode 13 is disposed inside the inlet 5, all the particulate matter contained in the gas 7a is ionized.
  • the ionization elec ⁇ trode 13 can be disposed substantially at the end of the inlet 5, such that, the flow-path of the contaminated gas 7a comprising the charged particulate matter inside the inlet is minimum. This further enables in avoiding precipitation of the charged particulate matter on the wall 6a of the inlet duct 6.
  • the gas flowing out of the ionization zone 9 thus comprises charged or ionized particulate matter.
  • This charged or ion ⁇ ized particulate matter is separated from the gas subse ⁇ quently at a separation zone 15 along a second flow-path 17 downstream of the inlet 5.
  • the swirl imparted to the gas 7a tends to concentrate the charged or ionized particulate mat- ter, particularly large sized particles towards the wall 19 of the casing 3 by centrifugal action.
  • the wall 19 of the casing 3 can be electrically grounded. As the wall 19 of the casing 3 is grounded, an electric field is produced between the ionized or charged particulate matter of the gas 7a and the wall 19 of the casing 3.
  • This electric field fur ⁇ ther assists in migration of charged or ionized particles to ⁇ wards the grounded wall 19 of the casing 3.
  • the combination of the centrifugal action and the electrical field increases the tendency of the particulate matter, particularly large sized particles, to concentrate towards the wall 19 of the casing 3, to produce a resultant partially clean gas 7b.
  • an ad ⁇ ditional electric field can be produced in at least a portion of the separation zone 15.
  • an electrically conducting separation electrode 22 can be disposed in the portion of the separation zone 15 for producing the additional electric field.
  • the separation electrode 22 can be electrically connected to an electric potential provided to the ionization electrode 13 of the ionization zone 9 for pro ⁇ ducing the corona discharge.
  • an additional electric field is created between the wall 19 of the casing 3 and the separation electrode 22.
  • the additional electrical field results in additional electrostatic force acting on the charged or ionized particulate matter, and thus, further as ⁇ sists in migration of the charged or ionized particles to ⁇ wards the wall 19 of the casing 3.
  • the additional electric field assists in preventing re-entrainment of particles re ⁇ moved from the wall 19 of the casing 3 due to drag forces.
  • the particles are very likely charged or will be charged due to agglomeration with charged particles in the second flow- path 17, the particles removed from the wall 19 due to drag forces will be forced to migrate towards the wall 19 again due to the additional electric field.
  • re-entering of the particles separated from the gas 7b is prevented and this provides increase efficiency in removing the particulate mat ⁇ ter from the gas 7a.
  • the outlet 23 also known as a vortex finder, electrically insulated with the casing 3, is disposed radially inwardly in a third flow-path 25 of the partially clean gas 7b exiting the casing 3.
  • Advan ⁇ tageously, the outlet 23 can be in the form of a duct as il- lustrated in FIG 1.
  • the outlet 23 is insulated from the casing 3 via the insulators 27a and 27b.
  • the outlet 23 can be made of an electrically con ⁇ ductive material, for example, the outlet 23 can be made of the same material of which the casing 3 is made of.
  • both the casing 3 and the outlet 23 can be made of the same material.
  • the outlet 23 can be made of an insulating material also.
  • the outlet 23 is made of an electrically con ⁇ ductive material and the separation electrode 22 comprises the outlet 23 for producing the additional electric field in the separation zone 15.
  • the additional electric field in the separation zone is produced between the outlet 23 and the wall 19 of the casing 3. This eliminates the requirement of disposing an additional structure for producing the addi ⁇ tional electric field.
  • the outlet 23 is con ⁇ ductive and electrically connected to the electrical poten ⁇ tial provided to the ionization electrode 13 for producing the corona discharge
  • the ionization electrode 13 can be electrically connected to the outlet 23 for receiving the co ⁇ rona initiation electrical potential.
  • the partially clean gas 7b exits the casing 3 via the outlet 23, as illustrated by the third flow-path 25.
  • the separation electrode 22 can comprise an additional electrically conducting structure and can be disposed in the separation zone 15.
  • the separation electrode 22 can be disposed outside the outlet 23 along the length of the outlet 23.
  • the corona initiation electrical potential to the ionization electrode 13 of the ionization zone 9 is provided from an feed-through arrangement 29 disposed in the third flow-path 25 of the partially clean gas 7b.
  • the feed-through arrange ⁇ ment 29 is insulated from the casing 3 using an insulator 30.
  • the insulator 30 can advan ⁇ tageously be mounted in the third flow-path 25 of the par ⁇ tially clean gas 7b. Since, the insulator 30 encounters only the partially clean gas 7b, precipitation of particulate mat- ter on surfaces of the insulator 30 is reduced.
  • the feed-through arrangement 29 can extend into the outlet 23 for passing the corona initiation electrical poten ⁇ tial to the ionization electrode 13 of the ionization zone 9.
  • the feed-through arrangement 29 can be disposed coaxially in the outlet 23 and the ionization electrode 13 can be electrically connected to the feed-through arrangement 29.
  • the feed-through arrangement 29 can be electrically connected to the outlet 23, referenced as 31, and the ionization elec ⁇ trode 13 can be electrically connected to the outlet 23.
  • the separation electrode comprises the additional structure
  • the length of the structure can be such that it extends into the lower part of the casing 3.
  • the separa ⁇ tion electrode can comprise an additional electrode 33 dis- posed inwardly in the outlet 23.
  • the additional electrode 33 can be mounted such that it is substantially at the centre of the outlet 23 or can be mounted along the side of the outlet 23.
  • the end 34 of the additional electrode 33 proximal to the bottom of the casing 3 can be blunt as only an electric field is to be produced with re ⁇ spect to the electrically grounded casing 3 and no corona discharge is to be produced.
  • the additional electrode 33 can be electrically connected to the outlet 23 if the outlet is electrically con- nected to the feed-through arrangement 29.
  • an increased volume of the additional electric field can be created in the separation zone 15 between the additional electrode 33 and the wall 19 of the casing 3.
  • the more the ad- ditional electrode 33 is extended into the separation zone 15, the volume of the additional electric created can be in ⁇ creased.
  • the increased volume of the additional electric field in the separation zone 15 provides more efficient pre- vention of the re-entrainment of the separated particulate matter .
  • the additional electrode 33 can be electrically connected to the feed-through arrange ⁇ ment 29.
  • the increased volume of the ad ⁇ ditional electric field will be created by the electric field produced by the additional structure and the second electrode 33.
  • the embodiments described herein charge all the particulate matter contained in the contaminated gas 7a and thereafter the charged or ionized particulate matter are separated from the contaminated gas 7a by using centrifugal action and by means of electrostatic forces.
  • the charged particulate matter will be forced to migrate towards to the wall 19 of the cas ⁇ ing as the wall 19 of the casing 3 is grounded. Additionally, this prevents the deposition of the charged particulate mat ⁇ ter onto the surface of the insulator 27 insulating the out- let 23 from the casing 3.
  • the additional elec ⁇ tric field produced by the separation electrode 22 in the separation zone 15 further assists the migration of the charged particulate matter towards the wall 19 of the casing.
  • the additional electric field will prevent the re-entrainment of the particulate mat ⁇ ter removed from the contaminated gas 7a to produce a result ⁇ ing partially clean gas 7b.
  • the particulate matter in the gas 7a is more efficiently removed to produce the par ⁇ tially clean gas 7b.
  • the insulation of the feed-through arrangement 25 can be disposed in the third flow-path 25 of the partially clean gas 7b.
  • the insulator 30 is mounted in the third flow-path 25 of the partially clean gas 7b, deposition of particulate matter onto the surface of the insulator 30 is reduced. The particulate matter in the partially clean gas is reduced as a portion of the particulate matter is separated from the contaminated gas 7a in the separation zone 15.
  • the ionization zone 9 is disposed inside the inlet 5 an additional separate ionization stage is not required prior to the inter 5 of the casing 3. This achieves in reducing the footprint.
  • the mount ⁇ ing of the additional electrode 33 and the electrical connec ⁇ tion to the additional electrode 33 is simplified as the ad- ditional electrode 33 is connected to the same electrical po ⁇ tential as the feed-through arrangement 29, thus, avoiding complex insulation requirement.
  • FIG 2 illustrates an ionization electrode of the apparatus 1 according to another embodiment.
  • the ionization electrode 13 can comprise sharp edged members 13a along the length of the ionization electrode 13.
  • the sharp edges members 13a can be a plurality of discs arranged along the length of the ionization electrode 13. These sharp edged members 13a reduce the corona initiation electrical potential required for producing the corona discharge.
  • FIG 3 illustrates a top view of the apparatus 1 of FIG 1 ac ⁇ cording to an embodiment herein.
  • casing 3 is insulated from the outlet 23 using the insulators 27, illustrated as the hatched por ⁇ tion.
  • the feed-through arrangement 29 is electrically con ⁇ nected to the outlet 23, referenced as 31, insulated from the casing 3 through the insulator 30, and the ionization elec- trode 13 is electrically connected to the outlet 23.
  • FIGS 2-6 wherein like reference signs refer to like elements.
  • FIG 4 illustrates the apparatus 1 according another embodi ⁇ ment herein.
  • the outlet 23 can be insulated from the casing 3 using a single insulator 27. As illustrated in the example of FIG 4, the insulator 27 can be disposed coaxially around the outlet 23 to insulate the outlet 23 from the casing 3. Thus, the insulation of the outlet 23 from the casing 3 can be achieved depending on the construction of the casing 3.
  • the apparatus 1 comprises an additional ionization zone 35 for ionizing or charging the particulate matter remaining in the partially clean gas and a particle collection zone 39 for removing the charged remaining particulate matter. While the separation zone 15 is ef ⁇ fective for removing large sized particles, smaller and in ⁇ termediate sized particles would experience lesser centrifu- gal force or may not be ionized appropriately and therefore would remain with the partially clean gas 7b. Removal of such remaining small and intermediate sized particulate matter from the partially clean gas 7b is carried out by the addi ⁇ tional ionization zone 35 and the particle collection zone 39.
  • the additional ionization zone 35 is disposed along the third flow-path 25 of the partially clean gas 7b and comprises means for charging or ionizing the particulate matter remaining in the partially clean gas 7b. Accordingly, in the present example, the additional ioniza ⁇ tion zone 35 is illustrated as being disposed in the outlet 23. According to an aspect, the means for charging or ionizing the particulate matter can be achieved, by extending the additional electrode 33 into the additional ionization zone 35 as illustrated in the shown example of FIG 5. The first portion 37 of the additional electrode 33 extended into the additional ionization zone 35 can comprise sharp edges to aid the production of the corona discharge.
  • the first portion 37 of the additional electrode 33 produces a corona discharge in the third flow-path 25 of the partially clean gas 7b to ion ⁇ ize or charge the particulate matter remaining in the par- tially clean gas 7b.
  • the cross-sectional area of the flow-path 25, i.e., of the outlet 23 is designed to be sufficiently small such that the gas flowing there through has a high velocity (i.e., high energy), which, in turn increases the particle charging efficiency.
  • the outlet 23 is maintained at the same electric poten ⁇ tial as the additional electrode 33, the possibility of par ⁇ ticle collection within the outlet 23 is reduced.
  • the gas 7b flowing out of the additional ionization zone 35 thus comprises charged or ionized particulate matter.
  • This charged or ionized particulate matter is separated from the gas 7b subsequently at a particle collection zone 39.
  • the particle collection zone 39 can be formed by disposing an ad ⁇ ditional casing 41 in the fourth flow-path 43 of egress of the partially clean gas 7b from the outlet 23.
  • the velocity of the gas is suitably reduced in order to provide enough residence time for parti ⁇ cle separation. Accordingly, the cross-sectional area of the fourth flow-path 43 is increased relative to that of the third flow-path 25.
  • the additional casing 41 having an increased cross-sectional area is disposed downstream of the outlet 23 in fluid communication with the outlet 23.
  • the additional casing 41 is disposed coaxially with respect to the outlet 23 and such that the partially clean gas 7b flowing out of the outlet 23 can enter the additional casing 41.
  • the additional casing 41 is elec ⁇ trically grounded and is insulated from the outlet 23 using the insulator 27. As the additional casing 41 is electrically grounded the charged or ionized particles in the partially clean gas 7b will migrate towards the additional casing 41. Once the charged particles are deposited at the additional casing 41 they may be removed either using some impulse/force in case of a dry system or liquid such as water in the case of a wet system. Since the velocity of particles in the out ⁇ let 23 is high, the deposition particles in the outlet 23 would be comparatively low and this can be cleaned by using some rapping mechanism at the end of operation.
  • the insulator 30 can be mounted onto the additional casing 41 and the feed-through arrange ⁇ ment can be disposed into the casing 3 thereon. As only the partially clean gas 7b enters the additional casing 41, the deposition of particulate matter of the insulator 30 is re ⁇ pokerd and thus, preventing short circuit of the insulator 30.
  • FIG 6 illustrates the apparatus 1 according to another em ⁇ bodiment herein.
  • a second por- tion 45 of the additional electrode 33 is extended into the additional casing 41 such that a gap is maintained between the casing 41 and the portion 45 of the electrode 33.
  • the portion 45 of the additional electrode 33 extended into the additional casing 41 will produce a radial electric field be- tween the portion 45 and the additional casing 41. This fur ⁇ ther assists in migration of charged particles towards the casing 41.
  • FIG 7 illustrates the second portion 37 of the additional electrode 33 extending into the additional ionization zone 35 according to an embodiment here.
  • the portion 37 can comprise additional structures including a plurality of discs 37a hav ⁇ ing sharp edges along the length of the portion 37.
  • these additional structures reduce the corona ini- tiation electrical potential required for producing the co ⁇ rona discharge.
  • FIG 8 illustrates the apparatus 1 according to another em ⁇ bodiment herein.
  • the addi- tional ionization zone 35 comprises an additional ionization electrode 47 for producing the corona discharge.
  • the addi ⁇ tional ionization electrode 47 can electrically be connected to the outlet 23, the additional electrode 33 or to the feed- through arrangement 29.
  • the additional ionization electrode 47 can comprise a metallic rod having sharp edges to aid in the production of the corona discharge.
  • the additional elec ⁇ trode 33 can extend into the additional ionization zone 35 and into the additional casing 41. However, as the corona discharged is produced by the additional ionization electrode 47, the portions 37 and 45 of the additional electrode may produce only a radial electric field.

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  • Electrostatic Separation (AREA)

Abstract

L'invention concerne un appareil (1) qui sert à éliminer une matière particulaire dans un gaz et qui comporte : un boîtier (3) comprenant une entrée (5) pour recevoir un gaz contaminé (7a) contenant la matière particulaire et pour induire un tourbillon dans ledit gaz contaminé, une zone d'ionisation (9) disposée à l'intérieur de l'entrée (5) dans une première voie d'écoulement (11) du gaz contaminé (7a) servant à ioniser la matière particulaire du gaz contaminé (7a) en produisant une décharge à effet corona, une zone de séparation (15) disposée dans une deuxième voie d'écoulement (5) du gaz contaminé (7a) en aval de l'entrée (5) qui sert à séparer une partie de la matière particulaire ionisée du gaz contaminé (7a) dans lequel un tourbillon est induit par une action centrifuge et par un champ électrique pour produire un gaz partiellement propre (7b), et une électrode de séparation (22) servant à produire un champ électrique supplémentaire dans au moins une partie de la zone de séparation (15), l'électrode de séparation (22) étant reliée électriquement à un potentiel électrique fourni à la zone d'ionisation (15) pour produire la décharge à effet corona.
PCT/EP2011/055839 2011-04-13 2011-04-13 Appareil d'élimination de matière particulaire dans un gaz WO2012139642A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/EP2011/055839 WO2012139642A1 (fr) 2011-04-13 2011-04-13 Appareil d'élimination de matière particulaire dans un gaz

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/EP2011/055839 WO2012139642A1 (fr) 2011-04-13 2011-04-13 Appareil d'élimination de matière particulaire dans un gaz

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Publication Number Publication Date
WO2012139642A1 true WO2012139642A1 (fr) 2012-10-18

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20150090120A1 (en) * 2013-10-01 2015-04-02 Honeywell International Inc. Aircraft electronic particle separation system
US20150090114A1 (en) * 2013-10-01 2015-04-02 Honeywell International Inc. Aircraft electrostatic particle separation control system
US20150090119A1 (en) * 2013-10-01 2015-04-02 Honeywell International Inc. Self-contained aircraft electronic air treatment system
EP3034174A1 (fr) 2014-12-08 2016-06-22 Svoboda Piotr Slebioda Filtre cyclonique avec une unité électrostatique auxiliaire

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1421969A (en) * 1972-11-29 1976-01-21 Nissan Motor Air purifier
US4352681A (en) * 1980-10-08 1982-10-05 General Electric Company Electrostatically augmented cyclone apparatus
DE3723153A1 (de) * 1987-07-14 1989-01-26 Navsat Gmbh Vorrichtung fuer die abscheidung von russ aus dem abgas eines verbrennungsmotors
US5968231A (en) * 1993-12-14 1999-10-19 Grignotage, (Sarl) Cyclone exchanger with tranquilizing tank and method for purifying and decontaminating air
EP0995494A2 (fr) * 1998-09-25 2000-04-26 Golden Showcase Intellectual Properties Sdn Bhd Un dispositif de filtration électrostatique
EP1097749A1 (fr) * 1999-11-05 2001-05-09 Bayerische Motoren Werke Aktiengesellschaft Filtre a air de type cyclone avec séparateur électrostatique
US20080060522A1 (en) * 2006-09-13 2008-03-13 United Technologies Corporation Electrostatic particulate separation system and device
US20090101009A1 (en) * 2007-10-23 2009-04-23 United Technologies Corporation Core separator integration for mercury removal from flue gases of coal-fired boilers
US20090277325A1 (en) * 2008-05-07 2009-11-12 Gottung Eric J Electrostatic particulate separation for emission treatment systems

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1421969A (en) * 1972-11-29 1976-01-21 Nissan Motor Air purifier
US4352681A (en) * 1980-10-08 1982-10-05 General Electric Company Electrostatically augmented cyclone apparatus
DE3723153A1 (de) * 1987-07-14 1989-01-26 Navsat Gmbh Vorrichtung fuer die abscheidung von russ aus dem abgas eines verbrennungsmotors
US5968231A (en) * 1993-12-14 1999-10-19 Grignotage, (Sarl) Cyclone exchanger with tranquilizing tank and method for purifying and decontaminating air
EP0995494A2 (fr) * 1998-09-25 2000-04-26 Golden Showcase Intellectual Properties Sdn Bhd Un dispositif de filtration électrostatique
EP1097749A1 (fr) * 1999-11-05 2001-05-09 Bayerische Motoren Werke Aktiengesellschaft Filtre a air de type cyclone avec séparateur électrostatique
US20080060522A1 (en) * 2006-09-13 2008-03-13 United Technologies Corporation Electrostatic particulate separation system and device
US20090101009A1 (en) * 2007-10-23 2009-04-23 United Technologies Corporation Core separator integration for mercury removal from flue gases of coal-fired boilers
US20090277325A1 (en) * 2008-05-07 2009-11-12 Gottung Eric J Electrostatic particulate separation for emission treatment systems

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20150090120A1 (en) * 2013-10-01 2015-04-02 Honeywell International Inc. Aircraft electronic particle separation system
US20150090114A1 (en) * 2013-10-01 2015-04-02 Honeywell International Inc. Aircraft electrostatic particle separation control system
US20150090119A1 (en) * 2013-10-01 2015-04-02 Honeywell International Inc. Self-contained aircraft electronic air treatment system
US9199248B2 (en) * 2013-10-01 2015-12-01 Honeywell International Inc. Aircraft electronic particle separation system
US9216827B2 (en) * 2013-10-01 2015-12-22 Honeywell International Inc. Self-contained aircraft electronic air treatment system
US9427746B2 (en) * 2013-10-01 2016-08-30 Honeywell International Inc. Aircraft electrostatic particle separation control system
EP3034174A1 (fr) 2014-12-08 2016-06-22 Svoboda Piotr Slebioda Filtre cyclonique avec une unité électrostatique auxiliaire

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