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US2422564A - Electrical dust-precipitator - Google Patents

Electrical dust-precipitator Download PDF

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US2422564A
US2422564A US603930A US60393045A US2422564A US 2422564 A US2422564 A US 2422564A US 603930 A US603930 A US 603930A US 60393045 A US60393045 A US 60393045A US 2422564 A US2422564 A US 2422564A
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dust
tubes
gas
tube
electrodes
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Edward H R Pegg
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Westinghouse Electric Corp
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    • 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
    • B03C3/49Collecting-electrodes tubular
    • 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
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/86Electrode-carrying means

Definitions

  • My invention is generally directed to improvements in electrical dust-precipitators for cleaning a dust-carrying gas, and is more particularly directed to improvements in that type of electrical dust-precipitators which clean a flowing gas principally by charging gas-borne dust-particles in one region, and subsequently precipitate the charged dust-particles from the gas in another separate region, spaced downstream from the dust-charging region.
  • a further object of my invention is to provide an electrical dust-precipitator which is sturdily built as a complete structural unit so that it can be bodily inserted into, or removed from, gas conduits of corresponding size.
  • Figure 1 is a vertical central sectional view, with some parts broken away for clarity, of an electrical dust-precipitator in accordance with my invention, the dust-precipitator being shown in a gas-duct;
  • Fig. 2 is a vertical sectional view, transverse to Fig. 1, substantially on the line IIII thereof, without the gas-duct. Without the sectioned parts, this figure also illustrates end views of the gas-cleaning unit;
  • Fig. 3 is a vertical sectional view, substantially on the line III-III of Fig. 1, with some parts omitted;
  • Fig. 4 is an elevational view of a grating used to support the insulated electrodes of theelectrical dust-precipitator
  • Figs. 5 and 6 are details of 60-angle members which are secured to gratings such as shown in Fig. 4;
  • Figs. 7 and 8 are longitudinal and transverse sectional views, respectively, of an insulated nondischarging electrode and its support;
  • Fig. 9 is an exploded View of an ionizing wire and supporting means therefor.
  • a gas-cleaning means in accordance with my invention comprises an upstream dust-charging means, indicated in its entirety by the reference numeral 2, and a downstream dust-precipitating means, indicated in its entirety by the reference numeral t.
  • a gas-cleaning means is built as a rigid unit for installation into a suitable gas-duct such as the gas-duct 6 Which, in this case, is round.
  • the gas-cleaning unit comprises a plurality of coaxial rings or hoops 8, ill, l2 and M which are alike. These rings are short hollow cylinders and are spaced longitudinally in the direction of gas-flow Which is indicated by the arrows A.
  • the ring 8 is a part of the dust-charging means Land is the farthest upstream'ring.
  • the rings l0, l2 and. M are part of the dust-precipitating means 4, and are successively further downstream than the ring 8. These rings carry the structural parts of the gascleaning means, the intermediate ring I: being a reenforcing ring of which as many can be provided as the desired strength, length, and rigidity of the gas-cleaning unit demands.
  • the dust-charging means also comprises a plurality of low potential or uninsulated electrodes in the form of tubes-l6, and a plurality of insulated ionizing Wires IS; an ionizing wire is extending coaxially through each tube 96.
  • the tubeelectrodes 16 have their axes extending longitudinally, following the direction of gas-flow. They have a regular hexagon contour in crosssection and are assembled so as to provide a tube assembly which lies within the ring 8.
  • the dust-precipitating means 4 also includes a plurality of low potential or uninsulated electrodes in the form of tubes 28, and a plurality of insulated non-discharging electrodes 30 in the form of hollow rods; a rod 30 extending coaxially through each tube.
  • the tubes 28 are assembled to provide a tube-assembly which lies within the rings l0, l2 and I 4.
  • the tubes 16 of the dust-charging means and the tubes 28 of the dust-precipitating means are of the same construction, except with respect to length; the tubes It being relatively much shorter than the tubes 28, or conversely, the tubes 28 being comparatively relatively long.
  • each tube-assembly has a lengthwise or longitudinal slit in one of its sides, this side being placed against a solid side of the abutting tube.
  • Each tubeassembly has a series of nested or concentric hexagon layers about a center tube B, except for the outermost groups of tubes C, as indicated in Figs. 2 and 3. In order to get as many hexagonal tubes as possible within the circular periphery of the rings, corner tubes of the outermost layer which comprises groups C, are omitted.
  • Sealing means are used for barring gas-"flow between the inside of a ring and the outside of the associated tube-assembly,'the sealing means comprising a plurality of separate segments 3
  • the segment 3! has a serrated edge embracing side of single corners of hexagons; while the segment 3
  • tubes have been omitted to show the segments more clearly.
  • the ring 8, the tube-assembly of the tubes Iii, and the associated sealing segments 3! and 3! arewelded, or otherwise secured. into a first unit-part; and the rings I0, l2 and M, the associated segments 3
  • the unit-parts are rigidly secured together into a more comprehensive unit by means of a plurality of strong intermediate plates 32 extending between and secured to the insides of the rings-8 and [0. In the embodiment shown, four plates 32 have been provided, each being in vertical and horizontal alignment with another, as is apparent from Fig. 2, but additional plates may be provided if desired.
  • the four plates specifically mentioned also support insulating means for the insulated electrodes of the dust-charging means and the dust-precipitating means.
  • a feature of the construction shown resides in the use of common insulators for supporting the facing ends of the electrodes of both the dust-charging means and the dustprecipitating means.
  • an upper angle bar 34 is rigidly secured to the upper plates 32 and a lower angle bar 38 is rigidly secured to the lower plates 32.
  • the angle bars 36 and 36 are parallel, and are disposed so as to securely receive spaced upper and lower insulating assemblies 38 and M], respectively.
  • eachinsulating assembly comprises relatively insulated nested oppositelydirected metal cans or cups 42 and M,'the cup 42 being secured to the uni-nsulated end of an inner insulator 46 and the cup 44 being secured to the insulated end of the insulator.
  • the cups may be provided with one or more drainage holes.
  • An upper angular cross-bar 0 is secured across the upper insulating assemblies 38 and a similar lower bar 52 across the insulated ends of the lower insulating assemblies 40.
  • insulating structures are provided at the upstream and downstream ends of the gas-cleaning unit.
  • plates '54 are secured to the ring 8, with portions protruding upstream.
  • An upper insulated angular cross-bar 54 extends between the insulatedends ,of the upper insulating assemblies fill and a lo'wer insulated cross-bar 66 extends between the insulated ends of the lower insulating assemblies ,62.
  • plates 58 support upper and lower angle, barsflfl and 1,2 which,carry upper and lower --insulating assemblies vHI and :16, respectively, insulatedly carrying upper and lower angular cross-bars l3 and 80, respectively.
  • gratings 82 and 64 are provided at the respective ends of the tube-electrodes l6 and gratings86 and 88 are provided at the respective ends of the tube-electrodes 28.
  • Each grating is in the form of a spider-web and of a size to lie within the supporting structure with adequate air insulation.
  • Secured to each grating is a plurality of 60-angle bars 99 which extend away from the electrodes supported by the associated grating and are secured to the upper and lower insulated cross-bars 50 and 52, or 64 and 66, or l3 and 83, as the case may be.
  • Fig. 5 shows a 60-angle bar for use with the extreme. upstream and downstream gratings 82 and 88.
  • Fig. 6 shows two such angle bars extending toward each other from the gratings 86 and 86, one of the bars being provided with a hole 9 2 for bolting to an insulated cross-bar 5B or 52.
  • the gratings 82, 84 at each end ofthe dustcharging means 2 are provided .with a plurality of blocks 96 aligned with the axes of the tubeelectrodes 16.
  • Each pair of directly facing blocks 55% carries means for resiliently removably .carrying an ionizing wire it in tension.
  • each ionizing wire is preformed with end loops, I00, one of which fits a hook 98and the other of which fits an end of a springlllZ whose other end fits the other hook 9B.
  • the hooks 58 are fastened to the blocks 96.
  • the gratings 86, 88 at each end of the dustprecipitating means 4 are provided with cooperating stub-shafts Hi4 and I06 aligned with the axes of the tube-electrodes 28, eachsuch pair of directly facing stub-shafts removably holding a hollow non-discharging rod-electrode 3 As shown in Figs. 7 and 8, the stub-shaft 104 on the grating 86 is shorter than the stub-shaft I06 on the grating 88.
  • a single highpotential conductor connected to anyof the insulated crossbars, will energize or chargethe insulated ionizing wires l8 and the insulating nondischarging rod-electrodes 30.
  • the ionizing wires discharge to the tube-electrode l5,,,thereby providing a shallow ionized electrostatic field within each tube through which the gas passesso that the gas-borne dust-particles .are electrically charged.
  • the charged dust-particles are carried into the dust-precipitating means .where they are precipitated to the tube electrodes28 bythe substantially non-ionized electrostatic field between each non-discharging electrode 3! and its associated tube-electrode 23.
  • the ionizing wires When arranged longitudinally as shown-the ionizing wires can be comparatively short to minimize vibration and breakage. Except for the insulators, all of the tubes, plates, anglebaracross bars, and other parts of the gas-cleaning unit can be made of stainless steel, copper alloys, or other materials resistant to corrosion by salt-water and sea-air.
  • the arrangement of hexagonal tubes provides a honeycomb structure of great strength With a maximum number of tube for a circular gas-duct.
  • the insulated electrodes are supported by a simple rigid structure lying within the confines of the rings 3, i0, i2, and i l about which the unit is built.
  • An indication of the size of an apparatus embodying my invention, to which I am by no means limited, may be obtained from the following dimensions of a specific construction for cleaning gases flowing at about 1000 feet per minute.
  • the unit had an overall length of 77%; inches and a diameter of close to 36 inches.
  • the tubeelectrodes for the dust-charging means were 2 /2 inches long and the tube-electrodes for the dustprecipitating means 47 inches long, all tubes being 2 inches between parallel opposite sides.
  • the ionizing wires had a length of about 3% inches between centers of their end loops and a .015 inch diameter.
  • the nondischarging rodelectrodes had an overall length of 48%, inches and an outside diameter of inch.
  • Electrostatic equipment of a type described adapted to treat a gas flowing longitudinally comprising a hollow cylindrical gas-duct, electrode-means comprising a first group and a second group of substantially coextensive juxtaposed hexagonal tubes, the tubes of each group being secured together inside said cylindrical gas-duct, sealing means for closing the space between each of said groups of tubes and said cylindrical gas-duct, said sealing means being secured to each of said groups of tube and to said cylindrical gas-duct, a plurality of bar members carried by said cylindrical gas-duct, and extending transversely across it at the ends of said tubes, a plurality of'insulators carried by said bar members, the insulators between said groups of tubes having longitudinal bars secured thereto, transverse grating means carried by the insulators at the far ends of said tubes, transverse grating means carried at each end of said longitudinal bars, and electrode carried by said grating means axially passing through said tubes, in insulated spaced relation thereto.
  • Electrostatic equipment of a type described for treating a gas flowing longitudinally comprising a plurality of ring members spaced longitudinally, a first group of substantially coextensive juxtaposed relatively short hexagonal tubes secured together, said group being secured to and inside of an upstream one of said ring members, a second group of substantially coextensive juxtaposed relatively long hexagonal tubes secured together, said second group being secured to and inside of a plurality of spaced downstream ring members, longitudinal bar members rigidly connecting said upstream ring member and the downstream ring member next adjacent to it, in
  • non-discharging electrodes carried by the grating members at opposite ends of said second group of tubes, said electrodes passing centrally through the tubes of said second group.
  • Gas cleaning means for a gas flowing longitudinally comprising a downstream dust-charging means and an upstream dust-precipitating means; said dust-charging means comprising a plurality of substantially coextensive longitudinal relatively short hexagonal tube-electrodes, an ionizing wire insulatedly extending through each of said tube-electrodes, and a transverse insulated grating at each end of said dust-charging means, having means for anchoring each end of said ionizing wires; said dust-precipitating means comprising a plurality of substantially coextensive longitudinal relatively long hexagonal-tube precipitating-electrodes, a non-discharging electrode insulatedly extending through each of said precipitating-electrodes, and a transverse insulated grating at each end of said dust-precipitating means, having means for anchoring each end of said precipitating-electrodes; said gas-cleaning means comprising insulators at each of its ends for carrying the gratings thereat
  • Dust-precipitating means comprising a tubular outer electrode, a non-discharging hollow rod-electrode inside said outer electrode, and means for replaceably supporting said rod-electrode, comprising a stub-rod fitting one end of said rod-electrode, another relatively longer stubrod fitting the other end of said rod-electrode, said rod-electrode having a bulge spaced from said longer stub-rod, a perforated disc bearing on said bulge, and a compression spring bearing on said disc and said longer stub-rod.

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Description

June 17, 1947. R, E G 2,422,564
ELECTRICAL DUST-PRECIPITATOR Filed July 9, 1945 2 Sheets-Sheet 2 a l l all INVENTOR 71M wdzjlg/m 98 Y v axzw wzz [-7 '9 ATTORNEY Patented June 17, 1947 ELECTRICAL DUST-PRECIPITATOR Edward H. R. Pegg, Cranford, N. J., assignor to Westinghouse Electric Corporation, East Pittsburgh, Pa., a corporation of Pennsylvania Application July 9, 1945, Serial No. 603,930
4 Claims. ((31. 183-7) My invention is generally directed to improvements in electrical dust-precipitators for cleaning a dust-carrying gas, and is more particularly directed to improvements in that type of electrical dust-precipitators which clean a flowing gas principally by charging gas-borne dust-particles in one region, and subsequently precipitate the charged dust-particles from the gas in another separate region, spaced downstream from the dust-charging region.
It is among the objects of my invention to provide an electrical dust-precipitator of a type described which is simple and sturdy in construction, using many duplicate parts, which is rugged for withstanding shock and vibration, and which will remove extremely fine dust-particles from a gas with a high eificiency in the order of that attained only with electrical precipitators.
A further object of my invention is to provide an electrical dust-precipitator which is sturdily built as a complete structural unit so that it can be bodily inserted into, or removed from, gas conduits of corresponding size.
It is also among the objects of my invention to provide an electrical dust-precipitator of the type described for removing carbonaceous dustparticles from a gas flowing at a high velocity.
Other features and objects of my invention, in addition to the foregoing, will be discernible from the following description of a preferred embodiment, which is to be taken in conjunction with the accompanying drawings on various scales.
In the drawings:
Figure 1 is a vertical central sectional view, with some parts broken away for clarity, of an electrical dust-precipitator in accordance with my invention, the dust-precipitator being shown in a gas-duct;
Fig. 2 is a vertical sectional view, transverse to Fig. 1, substantially on the line IIII thereof, without the gas-duct. Without the sectioned parts, this figure also illustrates end views of the gas-cleaning unit;
Fig. 3 is a vertical sectional view, substantially on the line III-III of Fig. 1, with some parts omitted;
Fig. 4 is an elevational view of a grating used to support the insulated electrodes of theelectrical dust-precipitator;
Figs. 5 and 6 are details of 60-angle members which are secured to gratings such as shown in Fig. 4;
Figs. 7 and 8 are longitudinal and transverse sectional views, respectively, of an insulated nondischarging electrode and its support;
Fig. 9 is an exploded View of an ionizing wire and supporting means therefor.
A gas-cleaning means in accordance with my invention comprises an upstream dust-charging means, indicated in its entirety by the reference numeral 2, and a downstream dust-precipitating means, indicated in its entirety by the reference numeral t. Such a gas-cleaning means is built as a rigid unit for installation into a suitable gas-duct such as the gas-duct 6 Which, in this case, is round. structurally, the gas-cleaning unit comprises a plurality of coaxial rings or hoops 8, ill, l2 and M which are alike. These rings are short hollow cylinders and are spaced longitudinally in the direction of gas-flow Which is indicated by the arrows A. The ring 8 is a part of the dust-charging means Land is the farthest upstream'ring. The rings l0, l2 and. M are part of the dust-precipitating means 4, and are successively further downstream than the ring 8. These rings carry the structural parts of the gascleaning means, the intermediate ring I: being a reenforcing ring of which as many can be provided as the desired strength, length, and rigidity of the gas-cleaning unit demands.
The dust-charging means also comprises a plurality of low potential or uninsulated electrodes in the form of tubes-l6, and a plurality of insulated ionizing Wires IS; an ionizing wire is extending coaxially through each tube 96. The tubeelectrodes 16 have their axes extending longitudinally, following the direction of gas-flow. They have a regular hexagon contour in crosssection and are assembled so as to provide a tube assembly which lies within the ring 8.
The dust-precipitating means 4 also includes a plurality of low potential or uninsulated electrodes in the form of tubes 28, and a plurality of insulated non-discharging electrodes 30 in the form of hollow rods; a rod 30 extending coaxially through each tube. The tubes 28 are assembled to provide a tube-assembly which lies within the rings l0, l2 and I 4.
In this particular embodiment, the tubes 16 of the dust-charging means and the tubes 28 of the dust-precipitating means are of the same construction, except with respect to length; the tubes It being relatively much shorter than the tubes 28, or conversely, the tubes 28 being comparatively relatively long.
The tube-assemblies of the dust-charging means 2 and of the dust-precipitating means 4 are similarly constructed. The tubes of each tube-assembly are coextensive and are welded together in juxtaposed position with sides fitting after the fashion indicated in Figs. 2 and 3. For convenience and economy in manufacturing, each tube has a lengthwise or longitudinal slit in one of its sides, this side being placed against a solid side of the abutting tube. Each tubeassembly has a series of nested or concentric hexagon layers about a center tube B, except for the outermost groups of tubes C, as indicated in Figs. 2 and 3. In order to get as many hexagonal tubes as possible within the circular periphery of the rings, corner tubes of the outermost layer which comprises groups C, are omitted.
Sealing means are used for barring gas-"flow between the inside of a ring and the outside of the associated tube-assembly,'the sealing means comprising a plurality of separate segments 3| and BI, of two forms only, which are alternately arranged around the inside of each ring, as shown in Figs, 2 and 3. The segment 3! has a serrated edge embracing side of single corners of hexagons; while the segment 3| has a serrated edge embracing three sides of hexagons. In Fig. 3, tubes have been omitted to show the segments more clearly.
The ring 8, the tube-assembly of the tubes Iii, and the associated sealing segments 3! and 3! arewelded, or otherwise secured. into a first unit-part; and the rings I0, l2 and M, the associated segments 3| and 3!, and the tube-assembly of the tubes 28 are similarly secured into a second unit-part. The unit-parts are rigidly secured together into a more comprehensive unit by means of a plurality of strong intermediate plates 32 extending between and secured to the insides of the rings-8 and [0. In the embodiment shown, four plates 32 have been provided, each being in vertical and horizontal alignment with another, as is apparent from Fig. 2, but additional plates may be provided if desired.
The four plates specifically mentioned also support insulating means for the insulated electrodes of the dust-charging means and the dust-precipitating means. A feature of the construction shown resides in the use of common insulators for supporting the facing ends of the electrodes of both the dust-charging means and the dustprecipitating means. To this end, an upper angle bar 34 is rigidly secured to the upper plates 32 and a lower angle bar 38 is rigidly secured to the lower plates 32. The angle bars 36 and 36 are parallel, and are disposed so as to securely receive spaced upper and lower insulating assemblies 38 and M], respectively.
As indicatdin Fig. 1, eachinsulating assembly comprises relatively insulated nested oppositelydirected metal cans or cups 42 and M,'the cup 42 being secured to the uni-nsulated end of an inner insulator 46 and the cup 44 being secured to the insulated end of the insulator. When the cups are oppositely charged, an electrostatic field is provided between them for precipitating any dust tending to flowtoward the insulator 45. The cups may be provided with one or more drainage holes. An upper angular cross-bar 0 is secured across the upper insulating assemblies 38 and a similar lower bar 52 across the insulated ends of the lower insulating assemblies 40.
Generally similar insulating structures are provided at the upstream and downstream ends of the gas-cleaning unit. At the upstream end, plates '54 are secured to the ring 8, with portions protruding upstream. An upper angle bar 56 and a lower bar 58, carried by the plates 54, support spaced ripper. and lower insulating assemblies 60 and 62, respectively. An upper insulated angular cross-bar 54 extends between the insulatedends ,of the upper insulating assemblies fill and a lo'wer insulated cross-bar 66 extends between the insulated ends of the lower insulating assemblies ,62. At the downstream endof the unit,.plates 58 support upper and lower angle, barsflfl and 1,2 which,carry upper and lower --insulating assemblies vHI and :16, respectively, insulatedly carrying upper and lower angular cross-bars l3 and 80, respectively.
For supporting the ends of the insulated electrodes of the dust-charging means and the dustprecipitating means, gratings 82 and 64 are provided at the respective ends of the tube-electrodes l6 and gratings86 and 88 are provided at the respective ends of the tube-electrodes 28. Each grating is in the form of a spider-web and of a size to lie within the supporting structure with adequate air insulation. Secured to each grating is a plurality of 60-angle bars 99 which extend away from the electrodes supported by the associated grating and are secured to the upper and lower insulated cross-bars 50 and 52, or 64 and 66, or l3 and 83, as the case may be.
Fig. 5 shows a 60-angle bar for use with the extreme. upstream and downstream gratings 82 and 88.
Fig. 6 shows two such angle bars extending toward each other from the gratings 86 and 86, one of the bars being provided with a hole 9 2 for bolting to an insulated cross-bar 5B or 52. A plate as is fastened to both legs of the bars so that these bars'fifl are unitary and carry the gratings to which they are secured and associated parts. Accordingly, each grating is securely carried by an insulating assembly,
The gratings 82, 84 at each end ofthe dustcharging means 2 are provided .with a plurality of blocks 96 aligned with the axes of the tubeelectrodes 16. Each pair of directly facing blocks 55% carries means for resiliently removably .carrying an ionizing wire it in tension. As shown in Fig. 9, each ionizing wireis preformed with end loops, I00, one of which fits a hook 98and the other of which fits an end of a springlllZ whose other end fits the other hook 9B. The hooks 58 are fastened to the blocks 96. I
The gratings 86, 88 at each end of the dustprecipitating means 4 are provided with cooperating stub-shafts Hi4 and I06 aligned with the axes of the tube-electrodes 28, eachsuch pair of directly facing stub-shafts removably holding a hollow non-discharging rod-electrode 3 As shown in Figs. 7 and 8, the stub-shaft 104 on the grating 86 is shorter than the stub-shaft I06 on the grating 88. Both fit into the rod-electrode 30 with enough end clearance to permit the rod-electrode to be pushed against a compression spring I03 so that the end ofthe rod-electrode at the stub-shaft I04 can he slipped by it. The spring I08 is braced against a perforated disc I I0 bearing on an inside bulge I l2 in the rod-electrode 30.
With the structure described, a single highpotential conductor. connected to anyof the insulated crossbars, will energize or chargethe insulated ionizing wires l8 and the insulating nondischarging rod-electrodes 30. The ionizing wires discharge to the tube-electrode l5,,,thereby providing a shallow ionized electrostatic field within each tube through which the gas passesso that the gas-borne dust-particles .are electrically charged. The charged dust-particles are carried into the dust-precipitating means .where they are precipitated to the tube electrodes28 bythe substantially non-ionized electrostatic field between each non-discharging electrode 3!! and its associated tube-electrode 23.
When arranged longitudinally as shown-the ionizing wires can be comparatively short to minimize vibration and breakage. Except for the insulators, all of the tubes, plates, anglebaracross bars, and other parts of the gas-cleaning unit can be made of stainless steel, copper alloys, or other materials resistant to corrosion by salt-water and sea-air. The arrangement of hexagonal tubes provides a honeycomb structure of great strength With a maximum number of tube for a circular gas-duct. The insulated electrodes are supported by a simple rigid structure lying within the confines of the rings 3, i0, i2, and i l about which the unit is built.
An indication of the size of an apparatus embodying my invention, to which I am by no means limited, may be obtained from the following dimensions of a specific construction for cleaning gases flowing at about 1000 feet per minute. The unit had an overall length of 77%; inches and a diameter of close to 36 inches. The tubeelectrodes for the dust-charging means were 2 /2 inches long and the tube-electrodes for the dustprecipitating means 47 inches long, all tubes being 2 inches between parallel opposite sides. The ionizing wires had a length of about 3% inches between centers of their end loops and a .015 inch diameter. The nondischarging rodelectrodes had an overall length of 48%, inches and an outside diameter of inch.
While I have described my invention in a preferred form, it is obvious that features of it are subject to modification. For example, instead of hexagonal tubes, round tubes might be used for the uninsulated electrodes; nor need the tubes of the dust-charging means be of the same crosssectional area as those of the dust-precipitating means.
I claim as my invention:
1. Electrostatic equipment of a type described adapted to treat a gas flowing longitudinally, comprising a hollow cylindrical gas-duct, electrode-means comprising a first group and a second group of substantially coextensive juxtaposed hexagonal tubes, the tubes of each group being secured together inside said cylindrical gas-duct, sealing means for closing the space between each of said groups of tubes and said cylindrical gas-duct, said sealing means being secured to each of said groups of tube and to said cylindrical gas-duct, a plurality of bar members carried by said cylindrical gas-duct, and extending transversely across it at the ends of said tubes, a plurality of'insulators carried by said bar members, the insulators between said groups of tubes having longitudinal bars secured thereto, transverse grating means carried by the insulators at the far ends of said tubes, transverse grating means carried at each end of said longitudinal bars, and electrode carried by said grating means axially passing through said tubes, in insulated spaced relation thereto.
2. Electrostatic equipment of a type described for treating a gas flowing longitudinally, comprising a plurality of ring members spaced longitudinally, a first group of substantially coextensive juxtaposed relatively short hexagonal tubes secured together, said group being secured to and inside of an upstream one of said ring members, a second group of substantially coextensive juxtaposed relatively long hexagonal tubes secured together, said second group being secured to and inside of a plurality of spaced downstream ring members, longitudinal bar members rigidly connecting said upstream ring member and the downstream ring member next adjacent to it, in
.ried by said insulator means near each end of each said group of tubes, ionizing wires carried by the gratin members at opposite ends of said first group of tubes, said ionizing wires passing centrally through the tubes of said first group,
and non-discharging electrodes carried by the grating members at opposite ends of said second group of tubes, said electrodes passing centrally through the tubes of said second group.
3. Gas cleaning means for a gas flowing longitudinally, comprising a downstream dust-charging means and an upstream dust-precipitating means; said dust-charging means comprising a plurality of substantially coextensive longitudinal relatively short hexagonal tube-electrodes, an ionizing wire insulatedly extending through each of said tube-electrodes, and a transverse insulated grating at each end of said dust-charging means, having means for anchoring each end of said ionizing wires; said dust-precipitating means comprising a plurality of substantially coextensive longitudinal relatively long hexagonal-tube precipitating-electrodes, a non-discharging electrode insulatedly extending through each of said precipitating-electrodes, and a transverse insulated grating at each end of said dust-precipitating means, having means for anchoring each end of said precipitating-electrodes; said gas-cleaning means comprising insulators at each of its ends for carrying the gratings thereat, and a plurality of common insulators for carrying the gratings which are disposed between said tubeelectrodes and said precipitating-electrodes.
4. Dust-precipitating means comprising a tubular outer electrode, a non-discharging hollow rod-electrode inside said outer electrode, and means for replaceably supporting said rod-electrode, comprising a stub-rod fitting one end of said rod-electrode, another relatively longer stubrod fitting the other end of said rod-electrode, said rod-electrode having a bulge spaced from said longer stub-rod, a perforated disc bearing on said bulge, and a compression spring bearing on said disc and said longer stub-rod.
EDWARD H. R. PEGG.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 2,221,601 Nielsen Nov. 12, 1940 1,634,372 Lewers July 5, 1927 2,024,226 Irwin et al. Dec. 17, 1935 1,357,466 Moller Nov. 2, 1920 1,478,798 Schmidt Dec. 25, 1923 1,982,470 Franks Nov. 27, 1934 2,008,246 Deutsch July 16, 1935 FOREIGN PATENTS Number Country Date 553,753 Great Britain June 3, 1943
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Cited By (16)

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US2537558A (en) * 1947-05-10 1951-01-09 Air Preheater Removal of solids from gases
US2571079A (en) * 1948-12-01 1951-10-09 Westinghouse Electric Corp Electrostatic precipitator
US2582133A (en) * 1947-05-10 1952-01-08 Air Preheater Gas cleaning
US2708007A (en) * 1952-03-27 1955-05-10 Apra Precipitator Corp Electrode positioning grids
US2711225A (en) * 1953-10-08 1955-06-21 Research Corp High efficiency high velocity electrostatic air cleaner
US2726730A (en) * 1949-06-16 1955-12-13 Apra Precipitator Corp Gas cleaning device
DE1004143B (en) * 1952-04-18 1957-03-14 Metallgesellschaft Ag Round electrostatic precipitator
US2979158A (en) * 1958-10-17 1961-04-11 Gordon M Genge & Company Inc Electrostatic particle separating apparatus
US3633337A (en) * 1969-04-25 1972-01-11 Cottrell Res Inc Gas-handling method and apparatus
US4230466A (en) * 1979-05-10 1980-10-28 Santek, Inc. Discharge electrode structure for electrostatic precipitator
EP0180094A1 (en) * 1984-10-30 1986-05-07 Siemens Aktiengesellschaft Process for separating isotopes, especially for separating istopes of uranium, device for performing it and use thereof
EP0757923A1 (en) * 1995-08-07 1997-02-12 Environmental Elements Corporation Laminar flow electrostatic precipitation system
US20060226373A1 (en) * 2005-03-02 2006-10-12 Eisenmann Corporation Wet electrostatic precipitator for treating oxidized biomass effluent
US20060261265A1 (en) * 2005-03-02 2006-11-23 Eisenmann Corporation Dual flow wet electrostatic precipitator
US20070009411A1 (en) * 2005-07-08 2007-01-11 Eisenmann Corporation Method and apparatus for particulate removal and undesirable vapor scrubbing from a moving gas stream
US20070128090A1 (en) * 2005-12-06 2007-06-07 Eisenmann Corporation Wet electrostatic liquid film oxidizing reactor apparatus and method for removal of NOx, SOx, mercury, acid droplets, heavy metals and ash particles from a moving gas

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Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2537558A (en) * 1947-05-10 1951-01-09 Air Preheater Removal of solids from gases
US2582133A (en) * 1947-05-10 1952-01-08 Air Preheater Gas cleaning
US2571079A (en) * 1948-12-01 1951-10-09 Westinghouse Electric Corp Electrostatic precipitator
US2726730A (en) * 1949-06-16 1955-12-13 Apra Precipitator Corp Gas cleaning device
US2708007A (en) * 1952-03-27 1955-05-10 Apra Precipitator Corp Electrode positioning grids
DE1004143B (en) * 1952-04-18 1957-03-14 Metallgesellschaft Ag Round electrostatic precipitator
US2711225A (en) * 1953-10-08 1955-06-21 Research Corp High efficiency high velocity electrostatic air cleaner
US2979158A (en) * 1958-10-17 1961-04-11 Gordon M Genge & Company Inc Electrostatic particle separating apparatus
US3633337A (en) * 1969-04-25 1972-01-11 Cottrell Res Inc Gas-handling method and apparatus
US4230466A (en) * 1979-05-10 1980-10-28 Santek, Inc. Discharge electrode structure for electrostatic precipitator
EP0180094A1 (en) * 1984-10-30 1986-05-07 Siemens Aktiengesellschaft Process for separating isotopes, especially for separating istopes of uranium, device for performing it and use thereof
EP0757923A1 (en) * 1995-08-07 1997-02-12 Environmental Elements Corporation Laminar flow electrostatic precipitation system
US5707428A (en) * 1995-08-07 1998-01-13 Environmental Elements Corp. Laminar flow electrostatic precipitation system
AU715203B2 (en) * 1995-08-07 2000-01-20 Environmental Elements Corp. Laminar flow electrostatic precipitation system
CN1103250C (en) * 1995-08-07 2003-03-19 环境要素有限公司 Laminar flow electrostatic precipitation system
US20060226373A1 (en) * 2005-03-02 2006-10-12 Eisenmann Corporation Wet electrostatic precipitator for treating oxidized biomass effluent
US20060261265A1 (en) * 2005-03-02 2006-11-23 Eisenmann Corporation Dual flow wet electrostatic precipitator
US7297182B2 (en) 2005-03-02 2007-11-20 Eisenmann Corporation Wet electrostatic precipitator for treating oxidized biomass effluent
US7318857B2 (en) 2005-03-02 2008-01-15 Eisenmann Corporation Dual flow wet electrostatic precipitator
US20070009411A1 (en) * 2005-07-08 2007-01-11 Eisenmann Corporation Method and apparatus for particulate removal and undesirable vapor scrubbing from a moving gas stream
US20070128090A1 (en) * 2005-12-06 2007-06-07 Eisenmann Corporation Wet electrostatic liquid film oxidizing reactor apparatus and method for removal of NOx, SOx, mercury, acid droplets, heavy metals and ash particles from a moving gas

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