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US2482642A - Separator - Google Patents

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US2482642A
US2482642A US689885A US68988546A US2482642A US 2482642 A US2482642 A US 2482642A US 689885 A US689885 A US 689885A US 68988546 A US68988546 A US 68988546A US 2482642 A US2482642 A US 2482642A
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louver
air
dust
separator
particles
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US689885A
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Sylvan Stig G Son
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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
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • B01D45/14Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by rotating vanes, discs, drums or brushes

Definitions

  • the principal object of invention is to provide a novel, simp le and highly efie'ctive means forefficiently removing thecloud particles with sufiicient rapiditym'toprevent the. formation of a riti y d e lou -11; ⁇ . i
  • Fig, 3 is a perspectiveiviewiof a novel form of louver constructedin accordance with my inv ti i I I] f
  • Fig. 4 is a vector dia'gram'showing the relative ngle; between "the approaching air and the louver;
  • K Fig. 5 is a cross sectional detail showing the relationship of the dust removing louver in a separatorof the general type described herein;
  • Fig. 6 is a similarf'view of the relationship used-in the-separator of Fig. 1;
  • v I, y, -**I?igk 7 is -an 'a "a1 section-,"partly in elevation. showing one of my ,”rotary1ouver, separators with :o'ne form of 'sec on'dary" dust removing system;
  • Fig. '8 is an axial section of a separator of the character shown in Figs l and 2 with a modified form ofairinletf I Fig; 9 is amendelevation 'of-the Fig.
  • Fig! 11 is atop plan View of the separator of F a Y 1 12 shows anem'bodime'ntlike that of FigilO but with a'rota'r'y louveri and "Fig: 13 is-a diagrammatic-section of a modified louver separatori'j H U r
  • a dust separator louver having a series of slot-defining spaced vanes extending around an axis of rotation and across the path of the primary air flow, the louver vane being of a type which is adapted, upon the establishment of rotation relatively between said main air flow and the louver, to retain the dust on th upstream side of the louver; means for establishing relative rotation between the primary air and louver; means constraining the primary air to approach the upstream side of the louver in a manner such as to exert a force on retained dust particles causing those particles to move to
  • the separator shown in Figs. 1-3 includes a blower impeller I having an axial inlet 2 mounted within a conventional blower housing 3 and ar ranged to be driven through a shaft 4 by some suitable source of power not shown.
  • the inlet face of the blower housing has an axial opening large enough to permit the impeller to be inserted into or removed from the housing. This opening is reduced to air inlet proportions, by a centrally perforated disc plate 5.
  • a louver separator L is mounted in impeller inlet 2 and arranged to project upstream therefrom, through th opening in disc plate 5.
  • Louver separator L preferably is of the semispherical or dome shape shown in the drawings It has: an annular base portion 6 forming its downstream opening and providing a means of securing it to axial inlet 2 of the impeller I; an apex portion 1 at its opposite end; and a curved side wall portion extending from the base end to the apex end and containing a series of louverforming slot-defining spaced vanes 8'.
  • Vanes 8 may be cut or stamped from an integral sheet forming the curved side walls or louver portions of the separator or they may be formed individually and then secured to the apex and base portions of the louver separator. While the vanes,
  • Relative rotation between the air and the louver may be obtained by rotating the louver or by rotating the air about the louver or by a combination of both. In Figs. 1-4 such rotation is obtained solely by rotating louver separator L.
  • the incoming air is constrained to flow axially toward louver separator L' by an inlet piece 9.
  • the shape of this piece is co-ordinated to the shape of the upstream face of the louver separator to accommodate the inlet flow of the air in a well known manner such as to provide a uniform flow of air toward, or a uniform distribution of air over, the upstream face of the louver separator.
  • vanes 8 of the louver are spaced so that the total free area of the louver slots is approximately 10 greater than the cross-sectional area of the inlet piece 9 at its upstream end.
  • louver separator L As the air axially approaches louver separator L, and while it turns to pass inwardly through the slots between vanes 8, it has a velocity component which extends along the upstream face of the louver and in the direction of the base of the louver.
  • This axial velocity component exerts on the cloud forming dust particles, which are retained on the upstream side of the louver, a force causing those particles to move, as a whole, axially through the cloud forming area toward the base of the louver separator.
  • this axial velocity component of the incoming air is utilized to move the cloud forming particles to one side of the primary air flow, such side corresponding, in the structures of Figs. 12, to the base end of the louver separator.
  • louver vanes 8 should form an adjacent acute angle on the opposite side of the same upstream face, and these angles must point in a direction opposite the di rection of louver rotation.
  • the relative approach angle is, of course, determined, at any one point, by the tip speed of the rotating louver at that point and that velocity component of the incoming air which is directed radially'inward.
  • a vane 8 is shown'rotating counterclockwise about center C with a tip speed TS, the corresponding relative velocity of the air being shown by the opposite air speed vector AS.
  • the resultant air velocity will correspond to the vector RAV, this being the relative velocity of the approach air while the angle X represents the angle of approach.
  • the relative approach angle is determined by that velocity component of the air which corresponds to the tip speed of the louver and the radially inward velocity component of the air.
  • This angle should be about10 to 15 although it may vary over a somewhat wider range.
  • the average inclination angle of the vanes will normally reach between 10 and 30, it being understood that the inclination of the upstream portion of the width of the vanes will normally be difierent from the downstream portion of the width and also that the inclination willvary with the radius of rotation to compensate for the lower tip speed.
  • the angle of relative approach of the incoming air and the width, cross-sectional shape, and'inclination of the vanes must all be co-ordinated in a manner such that the air at the base end portion of the vanes discharges at one velocity and in one direction to produce a certain static pressure with a certain total pressure while the air, at other vane portions of progressively smaller radii, must discharge'at progressively higher velocities in appropriate directions to produce progressively lower static pressures with the .same total pressure.
  • inlet piece 9 is spaced axially from disekplate 5 of the blower housing to provide an annular dust discharge opening Ill leading radially'outward from the inlet chamber at a point corresponding to theibase end portion of-the separator which is at one side of the flow of primary air through the inlet chamber.
  • annular. sheet I l is arranged to extend around dust discharge opening and between-the blower'housing and the inlet piece, to both of which it is connected, to form an: annular chamber or dust-ring l2 communicating through the dust opening I I], with the inlet chamber.
  • the dust-ring is provided with outlet and inlet passages. l 3 and it through which it may be connected to a hopper, not shown.
  • the air in the dust ring not only rotates through the dust ring but a portion bf" that air passes through outlet passage l3 into the'dust hopper'where the velocity of the air is reduced so that some of the particles settle out of the air, the relative cleaner air flowing back into the dust ring through inlet passage I l.
  • none of the primary air is diverted into the dust removal system.
  • the outward passage of the dust particles into the dust ring may be facilitated by providing the base end of the louver separator with a series of blades I5 projecting radially from the separator through dust opening Hl into dust ring I2. Such blades will also effect a positive circulation of air in the dust ring and hopper.
  • FIG. 6 which shows a similarly enlarged detail, it will be :noted that the axia1 dimensions of dust opening loa and dustring l2a are b'arelysufficient to accommodate the blades I5.
  • I have secured 94% eiiiciency ofseparationof particles in a certain size range.
  • Fig. 7' shows an arrangement which'is substan: tially the same as'thatshown in-Figs. 1-2'and 6, except thata part ofthe primary air is diverted to the dust removingsystem for the purpose of creating a positive flow of air for sweeping particles from the base end portionof the separator into the dust removal system.
  • 'dust ring [2 is connected-by an outlet passage IE to a hopper ll where the air gives up at least part of its dust load, thetrelatively'clean air passing through conduit l8back into the inlet of the separator where it again mingles with the in coming air.':...
  • FIGs: 8* and 9 show an arrangement which is substantially the same asthat shown in Figs. 1 2?and6, except that the inlet piece of the earlier figures is replaced here by a scroll'type of inlethousingwhich constrains '.'the entering' 'air tofldw tangentially'so as to create a rotating stream of air which moves axially over-the louver... Accordinglyia, scroll housing l9'is provided'having'f'a tangentially directedinlet 20 and an axially directedioutlet "2
  • This arrangement operates in substantiallyjthe same'way as the arrangements of the earlier'figures.
  • the rotating body of air is made to :rotate preferably :in' the directionopposite to the direction" of. rotationof the louver,aalthough it:.will be. understood that louver'rotation is not essential .in'this. case.
  • the manner of particle separation'and removal' is the same as before. ..,..In Figs; 10 and .1'1, alouverconstructed in accordance-with m invention-is embodied in a housing. of'the cyclone type.
  • This housin is conventionally fzprovided with; a; tangential inlet 22 leading into a cyclone chamber having a conical bottom 23 and an axial outlet 24 to discharge clean air from the top of the housing.
  • Louver separator L is placed over the axial inlet of the discharge passage. It will be well appreciated that the entering air rotates about the axis of the cyclone housing and as it rotates, it moves axially toward and over the louver separator L to pass through that separator and out of discharge passage 24. Louver separator L functions in the same manner as previously described to form a cloud of particles around its upstream face.
  • the axial component of the incoming air 7 operates to move dust particles toward apex I of the louver separator and as the particles are thus moved axially, they gradually settle out of the primary air flow into the bottom of the conical hopper.
  • Fig. 12 The arrangement shown in Fig. 12 is identical to that of Figs. 10-11, except that louver separator L is mounted for rotation within the cyclone housing.
  • discharge passage 24a of the cyclone housing is secured to the axial inlet 2a of a blower impeller Ia. rotationally mounted within blower housing 311 and arranged to be rotated by motor 25.
  • motor 25 When motor 25 is energized, the impeller will be rotated to draw a stream of air through the cyclone discharge passage 2611 into blower housing 3a.
  • the separation of dust particles and their axial movement to the bottom of conical hopper 23 is effected in the same way as described in connection with Figs. 10-11.
  • Fig. 13 illustrates a modification wherein the air being cleaned passes from the interior of a separator L to the exterior thereof as distinguished from the reverse in Fig. 1.
  • Separator L is preferably of generally cylindrical shape with vanes 8a of much the same general shape and size as those of Fig. 1 in the'side walls of the cylinder, the vanes'however being designed to intercept the dust particles on the interior of the separator.
  • the separator may be mounted on a shaft 4a for rotation.
  • the clean air passes between vanes 8a into a surrounding scroll-type housing 26 having a discharge opening 21 connected to suitable air suction means.
  • Dust ring 12b may be formed as the dust ring of Fig. 5 or the dust ring of Fig. 6.
  • the dirty air enters the interior of the separator at the left end, the clean air passing out through the separator to housing 26 and the dust to housing 28.
  • the dust particles are moved to one side of the air flow, i. e., to the outside in Fig. 1 and to the inside in Fig. 13, the particles being relatively concentrated adjacent one end of the louver, and that the means to remove the particles from the vanes is on that same side of the air flow so that it is not necessary for the concentration to enter or pass through any portion of the main air flow before being removed.
  • the dust particles can be said to be gradually concentrated and edged out of the primary air flow to a point where they are taken over by the 8 removal means' such' as the secondary air flow in the dust ring.
  • a louver dust separator for cleaning a main flow of air upon the establishment of relative rotation between the incoming air and the louver, comprising: a louver separator having a series of slot-defining, spaced blade-like vanes extending around an axis of rotation, with each vane lying transversely across the path of the main air flow, and being inclined in relation to the upstream face of the louver to'form an acute angle which points in a direction opposite to the direction of rotation of the vane relatively to the approaching air, said vanes being constructed and arranged to prevent the passage of dust through said'slots and thereby cause a cloud of dust particles to form on the upstream side of the vanes; means for constraining the incoming air flow to approach the louver in an axial direction such as to effect an axial movement of cloud particles toward one side of the air flow and thereb relatively concentrate said particles adjacent one end of the louver; a dust ring arranged on the same side of the air fiow to extend around said one end of the louver, said ring being outwardly spaced
  • louver separator of claim 1 wherein the axial dimension of the dust ring annular opening is substantially larger than the corresponding dimension of the blades at the point where they enter the opening, a substantial portion of the opening being radially lined with the vane area of the louver adjacent said one end.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
  • Separating Particles In Gases By Inertia (AREA)

Description

P 1949- s. G:SON SYLVAN 2,482,642
' SEPARATOR Filed Aug. 12, 1946 3 Sheets-Sheet 1 INVEN TOR.
I 527' 6:500 5 Ivan F107 3 f BY 1/ M M ATTORNEY p 1949. s. G:SON SYLVAN SEPARA'I'OR Filed Aug. 12, 1946 3 Sheets-Sheet 2 INVENTOR. 5h 6:500 .5 Ivan BY 7 A TTO/ZNEY Sept. 20, 1949. 5 G;$QN s v' 7 2,482,642
. SEPARATOR Filed Aug. 12, 1946 s Shee ts-Sheet 5 nvmvrozz.
577g 6:500 Sylvan BY mm m ATTORNEY Patented Sept. 2Q, 1949 PATENT OFFICE .SEPARATQR 'Stig .Ga o v 9kho1 weden s n "to American AirFilter Company, Inc., Louisville, Kyr, a' corp'orationofDelaware Application August 12, 1946, Serial No. 689,885
It. has been proposedin such U. S. Patents as Knickerbocker No, 382,614, f'l3dehniiig No. 408,- 285, Goodier Nor'645;49; ana Haber 12934,- 467 to clean an air streamby passing it through a louver which effects asharp deflection of the airflow, the dust particles being retainedfon the upstream side of ltlie louver and tending 'tOfCOI'ltinue in theiroriginal'direetion along that side. The upstream or deflecting" edges. of the slotdefining louver vanes".usually. extend at right angles transverselyacrossi the air stream while the vanes and the approaching air extend at adjacent acuteangles tofopposite sides of the upstream face of theflouver; Thisprinciple of cleaning has been ,applied 1 to" rotary structures in such U. 'S. patents as Linderoth No. 2,328,220 and possibly Newcombe"No1;420;665. 'In rotary structures. the smaller particles (usually one to 3Clai ns. 01.13347) twenty micronsmore or'less); which are retained on the upstream "sidegof the louver, collect in an area adjacent tob'ut slightly spaced from the upstream face of the louver. "They form a cloud which rotates about the louver and which, unless removed, increases in densitytoa critical value at which it loses'dust through the louver at apparently the samef rate it receives "dust from the incoming air..
While the formation of; this cloud; is difiicult toexplain, it is plausiblethat the particles in the incoming air'ar'e made to spin or rotate at increasingl faster rates as they progressively approach the louverand are thus subjected to aerodynamic forces'which-tend'to force the particles away from the louver, these forces being u counter-balanced in thecloud area by the force of the air stream whic'h tends to carry the particles through the louver.-'Ihe possibility that the particles are thus made to rotate' is indicated by these facts: first, the incoming air has one velocity component which is parallel to the upstream face of the louver and which, during deflection, initially decreases in one direction between the beginning and reversal p0ints 'of the deflection from a. high maximumgvalue to zero and then increasesin'the opposite direction between the reversal and'end points of the deflection from zero to a high maximum value; and second, as aresultof this changing velocity component, the opposite sides of eachparticle appear to be subjected" simultaneously to' relatively high and low air velocity corripoiients which apparently; bring about the aerodynamic forces that cause the particles to move away from the louver; 1
' The problem .ofremovingflthe cloudforming dustfparticle's, with sufiicient rapidity to prevent the clouds from reaching the critical density, is difiicult 'of' solution): If] Newcombes structure produces such a, cloud, f he makes noattempt to remove it. Linderoth proposesa suction skimmer which is tangentially arranged relatively to the louver surface but this arrangement, if otherwise practical, is objectionable because it involves an independently operated suction" system.
' The principal object of invention is to provide a novel, simp le and highly efie'ctive means forefficiently removing thecloud particles with sufiicient rapiditym'toprevent the. formation of a riti y d e lou -11;}. i
j nnother important object is to' provide a means which requires "little.orinoflauxiliary air flow in eflecting the removal'ar'id' which avoids the necessityf of an independently operated dust removal air' systemg l, p 1' A further object is oprovide a novel form of louver. 1 j
heinvention isillustratedinthe accompany- 'ingdrawings wherei v j @Fig'. 1 is an axia W ctionf partly inelevation, of one of myv rotary louver 1 separators Fig. 2 is a section taken on line 2-2 of Fig. 1;
Fig, 3 is a perspectiveiviewiof a novel form of louver constructedin accordance with my inv ti i I I] f Fig. 4 is a vector dia'gram'showing the relative ngle; between "the approaching air and the louver;
K Fig. 5 is a cross sectional detail showing the relationship of the dust removing louver in a separatorof the general type described herein; "Fig. 6 is a similarf'view of the relationship used-in the-separator of Fig. 1; v I, y, -**I?igk 7 is -an 'a "a1 section-,"partly in elevation. showing one of my ,"rotary1ouver, separators with :o'ne form of 'sec on'dary" dust removing system; Fig. '8 is an axial section of a separator of the character shown in Figs l and 2 with a modified form ofairinletf I Fig; 9 is amendelevation 'of-the Fig. 8 separapor; v :r o g "Fig. 10' isanfaxial section of anotherembodimerit 'in which in'y louver is stationarily mounted 'in-a cycIOne typeofhousihgjf; i
Fig! 11 is atop plan View of the separator of F a Y 1 12 shows anem'bodime'ntlike that of FigilO but with a'rota'r'y louveri and "Fig: 13 is-a diagrammatic-section of a modified louver separatori'j H U r In *gener'al ternisf ai louvr separator constructed in accordance with my invention for cleaning a primary flow of air may be described as comprising: a dust separator louver having a series of slot-defining spaced vanes extending around an axis of rotation and across the path of the primary air flow, the louver vane being of a type which is adapted, upon the establishment of rotation relatively between said main air flow and the louver, to retain the dust on th upstream side of the louver; means for establishing relative rotation between the primary air and louver; means constraining the primary air to approach the upstream side of the louver in a manner such as to exert a force on retained dust particles causing those particles to move to one side of the air flow; and means on the same side of the primary flow to remove said particles rom said flow.
The separator shown in Figs. 1-3 includes a blower impeller I having an axial inlet 2 mounted within a conventional blower housing 3 and ar ranged to be driven through a shaft 4 by some suitable source of power not shown. The inlet face of the blower housing has an axial opening large enough to permit the impeller to be inserted into or removed from the housing. This opening is reduced to air inlet proportions, by a centrally perforated disc plate 5. A louver separator L is mounted in impeller inlet 2 and arranged to project upstream therefrom, through th opening in disc plate 5. t
Louver separator L preferably is of the semispherical or dome shape shown in the drawings It has: an annular base portion 6 forming its downstream opening and providing a means of securing it to axial inlet 2 of the impeller I; an apex portion 1 at its opposite end; and a curved side wall portion extending from the base end to the apex end and containing a series of louverforming slot-defining spaced vanes 8'. Vanes 8 may be cut or stamped from an integral sheet forming the curved side walls or louver portions of the separator or they may be formed individually and then secured to the apex and base portions of the louver separator. While the vanes,
as shown, are longitudinally curved from the base end inwardly toward the apex end, they may be made longitudinally straight and arranged to extend from the base end portion either parallel with the axis of rotation or at an inwardly inclined angle to the axis of rotation so that they form in one case a cylinder and in the other case a cone. I
To obtain good air cleaning results, I have found that it is necessary; first, to establish relative rotation between the incoming air and the louver separator; second, to constrain the incoming air to approach the upstream face of the louver in such a manner as to provide an air velocity component directed along the face of the louver axially toward one end or the other of the louver and thus toward one side or the other of the primary air flow; third, toobtainasharp deflection of the air; and fourth, to obtain a somewhat uniform blower effect in the louver.
Relative rotation between the air and the louver may be obtained by rotating the louver or by rotating the air about the louver or by a combination of both. In Figs. 1-4 such rotation is obtained solely by rotating louver separator L.
In Figures 1-2, the incoming air is constrained to flow axially toward louver separator L' by an inlet piece 9. The shape of this piece is co-ordinated to the shape of the upstream face of the louver separator to accommodate the inlet flow of the air in a well known manner such as to provide a uniform flow of air toward, or a uniform distribution of air over, the upstream face of the louver separator. Preferably also vanes 8 of the louver are spaced so that the total free area of the louver slots is approximately 10 greater than the cross-sectional area of the inlet piece 9 at its upstream end. With this arrangement, as the air axially approaches louver separator L, and while it turns to pass inwardly through the slots between vanes 8, it has a velocity component which extends along the upstream face of the louver and in the direction of the base of the louver. This axial velocity component exerts on the cloud forming dust particles, which are retained on the upstream side of the louver, a force causing those particles to move, as a whole, axially through the cloud forming area toward the base of the louver separator. In other words, this axial velocity component of the incoming air is utilized to move the cloud forming particles to one side of the primary air flow, such side corresponding, in the structures of Figs. 12, to the base end of the louver separator.
To secure sharp deflection of the air by the louver, the incoming air must have a small or acute angle of relative approach on one side of the upstream face of the louver, louver vanes 8 should form an adjacent acute angle on the opposite side of the same upstream face, and these angles must point in a direction opposite the di rection of louver rotation. With a rotating louver, the relative approach angle is, of course, determined, at any one point, by the tip speed of the rotating louver at that point and that velocity component of the incoming air which is directed radially'inward. For example, in Fig. 4, a vane 8 is shown'rotating counterclockwise about center C with a tip speed TS, the corresponding relative velocity of the air being shown by the opposite air speed vector AS. With the inward air speed shown by the vector IS, the resultant air velocity will correspond to the vector RAV, this being the relative velocity of the approach air while the angle X represents the angle of approach.
With relative rotation between the louver and the incoming air, it will thus be seen that the relative approach angle is determined by that velocity component of the air which corresponds to the tip speed of the louver and the radially inward velocity component of the air. This angle should be about10 to 15 although it may vary over a somewhat wider range. The average inclination angle of the vanes will normally reach between 10 and 30, it being understood that the inclination of the upstream portion of the width of the vanes will normally be difierent from the downstream portion of the width and also that the inclination willvary with the radius of rotation to compensate for the lower tip speed.
To secure a somewhat uniform blower efiect, the angle of relative approach of the incoming air and the width, cross-sectional shape, and'inclination of the vanes must all be co-ordinated in a manner such that the air at the base end portion of the vanes discharges at one velocity and in one direction to produce a certain static pressure with a certain total pressure while the air, at other vane portions of progressively smaller radii, must discharge'at progressively higher velocities in appropriate directions to produce progressively lower static pressures with the .same total pressure. This, apparently, has not heretofore been appreciated in the air cleaning art but once the necessity of co-ordina-ting such factors, to produce a more or less uniform blower efi'ect, is realized, then it becomes obvious that the mode of effecting such co-ordination" is a matter of routine blower design; hence it should sufiice to say that, in the present case, the vanes, in accordance with well known design principles, are made .to decrease, from the large base end .to the small apex end, in width, camber and inclination; If the vanes were individually formed of constant or even increasing width: from the large base end tothe small apex end, the camber and inclinationshould bechanged accordinglyto provide a uniform blower effect with the same approach angle.
Whenan air flow is set up through the rotating louver above described, dust particles will. be retained on the upstream side of the louver and these particles will form a cloud. Since the in coming air, passing axially through inlet piece 9, approaches the louver axially and then turns inwardly to :pass' through the louver, it will be appreciated that an axial component of this flow is directed toward the base end of the louver. This axial component acts on the cloud, forcing its particles axially toward the base .end or the louverand thus increasing the relative concentration of particles at that end. If nothing more were 'done, this 'concentration'would ultimately increase to the critical value at which the cloud would begin to lose particles through the louver at a rate approximating the rate at which it receives particles from the incoming air.
In accordance withmy invention, however, means are provided to remove the particles from the baseendof the louver. Accordingly inlet piece 9 is spaced axially from disekplate 5 of the blower housing to provide an annular dust discharge opening Ill leading radially'outward from the inlet chamber at a point corresponding to theibase end portion of-the separator which is at one side of the flow of primary air through the inlet chamber. Preferably an annular. sheet I l is arranged to extend around dust discharge opening and between-the blower'housing and the inlet piece, to both of which it is connected, to form an: annular chamber or dust-ring l2 communicating through the dust opening I I], with the inlet chamber. .The' rotation of the louver will induce the air in dust ring [2 to rotate and the air forces causing that'induced flow also cause particles of dust adjacent the base end of the louver to pass outwardly into the-[dust chamber. 7 I V In Figs 1-2, the dust-ring is provided with outlet and inlet passages. l 3 and it through which it may be connected to a hopper, not shown. With this arrangement the air in the dust ring not only rotates through the dust ring but a portion bf" that air passes through outlet passage l3 into the'dust hopper'where the velocity of the air is reduced so that some of the particles settle out of the air, the relative cleaner air flowing back into the dust ring through inlet passage I l. With induced circulation of this character, none of the primary air is diverted into the dust removal system.
The outward passage of the dust particles into the dust ring may be facilitated by providing the base end of the louver separator with a series of blades I5 projecting radially from the separator through dust opening Hl into dust ring I2. Such blades will also effect a positive circulation of air in the dust ring and hopper.
The Figs. 1-2 arrangement of dust opening l0, dust ring I2, and blades [5 is shown on an enlarged scale in Fig. 6. Referring first however to 6 Fig. 5 which shows a similarly enlarged detail, it will be :noted that the axia1 dimensions of dust opening loa and dustring l2a are b'arelysufficient to accommodate the blades I5. With this Fig. 5 arrangement, I have secured 94% eiiiciency ofseparationof particles in a certain size range. In Fig.' -6, however, the corresponding axial dimensions of dust opening Ill and dust ring l2 are greatly increased so'that dust opening l0 overlies not only the base end of the separator butalso a substantial part ofthe base end portion of the vanes. With this arrangement, blades 15 cause the' air' in the dust'ring to circulate axially or sidewiseas itrotates about the axis Of rotation and, in circulating axially, the dust ring air approachingthe blades mingles with that portion of the mainair flow approaching the base end portion of the vanes. As a result, a better flow of cloud particles into the dust ring is obtained without'the diversion of any primary air flow. With the Fig. 6 arrangement,I obtain a 67% increase in efficiency over the efiiciency obtained withthe Fig. 5 arrangement, bringing the total efiici'ency'to 98% with allother factors remain ingthes'ame. r
Fig. 7' shows an arrangement which'is substan: tially the same as'thatshown in-Figs. 1-2'and 6, except thata part ofthe primary air is diverted to the dust removingsystem for the purpose of creating a positive flow of air for sweeping particles from the base end portionof the separator into the dust removal system. In this case,'dust ring [2 is connected-by an outlet passage IE to a hopper ll where the air gives up at least part of its dust load, thetrelatively'clean air passing through conduit l8back into the inlet of the separator where it again mingles with the in coming air.':...
ii"Figs: 8* and 9 show an arrangement which is substantially the same asthat shown in Figs. 1 2?and6, except that the inlet piece of the earlier figures is replaced here by a scroll'type of inlethousingwhich constrains '.'the entering' 'air tofldw tangentially'so as to create a rotating stream of air which moves axially over-the louver... Accordinglyia, scroll housing l9'is provided'having'f'a tangentially directedinlet 20 and an axially directedioutlet "2| tof iriustro conical shape. The conical shapex'of outletil'hasbeen foundito increase the separating "efliciency somewhat; This arrangement operates in substantiallyjthe same'way as the arrangements of the earlier'figures. The rotating body of air is made to :rotate preferably :in' the directionopposite to the direction" of. rotationof the louver,aalthough it:.will be. understood that louver'rotation is not essential .in'this. case. The manner of particle separation'and removal'is the same as before. ..,..In Figs; 10 and .1'1, alouverconstructed in accordance-with m invention-is embodied in a housing. of'the cyclone type. This housin is conventionally fzprovided with; a; tangential inlet 22 leading into a cyclone chamber having a conical bottom 23 and an axial outlet 24 to discharge clean air from the top of the housing. Louver separator L is placed over the axial inlet of the discharge passage. It will be well appreciated that the entering air rotates about the axis of the cyclone housing and as it rotates, it moves axially toward and over the louver separator L to pass through that separator and out of discharge passage 24. Louver separator L functions in the same manner as previously described to form a cloud of particles around its upstream face. The axial component of the incoming air 7 operates to move dust particles toward apex I of the louver separator and as the particles are thus moved axially, they gradually settle out of the primary air flow into the bottom of the conical hopper.
The arrangement shown in Fig. 12 is identical to that of Figs. 10-11, except that louver separator L is mounted for rotation within the cyclone housing. To this end discharge passage 24a of the cyclone housing is secured to the axial inlet 2a of a blower impeller Ia. rotationally mounted within blower housing 311 and arranged to be rotated by motor 25. When motor 25 is energized, the impeller will be rotated to draw a stream of air through the cyclone discharge passage 2611 into blower housing 3a. The separation of dust particles and their axial movement to the bottom of conical hopper 23 is effected in the same way as described in connection with Figs. 10-11.
Fig. 13 illustrates a modification wherein the air being cleaned passes from the interior of a separator L to the exterior thereof as distinguished from the reverse in Fig. 1. Separator L is preferably of generally cylindrical shape with vanes 8a of much the same general shape and size as those of Fig. 1 in the'side walls of the cylinder, the vanes'however being designed to intercept the dust particles on the interior of the separator. The separator may be mounted on a shaft 4a for rotation. The clean air passes between vanes 8a into a surrounding scroll-type housing 26 having a discharge opening 21 connected to suitable air suction means.
The intercepted dust continues travel in an axial direction along the inside of the separator until it passes into a dust ring 52?; which may also be of the scroll-type having a discharge opening at 28. The right end of the assembly is closed by a wall 29, which prevents the escape of dust particles except through the dust ring. Preferably impeller vanes |5a are secured to the right end of the separator to rotate therewith and aid in the removal of dust. Dust ring 12b may be formed as the dust ring of Fig. 5 or the dust ring of Fig. 6.
In operation, the dirty air enters the interior of the separator at the left end, the clean air passing out through the separator to housing 26 and the dust to housing 28.
It will be noted that in all the embodiments shown herein, the dust particles are moved to one side of the air flow, i. e., to the outside in Fig. 1 and to the inside in Fig. 13, the particles being relatively concentrated adjacent one end of the louver, and that the means to remove the particles from the vanes is on that same side of the air flow so that it is not necessary for the concentration to enter or pass through any portion of the main air flow before being removed. The dust particles can be said to be gradually concentrated and edged out of the primary air flow to a point where they are taken over by the 8 removal means' such' as the secondary air flow in the dust ring.
Having described my invention, I claim:
1. A louver dust separator for cleaning a main flow of air upon the establishment of relative rotation between the incoming air and the louver, comprising: a louver separator having a series of slot-defining, spaced blade-like vanes extending around an axis of rotation, with each vane lying transversely across the path of the main air flow, and being inclined in relation to the upstream face of the louver to'form an acute angle which points in a direction opposite to the direction of rotation of the vane relatively to the approaching air, said vanes being constructed and arranged to prevent the passage of dust through said'slots and thereby cause a cloud of dust particles to form on the upstream side of the vanes; means for constraining the incoming air flow to approach the louver in an axial direction such as to effect an axial movement of cloud particles toward one side of the air flow and thereb relatively concentrate said particles adjacent one end of the louver; a dust ring arranged on the same side of the air fiow to extend around said one end of the louver, said ring being outwardly spaced therefrom and having an annular opening communicating with the space therebetween; and a series of blades mounted on the louver to project radially into said annular opening to induce the passage of dust particles through said opening into the ring.
2. The louver separator of claim 1 wherein the axial dimension of the dust ring annular opening is substantially larger than the corresponding dimension of the blades at the point where they enter the opening, a substantial portion of the opening being radially lined with the vane area of the louver adjacent said one end.
3. The louver separator of claim 1 wherein the axial dimension of the dust ring is substantially larger than the corresponding dimension of the blades and the dust ring annular opening, and the blades are arranged to cause particles entering the dust ring to move axially toward one side of the ring.
STIG GZsON SYLVAN.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number 0 Name Date 992,260 Rush May 16, 1911 1,420,665 Newcombe June 2'7, 1922 2,039,127 Sylvan Apr. 28, 1936 2,209,607 Nutting July 30, 1940 FOREIGN PATENTS Number Country Date 365,003 France June 15, 1906
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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2738855A (en) * 1953-04-28 1956-03-20 Fallon John Apparatus for separating dust from gases
US2780309A (en) * 1948-12-10 1957-02-05 Loftheim Tor Bjorn Devices for removing dust and other impurities from air, funnel smoke and other gases, especially gases from chemical and electrochemical manufactories
US2944632A (en) * 1956-09-11 1960-07-12 Charles H Whitmore Centrifugal dust collector
US3292347A (en) * 1964-12-16 1966-12-20 Ametek Inc Dust and lint disposal apparatus
US3406504A (en) * 1966-12-13 1968-10-22 American Air Filter Co Combined gas moving and gas cleaning apparatus
US3516551A (en) * 1967-06-13 1970-06-23 Grubbens & Co Ab Cyclone separator
US3884656A (en) * 1974-06-28 1975-05-20 Clifford T Deane Recirculating air cleaner
US4095966A (en) * 1976-10-27 1978-06-20 Teledyne Industries, Inc. Air cleaner
US4285707A (en) * 1978-12-01 1981-08-25 Bbc Brown, Boveri & Company Limited Dust separator for separating dust from flowing gaseous media
US4685942A (en) * 1982-12-27 1987-08-11 General Electric Company Axial flow inlet particle separator

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR365003A (en) * 1906-04-07 1906-09-01 Robert Scheibe Equipment for the removal of materials accompanying gases and vapors
US992260A (en) * 1908-05-27 1911-05-16 Charles A Rush Vaporizer and separator.
US1420665A (en) * 1920-05-10 1922-06-27 John W Newcombe Centrifugal dust separator
US2039127A (en) * 1933-08-23 1936-04-28 American Air Filter Co Rotary dust separator
US2209607A (en) * 1938-08-01 1940-07-30 American Air Filter Co Blade tip for rotary dust separators

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR365003A (en) * 1906-04-07 1906-09-01 Robert Scheibe Equipment for the removal of materials accompanying gases and vapors
US992260A (en) * 1908-05-27 1911-05-16 Charles A Rush Vaporizer and separator.
US1420665A (en) * 1920-05-10 1922-06-27 John W Newcombe Centrifugal dust separator
US2039127A (en) * 1933-08-23 1936-04-28 American Air Filter Co Rotary dust separator
US2209607A (en) * 1938-08-01 1940-07-30 American Air Filter Co Blade tip for rotary dust separators

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2780309A (en) * 1948-12-10 1957-02-05 Loftheim Tor Bjorn Devices for removing dust and other impurities from air, funnel smoke and other gases, especially gases from chemical and electrochemical manufactories
US2738855A (en) * 1953-04-28 1956-03-20 Fallon John Apparatus for separating dust from gases
US2944632A (en) * 1956-09-11 1960-07-12 Charles H Whitmore Centrifugal dust collector
US3292347A (en) * 1964-12-16 1966-12-20 Ametek Inc Dust and lint disposal apparatus
US3406504A (en) * 1966-12-13 1968-10-22 American Air Filter Co Combined gas moving and gas cleaning apparatus
US3516551A (en) * 1967-06-13 1970-06-23 Grubbens & Co Ab Cyclone separator
US3884656A (en) * 1974-06-28 1975-05-20 Clifford T Deane Recirculating air cleaner
US4095966A (en) * 1976-10-27 1978-06-20 Teledyne Industries, Inc. Air cleaner
US4285707A (en) * 1978-12-01 1981-08-25 Bbc Brown, Boveri & Company Limited Dust separator for separating dust from flowing gaseous media
US4685942A (en) * 1982-12-27 1987-08-11 General Electric Company Axial flow inlet particle separator

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