US2297601A - Electric gas cleaner - Google Patents

Electric gas cleaner Download PDF

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US2297601A
US2297601A US355277A US35527740A US2297601A US 2297601 A US2297601 A US 2297601A US 355277 A US355277 A US 355277A US 35527740 A US35527740 A US 35527740A US 2297601 A US2297601 A US 2297601A
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electrodes
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gas
dielectric
filter
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Charles W Williams
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American Air Filter Co Inc
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American Air Filter Co Inc
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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
    • B03C3/02Plant or installations having external electricity supply
    • B03C3/04Plant or installations having external electricity supply dry type
    • B03C3/14Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
    • B03C3/155Filtration

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  • This invention relates to the art of cleaning gases electrically.
  • gas borne "dust particles are electrically charged by impressing high ionizing voltages between laterally spaced electrodes to create an electrical field and passing the gas longitudinally through the field -so created. Particles charged or ionized in this manner ⁇ gravitate slowly across the gas flow toward oppositely charged surfaces upon which they are intended ultimately to precipitate and collect.
  • An important object of this invention is to avoid or minimize the foregoing limitations and e objections, and, more particularly, to provide an improved form oi' device for effectively cleaning gas electrically, wherein the use of lower voltages and higher velocities are promoted and the removal of collected dust is facilitated.
  • 'A further object is to provide in a device o f this character an inexpensive dust collecting medium which can be easily and quickly removed and replaced.
  • a still furtherobiect is to provide a compact device having desirable operating characteristics, such as lowsoperating voltage, high gas handling capacity, low gas iiow resistance and high gas cleaning eiiiciency, and minimum maintenance requirements, such as low power consumption and low reconditioning expense.
  • Another important object is to maintain an effective electrostatic charge or4 potential upon a dielectric lter ⁇ mediumf through which gas is passed.
  • the gas is passed through the openings of an interstitial dielectric separator, while a potential difference is maintained betweenthe upstream and downstream faces of the separator.
  • Figure 1 is a vertical section taken through one embodiment of the invention in its operative gas cleaning position
  • FIG 2 is an enlarged fragmentary view taken from Figure l, in which the details are exaggerated for the sake of clearness;
  • Figure 3 is a similarly enlarged fragmentary viewv taken at right angles to Figure 2;
  • Figure 4 is a partly broken view of the upstream end of the device
  • Figure 5 is a partly broken view of the downstream end of the device
  • Figure 6 is a schematic view of an alternative arrangement for carrying out the invention.
  • Figure 7 is a practical embodiment of the arrangement shown in Figure 6;
  • Figure 8 is a detail of the air filter structure shown in Figure '7.
  • the embodiment, used to illustrate the invention, is shown as mounted in operative position within a gas duct D composed of wood. As shown, it includes interstitial upstream and downstream electrodes I and 2, which extend across the duct D and which are spaced from each other. 'Ihese electrodes may be composed of any suitable material, such, for example, as ordinary metal window screening material having a mesh large enough to avoid appreciable obstruction to the gas ilow.
  • the screen electrodes I and 2 are mounted on shallow rectangular frames la and 2a and arranged for connection to a suitable source of direct current which is indicated at 3.
  • the upstream and downstream electrodesA are shown as being connected to the positive and negative sides respectively of the direct current supply 3 but this is not essential and such connections may be reversed.
  • the dielectric separator includes an interstitial filter-medium 4 which possesses dielectric properties. While various filter mediums may be used, better results appear possible of attainment with those composed of short fibers. Particularlygood results have been obtained with a paper medium composed of a plurality of superimposed separable layers of sheet-like fibrous material, wherein each sheet comprises a thin matted net work of short fibered wood pulp, characterized by a multitude of fine air strainer openings. A highly satisfactory medium of this character is disclosed in Patent No.
  • the medium may be stretched straight across the gas flow with its upstream and downstream faces, either in contact with or minutely spaced from the upstream and downstream electrodes respectively.
  • This arrangement produces excellent cleaning results, but has the disadvantage of introducing a gasiiow resistance high enough to limit the gas flow velocities to values substantially under feet per minute.
  • the medium is preferably arranged in zigzag form. to provide a face area large enough to insure a satisfactorily low gas flow resistance with velocities ranging as high as 300 feet per minute.
  • a stiffener or cardboard spacer 5 is preferably arranged in each fold of the medium to support it and laterally corrugated to maintain free gas iiow spaces leading to and from each fold.
  • the medium 4 and spacers 5 may be mounted within the confines of an enclosing frame 6, having open upstream and downstream gas flow faces, and held therein by retaining flanges 6a, which extend laterally inward from the frame a short distance over the upstream and downstream margins of the filtering medium, as a whole.
  • the resulting filtering unit should be arranged between electrodes with its opposed faces in substantial contact therewith. As indicated before, if actual physical contact is not made, the spacing between the medium and the electrodes should be limited to minute distances in order to maintain an effective electrostatic relation between opposed surfaces. While this arrangement is capable of producing good results, I have found Vthat equally good and possibly better results can be secured with less power consumption by interposing between one face of the unit and one of the electrodes, preferably the upstream electrode, another dielectric body.
  • the separator therefore, also includes a dielectric body, preferably in the form of a series of laterally spaced parallel glass plates 1, extending in the direction of the gas flow. While I prefer the use of glass as a dielectric, it is to be understood that various other dielectric materials, including wood, have been and may be successfully used.
  • the dielectric body 1 should have its opposed faces in contact with, or minutely spaced from both the upstream electrode and the upstream face of the filtering unit.
  • the plates should be placed as close together as they can be without interposing any appreciable obstruction to the air flow. Ordinarily, a lateral spacing substantially under 2" and preferably around 1A" will be satisfactory.
  • the faces of the glass plates 1 may be coated if desired with relatively small particles of a different dielectric material such, for example, as crude vermiculite i. e. a flaky micaceous mineral.
  • a ⁇ coating of particulate or discrete dielectric material while not essential is, therefore, shown as indicated. at 8 in Figure 2.
  • the dielectric separator should occupy substantially the entire gas flow depth of the electric field between electrodes, and should either provide good contact throughout that depth oryavoid such contact by minute clearances only.
  • satisfactory contact between the upstream face of the separator'and the upstream electrode is easily secured. Due to surface irregularities of the filter unit, satisfactory contact or clearance between each face of the filter unit and the opposed faees of adjacent parts may not be so readily obtained.
  • a somewhat resilient, interstitial body 9 can be interposed and slightly compressed between each face of the lter unit and the adjacent faces of the dielectric 1 on one side and the downstream electrode 2 on the other.
  • the interposed body 9 in each case may be made of material having either electrically conductive or dielectric properties.
  • electrically conductive materials are used, they are preferably made in the form of a resilient pad or sheet, such, for example, as a pad or sheet of steel wool or of copper mesh fabric, the latter material being of the character shown in Patent No. 1,676,191 granted July 3, 1928.
  • electrical air cleaners having ionizers arranged in advance of cloth and other like filter mediums, have heretofore been proposed.
  • the ionizer 3o operates to agglomerate fume and smoke particles to a size which'facilitates their mechanical flltration from the air.
  • these arrangements contemplate the use of low air- K fiow velocities and the provision of substantial spacing between the ionizer and filter medium in A order to allow sulcient time for the agglomeration to take place.
  • the size of the agglomerates is so small as to require a dense filter medium to effect their mechanical filtra- 40 tion from the air.
  • a conventional ionizer having largeand small electrodes I0 and AI I, is arranged close enough to the upstream face of the filter medium to charge it with an effective 60.- electrostatic potential.
  • FIG. 1 A practicalembodiment of the structure schematically illustrated in Figure' is shown in Fig- Q ures '7 and '8.
  • the filter illustrated is not an all metal filter but, on the contrary, is an insulated filter in which the ngers I2 and I3 are composed of some insulating material such as Bakelite while a Bakelite screen? is placed on the air-outlet frame W in place of the metal screen normally used. Additionally, the frames M and W are respectively provided with charging electrodes I and 2. With this arrangement, good results have been obtained when either set or both sets of electrodes were energized with direct current at 12,000 volts.
  • the maximum permissiblespacing between the ionizer and filter medium will depend upon various factors which aifect the dissipation of the generated charge and since such factors will vary in different installations, it is diiiicult accurately to define the 0 maximum spacing limit; hence, in each particular installation, it may be necessary to determine such limit experimentally should conditions re.- quire the use of maximum spacing.
  • the generated charge apparently was entirely dissipated when a spacing of 15 feet was employed between an ionizer and filter medium in a metal duct having an area 24" x 24". It should suilice to say that the smaller spacings are recommended, that a minimum of metal be interposed between the ionizer and ⁇ filter medium in order to minimize the dissipation of the charge and that, to promote safety, all interposed metal be grounded.
  • An electric gas cleaner comprising: spaced upstream and downstream interstitial electrodes; an interstitial dielectric body arranged within the electric held space between electrodes and substantially in contact with the upstream electrode; and an interstitial dielectric air filter medium interposed between and in electrical contact with said dielectric body and said downstream electrode.
  • An electric gas cleaner comprising: spaced upstream and downstream interstitial electrodes; a series of laterally spaced substantially parallel dielectric plates extending from the upstream electrode toward the downstream electrode; and
  • a gas ow duct of an electrical gas cleaning device comprising: spaced upstream and downstream interstitial electrodes, each electrode extending laterally across the gas ow space of said duct; and an interstitial dielectric separator substantially occupying -the gas flow space of the duct between electrodes.
  • said meansin includes an ionizer ir. said gasiiow duct positioned upstream of said dielectric illter medium and suiiiciently close to the upstream face of. said dielectric lter medium to prevent the dissipation of charges imposed on the particles in the gas ow by said ionizer prior to their reaching said dielectric iilter medium.

Description

,` 1940 5 SheebS-Sheet l Filed Sept. 5
.NIN Il CHAPLES W WHL/MM5 c@ fNr/wrog Sept- 29, 1942. v C. w. WILLIAMS 2,297,601
ELECTRIC GAS CLEANER i, m' Filed Sept: 3, 1940 3\Sheeks -Sheet 2 mi l n e2 LLI Y N CHARLESWW/LL/AMJMJm/wro 12,000 volts) between the' Patented Sept. 1942 ELECTRIC Gas CLEANER Charles W. Williams, Louisville, Ky., assignor to American Air Filter Company, Inc.,
Louisville,
Ky., a corporation of Delaware Application September 3, 1940, Serial No. 355,277
(ci. 18s-7) 8 Claims.
duct; and an interstitial dielectric separator substantially occupying the gas now space of the duct between electrodes. l
This invention relates to the art of cleaning gases electrically. In the practical application of this art, gas borne "dust particles are electrically charged by impressing high ionizing voltages between laterally spaced electrodes to create an electrical field and passing the gas longitudinally through the field -so created. Particles charged or ionized in this manner` gravitate slowly across the gas flow toward oppositely charged surfaces upon which they are intended ultimately to precipitate and collect.
To create an electrical field, ionizing voltages ranging from 30,000 to 4more than 80,000 volts have been employed. Those high voltages necessitate wide spacing between electrodes, to avoid disruptive ash overs," while wide spacing, coupled with slow lateral movement of charged particles, tend to maximize the contact time required between the gas and the collecting surfaces to effect cleaning. Under such conditions the use of low gas velocities and long collecting surfaces is promoted.
It has been proposed to reduce contact or cleaning time by rst passing the gas through a. shallowelectric charging or ionizing field, created by impressing high voltages between the adjacent widely spaced short electrodes of a laterally arranged series, and then passing the charged gas through a deep electric collecting field, created by impressing a relatively low voltage (e. g. adjacent narrowly spaced long plate-like electrodes of a'laterally arranged series. AWhile such arrangement appears to eect a reductionV in cleaning time over.
other arrangements in which the charging and collecting neld are the same, the optimum results appear to be limited.
With the collection of dust accomplished,y the v l problem of its kremoval is presented. `Up to the present time-this has been done largely. .by jarring, scrapingl or similarly dislodging `the collected dustfrom the collectingY surfaces or by iiushing such vsurfacesso as to wash the dust therefrom.` As indicated in Patent No. 1,800,529, cleaning methods of this general. character involve many diiiiculties which lead to many com- 65 plexities. In fact, they have been so highly unsatisfactory that a considerable part of the time and effort spent by those actively engaged in the general development oi' this art has necessarily been diverted to the problem of removing collected. dust.
An important object of this invention is to avoid or minimize the foregoing limitations and e objections, and, more particularly, to provide an improved form oi' device for effectively cleaning gas electrically, wherein the use of lower voltages and higher velocities are promoted and the removal of collected dust is facilitated.
'A further object is to provide in a device o f this character an inexpensive dust collecting medium which can be easily and quickly removed and replaced.
A still furtherobiect is to provide a compact device having desirable operating characteristics, such as lowsoperating voltage, high gas handling capacity, low gas iiow resistance and high gas cleaning eiiiciency, and minimum maintenance requirements, such as low power consumption and low reconditioning expense.
. Another important object is to maintain an effective electrostatic charge or4 potential upon a dielectric lter` mediumf through which gas is passed.
I have discovered that the foregoing objectives may be largely attained by occupying the electric eld, created between suitably spaced interstitial upstream and downstream electrodes, with an interstitial dielectric separator comprising a dielectric air filter medium, and passing a gas successively through the interstices of the upstream electrode, the separator and the downstream electrode..
In other words,the gas is passed through the openings of an interstitial dielectric separator, while a potential difference is maintained betweenthe upstream and downstream faces of the separator. With an arrangement of this character, I have been able to obtain excellent cleaning results even when yusing operating voltages as low as 5,000 volts and gas velocities as high as 300 F. P. M. The danger of iiash overs" is substantially nil since theV spacing of electrodes can be varied sub-v stantially within safe limits'without appearing to aii'eci;A the 'cleaning eiiiciency v suspended particles, .collected ,in ythis way have ylargelyl been deposited upon the air filter medium hence their removal maybe effected simply by removing the filter. Since the foregoing results are possible of attainment with to any appreciable extent. Fume, smoke and other the use ot an inexpensive `filter having a low gas now resistance, it will be readily appreciated that the arrangement makes possible the attainment of excellent operating characteristics in an electric gas cleaning device having minimum maintenance requirements.
The invention is illustrated in the accompanying drawings wherein:
Figure 1 is a vertical section taken through one embodiment of the invention in its operative gas cleaning position;
Figure 2 is an enlarged fragmentary view taken from Figure l, in which the details are exaggerated for the sake of clearness;
Figure 3 is a similarly enlarged fragmentary viewv taken at right angles to Figure 2;
Figure 4 is a partly broken view of the upstream end of the device;
Figure 5 is a partly broken view of the downstream end of the device;
Figure 6 is a schematic view of an alternative arrangement for carrying out the invention;
Figure 7 is a practical embodiment of the arrangement shown in Figure 6; and
Figure 8 is a detail of the air filter structure shown in Figure '7.
The embodiment, used to illustrate the invention, is shown as mounted in operative position within a gas duct D composed of wood. As shown, it includes interstitial upstream and downstream electrodes I and 2, which extend across the duct D and which are spaced from each other. 'Ihese electrodes may be composed of any suitable material, such, for example, as ordinary metal window screening material having a mesh large enough to avoid appreciable obstruction to the gas ilow. The screen electrodes I and 2 are mounted on shallow rectangular frames la and 2a and arranged for connection to a suitable source of direct current which is indicated at 3. The upstream and downstream electrodesA are shown as being connected to the positive and negative sides respectively of the direct current supply 3 but this is not essential and such connections may be reversed. The experiments conducted with this device indicate that, while ,good cleaning results can be secured with an operating voltage of 5,000 volts, better results may possibly be obtained with higher voltages. For this reason, a higher voltage of, say, 12,000 volts, is suggested but even that may be raised or lowered if desired.
When the desired voltage is impressed on the electrodes, an electric field will be created between electrodes. Within this field the dielectric separator is placed. The dielectric separator includes an interstitial filter-medium 4 which possesses dielectric properties. While various filter mediums may be used, better results appear possible of attainment with those composed of short fibers. Particularlygood results have been obtained with a paper medium composed of a plurality of superimposed separable layers of sheet-like fibrous material, wherein each sheet comprises a thin matted net work of short fibered wood pulp, characterized by a multitude of fine air strainer openings. A highly satisfactory medium of this character is disclosed in Patent No. 1,897,976 granted February 14, 1933.` The medium may be stretched straight across the gas flow with its upstream and downstream faces, either in contact with or minutely spaced from the upstream and downstream electrodes respectively. This arrangement produces excellent cleaning results, but has the disadvantage of introducing a gasiiow resistance high enough to limit the gas flow velocities to values substantially under feet per minute. For that reason the medium is preferably arranged in zigzag form. to provide a face area large enough to insure a satisfactorily low gas flow resistance with velocities ranging as high as 300 feet per minute.
With the medium in zigzag form, a stiffener or cardboard spacer 5 is preferably arranged in each fold of the medium to support it and laterally corrugated to maintain free gas iiow spaces leading to and from each fold. The medium 4 and spacers 5 may be mounted within the confines of an enclosing frame 6, having open upstream and downstream gas flow faces, and held therein by retaining flanges 6a, which extend laterally inward from the frame a short distance over the upstream and downstream margins of the filtering medium, as a whole.
The resulting filtering unit should be arranged between electrodes with its opposed faces in substantial contact therewith. As indicated before, if actual physical contact is not made, the spacing between the medium and the electrodes should be limited to minute distances in order to maintain an effective electrostatic relation between opposed surfaces. While this arrangement is capable of producing good results, I have found Vthat equally good and possibly better results can be secured with less power consumption by interposing between one face of the unit and one of the electrodes, preferably the upstream electrode, another dielectric body.
The separator, therefore, also includes a dielectric body, preferably in the form of a series of laterally spaced parallel glass plates 1, extending in the direction of the gas flow. While I prefer the use of glass as a dielectric, it is to be understood that various other dielectric materials, including wood, have been and may be successfully used. The dielectric body 1 should have its opposed faces in contact with, or minutely spaced from both the upstream electrode and the upstream face of the filtering unit. The plates should be placed as close together as they can be without interposing any appreciable obstruction to the air flow. Ordinarily, a lateral spacing substantially under 2" and preferably around 1A" will be satisfactory.
The faces of the glass plates 1 may be coated if desired with relatively small particles of a different dielectric material such, for example, as crude vermiculite i. e. a flaky micaceous mineral. A `coating of particulate or discrete dielectric material while not essential is, therefore, shown as indicated. at 8 in Figure 2.
The dielectric separator, as a whole, should occupy substantially the entire gas flow depth of the electric field between electrodes, and should either provide good contact throughout that depth oryavoid such contact by minute clearances only. In the arrangement shown, satisfactory contact between the upstream face of the separator'and the upstream electrode is easily secured. Due to surface irregularities of the filter unit, satisfactory contact or clearance between each face of the filter unit and the opposed faees of adjacent parts may not be so readily obtained. To insure good contact, a somewhat resilient, interstitial body 9 can be interposed and slightly compressed between each face of the lter unit and the adjacent faces of the dielectric 1 on one side and the downstream electrode 2 on the other. The interposed body 9 in each case may be made of material having either electrically conductive or dielectric properties. Where electrically conductive materials are used, they are preferably made in the form of a resilient pad or sheet, such, for example, as a pad or sheet of steel wool or of copper mesh fabric, the latter material being of the character shown in Patent No. 1,676,191 granted July 3, 1928.
The gas iiow depth of the foregoing arrange.
ment may be varied widely within safe limits without appearing appreciably to affect the effectiveness of its operation. For example, with an operating voltage of 12,000 volts, the cleaning results obtained when the air flow depth of the glass plates was 11/2", o'f the iilter unit 4" and of the'device, as a whole, 6", were not noticeably varied even after the overall air flow depth was increased to 10" by correspondingly increasing the depth of the plates. No attempt is herein made to explain principle governing the operation of this device. It has been noted, however, that in operation particles are effectively deposited on the filter medium, principally in the areas where it either contacts other surfaces or is minutely spaced therefrom. Particle deposits have been noted not only at the points of contact or minute spacing between the filter medium and the adjacent upstream and downstream surfaces, but also at all points of contact or minute spacing between the filter medium l and other material such as the spacers 5.
In the'operation of this gas cleaner, it has also been observed: that ozoneis not produced in noticeable amounts if at all; that current variations, ranging from one microampere to one-half milliampere, appear to produce no observable change in its effectiveness; and that the effectiveness of the device is not instantly gained or lost upon connection to or disconnection from Y power, but on the contrary is gradually built up or dissipated over a period of time on the order of ten minutes more or' less. Consequently, although the underlying principle of operation has not been definitely ascertained, these observations may indicate that ionization is not the determining factor. It has been suggested that the effect may be due to polar or charged particles being forced from the air stream in a non-uniform electric eld. It may be, and I am strongly inclined to believe that it is, due to the distribution of charges of static electricity over the surface of the lter medium. From all indications, it would appear that charges of static electricity are distributed over the medium, that dust particlesfare effectively precipitated when brought under the influence of such charges, and
that the emciency of 'separation is proportional to what I term the electrostatic potential of the medium, thatis to say the number of charges which can be maintained upon the medium. All
this is indicated by the results secured in opy erating the arrangements shown in Figures 6 and 7.
I have discovered that the arrangement shown in Figures 1- through 5 may begreatly improved by eliminating the material `interposed between the dielectric kfilter medium 'I and the charging' electrodes I` and 2, and by placing'such electrodes into direct .contact with the filter mev dium or otherwise causing themediumto be charged with an effective electrostatic potentialff An Aarrangement of` this character is schematically indicated in Figure 6.
In this arrangement,` good results have been obtainedwith filter media such as Airmat," the paper disclosed in Patent #1,897,976, felted wool,
canton flannel, organdy, voile, rayon, matted` 5 composed wholly of short fibers or having a mul- 1 titude of such .fibers forming a nap over its surface. While upstream and downstream electrodes in the form of window-screen may be employed, electrodes composed of laterally spaced rods or wires are preferred' and illustrated in Figure 6. These electrodes maybe disposed on the same side of the medium, on opposite sides thereof, or on both sides, but, in any event, they preferably are placed in good contact with the medium along their length and laterally spaced sufficiently to prevent fiash-over. A direct 4current charging voltage of 12,000 volts is preferred, although this may be varied up or down as desired.
I have also discovered that a` conventional ionizer may be used in place of,or in combination with the charging electrodes I and 2 with good effect provided it is placed sufiiciently close to the filter medium to charge it with an eective electrostatic potential. In this connection, it
may be noted that electrical air cleaners, having ionizers arranged in advance of cloth and other like filter mediums, have heretofore been proposed. In these cleaners, however, the ionizer 3o operates to agglomerate fume and smoke particles to a size which'facilitates their mechanical flltration from the air. So 'far as is known, these arrangements contemplate the use of low air- K fiow velocities and the provision of substantial spacing between the ionizer and filter medium in A order to allow sulcient time for the agglomeration to take place. Even then, the size of the agglomerates is so small as to require a dense filter medium to effect their mechanical filtra- 40 tion from the air.
\ I have discovered that when a dielectric filter medium i's placed close to the downstream side of an ionizer, a substantial number of the electrostatic charges generated by the ionizer collect upon the lter medium, thus charging it with an electrostatic potential which iseffective to `precipitate substantialquantities of smoke and fume,`whereas, when it is spaced a substantial distance away from the downstream side of the ionizer, most, if not all, of the generated Fcharges are dissipated in some way before they 4reach the filter medium, with the result that it is charged with little or no electrostatic potential and, therefore, ineffective to precipitate even small quantitiesof smoke and fume. Ac-
v cordingly, when its use is desired, a conventional ionizer, having largeand small electrodes I0 and AI I, is arranged close enough to the upstream face of the filter medium to charge it with an effective 60.- electrostatic potential.
` A practicalembodiment of the structure schematically illustrated in Figure' is shown in Fig- Q ures '7 and '8. In this embodiment, an air Afilter of the 'type shown in the Nutting Patent 6;, .#2,211,382 granted August 13, 1940, is used, this filter comprising: a unitary'open-endedvair inlet frame M having outer side walls for confining -the airpassing through the frame, two laterally spaced side walls `being serrated to form two 70,1laterally spaced series of fingers vI2 extending in the direction of air flow: another unitary open-ended air outlet frame W having corresponding side walls, serrations and fingers I3, the latter being matable with the Ifingers I2 of the frame M and cooperating therewith, when the frames M`and W are mated, to pinch the intervening portion of a filter medium I interposed between the frames; and a corrugated screen I4 on the frame W to support'the filter medium against the force ofthe air flow.
Good results have been obtained with Aa dielectric filter medium 4 interposed between all metal frames M and W when such frames were operated in connection with an ionizer and either connected to ground or disconnected therefrom. For purposes of safety, however, a ground connection to the all metal frame is preferred.
In Figures 7 and 8, however, the filter illustrated is not an all metal filter but, on the contrary, is an insulated filter in which the ngers I2 and I3 are composed of some insulating material such as Bakelite while a Bakelite screen? is placed on the air-outlet frame W in place of the metal screen normally used. Additionally, the frames M and W are respectively provided with charging electrodes I and 2. With this arrangement, good results have been obtained when either set or both sets of electrodes were energized with direct current at 12,000 volts. For example, with a filter 24 x 24" in cross section, fitted withina wooden duct'D and positioned with its upstream face spaced 4" from the downstream face of the ionizer (or 9" from a vertical plane passing through the longitudinal axes of the ionizing electrodes I and II) and with both sets of electrodes energized by a direct current of 12,000 volts, cleaning-eidciency tests were conducted with various dielectric filter mediums using atmospheric air as the medium to be cleaned. The cleaning efficiencies obtained were measured by the discoloration method which is published in the August 1938 edition of the Joumal Section of the Heating, Piping and Air conditioning magazine. These results follow:
Per cent cleaning efficiencies Filter medium Sub' Initial quent Woven glass Below 40 Y 40 Ms" ply matted glass. 43 44 Rayon. 50 50 Voile l 60 Org dy 60 60 14 oz Ie ted wool 55 65 Same with surface roughened..- 80 82. 5 Same with surface rcsmoothed- 75 75 l2 oz. canton flannel 65 90 Same with surface singed 65 80 10 ply Airma 85 85 It will be understood that the emciencies shown by the discoloration method indicate the ability of the filter medium to remove smoke, fume and other extremely fine particles which cannot be effectively removed from air by mechanical illtration, When-the same test method is employed to measure the cleaning efficiencies of any-of the mediums above noted, such as Airmat, under conditions in which it is not subjected to an electrostatic charge or potential,
,the efficiencies obtained are substantially unaceaeci to ground, whereas this current dropped to 0.1 micro-amperes when such spacing was increased to 9". Again with an all metal filter connected to ground and having its upstream face spaced 3", 6" and 9" from a vertical plane passing' through th'e longitudinal axes of ionizing electrodes I0 and II energized at 20,000 volts, leakage currents of 100, 10 and 5 micro-amperes respectively were observed'in the ground connection of the filter. The amount of current in such ground 4connections appears to be an indication of the electrostatic potential of the filter medium,
and, as such, shows that such potential decreases rapidly with increases in the spacing between the filter and the ionizer. Nevertheless, while this is true, a small leakage current should not be taken as an absolute indication that the electrostatic potential of the filter mediumis ineffective, because the magnitude of the leakage current not only depends upon the magnitude of the electrostatic potential but upon the resistance afforded tothe flow of current. In this connection, it has been noted that the amount of leakage current normally'increases with an increase in the humidity of the atmosphere, although, at the same time, the efliciencies of the filter medium, and, no doubt, the magnitude of the electrostatic potential, decreases.
Generally speaking, it may be said that good results will always be obtained when an effective electrostatic potential is maintained on the filter medium, and that the maintenance of an effective electrostatic potential will be promoted by using short-fibered or napped filter mediums, by using the highest practical voltage or by increasing the dryness of the air o r gas being cleaned, where this is possible, and by decreasing the spacing between the filter medium and the ionizer when the latter is used. Since the maximum permissiblespacing between the ionizer and filter medium will depend upon various factors which aifect the dissipation of the generated charge and since such factors will vary in different installations, it is diiiicult accurately to define the 0 maximum spacing limit; hence, in each particular installation, it may be necessary to determine such limit experimentally should conditions re.- quire the use of maximum spacing. In this connection, it may be noted that the generated charge apparently was entirely dissipated when a spacing of 15 feet was employed between an ionizer and filter medium in a metal duct having an area 24" x 24". It should suilice to say that the smaller spacings are recommended, that a minimum of metal be interposed between the ionizer and `filter medium in order to minimize the dissipation of the charge and that, to promote safety, all interposed metal be grounded.
Having described my invention, I claim:
1. An electric gas cleaner comprising: spaced upstream and downstream interstitial electrodes; an interstitial dielectric body arranged within the electric held space between electrodes and substantially in contact with the upstream electrode; and an interstitial dielectric air filter medium interposed between and in electrical contact with said dielectric body and said downstream electrode.
2. An electric gas cleaner comprising: spaced upstream and downstream interstitial electrodes; a series of laterally spaced substantially parallel dielectric plates extending from the upstream electrode toward the downstream electrode; and
'a dielectric air filter medium arranged between aser/,eci
and in contact with the downstream electrode and the downstream edges of said plates.
3. A device as claimed i'n claim 2, wherein said lmedium is composed of fibrous material;
4. A device as claimed in claim 2, wherein said medium is composed of short bred material matted to form a. highly porous net work.
5. The combination with' a gas ow duct of an electrical gas cleaning device comprising: spaced upstream and downstream interstitial electrodes, each electrode extending laterally across the gas ow space of said duct; and an interstitial dielectric separator substantially occupying -the gas flow space of the duct between electrodes.
6. The combination with `a gas flow duct of an electrical gas cleaning device comprising: an interstitial dielectric lter medium with upstream andgdownstream air-flow faces extending across and means to establish and maintain an electrostatic potential on said idter medium to substantially increase the collecting ability of said filter medium for relatively iine particles including particles of smaller size than the interstices in said iilter medi said duct to lter the gas passing therethrough, l
7. The combination dened in claim 6 wherein: -said means include charging electrodes in physical contact with said dielectric illter medium.
8. 'I'he combination deiined in claim 6 wherein: said meansincludes an ionizer ir. said gasiiow duct positioned upstream of said dielectric illter medium and suiiiciently close to the upstream face of. said dielectric lter medium to prevent the dissipation of charges imposed on the particles in the gas ow by said ionizer prior to their reaching said dielectric iilter medium.
CHARLES W. WILLIAMS
US355277A 1940-09-03 1940-09-03 Electric gas cleaner Expired - Lifetime US2297601A (en)

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Cited By (44)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2428328A (en) * 1942-09-05 1947-09-30 American Cyanamid Co Process of removing bacteria from fluids
US2502560A (en) * 1946-10-18 1950-04-04 American Air Filter Co Electrical gas cleaner unit
US2579445A (en) * 1949-01-28 1951-12-18 Westinghouse Electric Corp Electrostatic precipitator
US2579441A (en) * 1950-02-25 1951-12-18 Westinghouse Electric Corp Electrostatic precipitator
US2589463A (en) * 1950-05-31 1952-03-18 Westinghouse Electric Corp Electrostatic precipitator
US2593377A (en) * 1946-05-15 1952-04-15 Research Corp Gas cleaning apparatus
US2626008A (en) * 1947-01-02 1953-01-20 Westinghouse Electric Corp Electrical precipitator
US2729302A (en) * 1949-02-11 1956-01-03 American Air Filter Co Electrostatic filter
US2814355A (en) * 1955-09-14 1957-11-26 Gen Electric Electrostatic gas filter
US2818134A (en) * 1956-07-20 1957-12-31 Gen Electric Electrostatic gas filter
US2822058A (en) * 1955-08-30 1958-02-04 Westinghouse Electric Corp Electrostatic precipitators
US2844214A (en) * 1955-07-11 1958-07-22 Wayne C Hall Electrostatic precipitator
US2847082A (en) * 1955-11-03 1958-08-12 Westinghouse Electric Corp Electrostatic precipitators
US2864460A (en) * 1957-01-10 1958-12-16 Gen Electric Electrode arrangement for electrostatic gas filter
US2898438A (en) * 1956-10-30 1959-08-04 Gen Motors Corp Domestic appliance
US2908347A (en) * 1957-10-21 1959-10-13 Westinghouse Electric Corp Electrostatic precipitators
US2990912A (en) * 1959-10-21 1961-07-04 Cottrell Res Inc Electrical precipitator and charged particle collecting structure therefor
US3018845A (en) * 1957-12-12 1962-01-30 Milton A Powers Filters
US3040497A (en) * 1954-12-08 1962-06-26 Schwab Louis Electrostatic gas filters
US3105750A (en) * 1959-07-29 1963-10-01 Mc Graw Edison Co Electrostatic filter apparatus
US3237387A (en) * 1960-04-20 1966-03-01 Skuttle Mfg Co Filter assembly
US3242649A (en) * 1963-09-17 1966-03-29 American Air Filter Co Electrical gas cleaner
US3271932A (en) * 1965-07-21 1966-09-13 Gen Electric Electrostatic precipitator
DE1226080B (en) * 1954-05-29 1966-10-06 American Air Filter Co Air filter cartridge made of dielectric material
US3386227A (en) * 1966-09-01 1968-06-04 American Air Filter Co Electrostatic filter device
US3724174A (en) * 1970-09-28 1973-04-03 Bergwerksverband Gmbh Electrically operated dust mask
US3744216A (en) * 1970-08-07 1973-07-10 Environmental Technology Air purifier
US3800509A (en) * 1972-02-14 1974-04-02 Carrier Corp Electrostatic precipitator
US3910779A (en) * 1973-07-23 1975-10-07 Gaylord W Penney Electrostatic dust filter
US3945813A (en) * 1971-04-05 1976-03-23 Koichi Iinoya Dust collector
US4357150A (en) * 1980-06-05 1982-11-02 Midori Anzen Co., Ltd. High-efficiency electrostatic air filter device
DE3237780A1 (en) * 1981-10-12 1983-04-28 Senichi Tokyo Masuda HIGH-PERFORMANCE ELECTROSTATIC FILTER ARRANGEMENT
US4405342A (en) * 1982-02-23 1983-09-20 Werner Bergman Electric filter with movable belt electrode
US4555252A (en) * 1983-06-04 1985-11-26 Dragerwerk Aktiengesellschaft Electrostatic filter construction
US4715870A (en) * 1984-02-18 1987-12-29 Senichi Masuda Electrostatic filter dust collector
US4750921A (en) * 1984-06-22 1988-06-14 Midori Anzen Industry Co., Ltd. Electrostatic filter dust collector
US4853005A (en) * 1985-10-09 1989-08-01 American Filtrona Corporation Electrically stimulated filter method and apparatus
US4940470A (en) * 1988-03-23 1990-07-10 American Filtrona Corporation Single field ionizing electrically stimulated filter
US4978372A (en) * 1988-03-11 1990-12-18 William Pick Pleated charged media air filter
US5108470A (en) * 1988-11-01 1992-04-28 William Pick Charging element having odor and gas absorbing properties for an electrostatic air filter
US6491743B1 (en) * 2000-09-11 2002-12-10 Constantinos J. Joannou Electronic cartridge filter
US20080108119A1 (en) * 2004-02-26 2008-05-08 Gert Bolander Jensen Method, Chip, Device and System for Extraction of Biological Materials
US20080190219A1 (en) * 2004-02-26 2008-08-14 Gert Bolander Jensen Method, Chip, Device and System For Collection of Biological Particles
US20080220414A1 (en) * 2004-02-26 2008-09-11 Thomsen Bioscience A/S Method, Chip, Device and Integrated System for Detection Biological Particles

Cited By (47)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2428328A (en) * 1942-09-05 1947-09-30 American Cyanamid Co Process of removing bacteria from fluids
US2593377A (en) * 1946-05-15 1952-04-15 Research Corp Gas cleaning apparatus
US2502560A (en) * 1946-10-18 1950-04-04 American Air Filter Co Electrical gas cleaner unit
US2626008A (en) * 1947-01-02 1953-01-20 Westinghouse Electric Corp Electrical precipitator
US2579445A (en) * 1949-01-28 1951-12-18 Westinghouse Electric Corp Electrostatic precipitator
US2729302A (en) * 1949-02-11 1956-01-03 American Air Filter Co Electrostatic filter
US2579441A (en) * 1950-02-25 1951-12-18 Westinghouse Electric Corp Electrostatic precipitator
US2589463A (en) * 1950-05-31 1952-03-18 Westinghouse Electric Corp Electrostatic precipitator
DE1226080B (en) * 1954-05-29 1966-10-06 American Air Filter Co Air filter cartridge made of dielectric material
US3040497A (en) * 1954-12-08 1962-06-26 Schwab Louis Electrostatic gas filters
US2844214A (en) * 1955-07-11 1958-07-22 Wayne C Hall Electrostatic precipitator
US2822058A (en) * 1955-08-30 1958-02-04 Westinghouse Electric Corp Electrostatic precipitators
US2814355A (en) * 1955-09-14 1957-11-26 Gen Electric Electrostatic gas filter
US2847082A (en) * 1955-11-03 1958-08-12 Westinghouse Electric Corp Electrostatic precipitators
US2818134A (en) * 1956-07-20 1957-12-31 Gen Electric Electrostatic gas filter
US2898438A (en) * 1956-10-30 1959-08-04 Gen Motors Corp Domestic appliance
US2864460A (en) * 1957-01-10 1958-12-16 Gen Electric Electrode arrangement for electrostatic gas filter
US2908347A (en) * 1957-10-21 1959-10-13 Westinghouse Electric Corp Electrostatic precipitators
US3018845A (en) * 1957-12-12 1962-01-30 Milton A Powers Filters
US3105750A (en) * 1959-07-29 1963-10-01 Mc Graw Edison Co Electrostatic filter apparatus
US2990912A (en) * 1959-10-21 1961-07-04 Cottrell Res Inc Electrical precipitator and charged particle collecting structure therefor
US3237387A (en) * 1960-04-20 1966-03-01 Skuttle Mfg Co Filter assembly
US3242649A (en) * 1963-09-17 1966-03-29 American Air Filter Co Electrical gas cleaner
US3271932A (en) * 1965-07-21 1966-09-13 Gen Electric Electrostatic precipitator
US3386227A (en) * 1966-09-01 1968-06-04 American Air Filter Co Electrostatic filter device
US3744216A (en) * 1970-08-07 1973-07-10 Environmental Technology Air purifier
US3724174A (en) * 1970-09-28 1973-04-03 Bergwerksverband Gmbh Electrically operated dust mask
US3945813A (en) * 1971-04-05 1976-03-23 Koichi Iinoya Dust collector
US3800509A (en) * 1972-02-14 1974-04-02 Carrier Corp Electrostatic precipitator
US3910779A (en) * 1973-07-23 1975-10-07 Gaylord W Penney Electrostatic dust filter
US4357150A (en) * 1980-06-05 1982-11-02 Midori Anzen Co., Ltd. High-efficiency electrostatic air filter device
DE3237780A1 (en) * 1981-10-12 1983-04-28 Senichi Tokyo Masuda HIGH-PERFORMANCE ELECTROSTATIC FILTER ARRANGEMENT
US4405342A (en) * 1982-02-23 1983-09-20 Werner Bergman Electric filter with movable belt electrode
US4555252A (en) * 1983-06-04 1985-11-26 Dragerwerk Aktiengesellschaft Electrostatic filter construction
US4715870A (en) * 1984-02-18 1987-12-29 Senichi Masuda Electrostatic filter dust collector
US4750921A (en) * 1984-06-22 1988-06-14 Midori Anzen Industry Co., Ltd. Electrostatic filter dust collector
US4853005A (en) * 1985-10-09 1989-08-01 American Filtrona Corporation Electrically stimulated filter method and apparatus
US4978372A (en) * 1988-03-11 1990-12-18 William Pick Pleated charged media air filter
US4940470A (en) * 1988-03-23 1990-07-10 American Filtrona Corporation Single field ionizing electrically stimulated filter
US5108470A (en) * 1988-11-01 1992-04-28 William Pick Charging element having odor and gas absorbing properties for an electrostatic air filter
US6491743B1 (en) * 2000-09-11 2002-12-10 Constantinos J. Joannou Electronic cartridge filter
US20080108119A1 (en) * 2004-02-26 2008-05-08 Gert Bolander Jensen Method, Chip, Device and System for Extraction of Biological Materials
US20080190219A1 (en) * 2004-02-26 2008-08-14 Gert Bolander Jensen Method, Chip, Device and System For Collection of Biological Particles
US20080220414A1 (en) * 2004-02-26 2008-09-11 Thomsen Bioscience A/S Method, Chip, Device and Integrated System for Detection Biological Particles
US7892794B2 (en) 2004-02-26 2011-02-22 Delta, Dansk Elektronik, Lys & Akustik Method, chip, device and integrated system for detection biological particles
US7932024B2 (en) 2004-02-26 2011-04-26 Delta, Dansk Elektronik, Lys & Akustik Method, chip, device and system for collection of biological particles
US7985540B2 (en) 2004-02-26 2011-07-26 Delta, Dansk Elektronik, Lys & Akustik Method, chip, device and system for extraction of biological materials

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