US2186804A - Nozzle - Google Patents

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Publication number
US2186804A
US2186804A US172753A US17275337A US2186804A US 2186804 A US2186804 A US 2186804A US 172753 A US172753 A US 172753A US 17275337 A US17275337 A US 17275337A US 2186804 A US2186804 A US 2186804A
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United States
Prior art keywords
swirl
spray
nozzle
plate
passages
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Expired - Lifetime
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US172753A
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Hamilton William Fownes
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WALTER R ALLEN
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WALTER R ALLEN
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B1/00Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
    • B05B1/34Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to influence the nature of flow of the liquid or other fluent material, e.g. to produce swirl
    • B05B1/3405Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to influence the nature of flow of the liquid or other fluent material, e.g. to produce swirl to produce swirl
    • B05B1/341Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to influence the nature of flow of the liquid or other fluent material, e.g. to produce swirl to produce swirl before discharging the liquid or other fluent material, e.g. in a swirl chamber upstream the spray outlet
    • B05B1/3421Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to influence the nature of flow of the liquid or other fluent material, e.g. to produce swirl to produce swirl before discharging the liquid or other fluent material, e.g. in a swirl chamber upstream the spray outlet with channels emerging substantially tangentially in the swirl chamber

Definitions

  • This invention relates to an atomizer of the mechanical atomization type; that is, one which is capable of converting a liquid into a fine mist without the aid of compressed gas.
  • a particular advantage of the invention is that it makes possible atomization with a flow con siderably below the minimumflow of mechanically atomizing nozzles in use at the present time.
  • the minimum flow available heretofore was approximately 2.5 gallons per hour, whereas nozzles have been made according to the principles of my invention which atomized liquids at the rate of 2 or 3 quarts per hour. It may be possible to achieve even slower rates of atomization with nozzles constructed according tomy invention, while higher rates can be handled equally well by simply enlarging the dimensions of the nozzle.
  • One application of the invention is in the atgo omization of oil, such as fuel oil, into sufficiently fine mist for smokeless combustion, for instance for orchard heating purposes.
  • oil such as fuel oil
  • the invention has the advantage of requiring only a moderate pressure to effect atomization.
  • the invention will be explained in detail with reference to several illustrative forms shown in the accompanying drawing.
  • the dimensions referred to in this description have been found satisfactory for a nozzle designed for a flow of about 2 or 3 quarts per hour; for different rates of flow the dimensions should be modified conformably.
  • FIG. l is an axial section of an atomizing nozzle in accordance with the invention, showing the same inserted in the end of a pipe which appears partly in elevation;
  • Fig. 2 is an axial section of the two nozzle plates of the atomizing nozzle shown in Fig. 1;
  • Fig. 3 is an elevational view of the central portion of the nozzle plates seen from the right in Fig. 2;
  • Fig. 4 is an elevation of the central portion of the spray plate, indicating the direction of the 45 jets from the swirl plate;
  • Fig. 5 is a view similar to Fig. 2 of a slightly modified form of the nozzle plate unit.
  • Fig. 6 is an elevation of the central portion of another modification of the nozzle plates.
  • the nozzle may be designed to screw into the end of a pipe 2 to which liquid 4 is supplied under pressure from a source not shown in the drawing.
  • the nozzle in this case comprises a threaded nipple 5 having an end 6 55 which screws into the pipe 2 and an end 8 onto which is screwed a cap III which holds the nozzle parts in place.
  • a spray plate l2 and a swirl plate M are held in a cup l6 by a washer l8, the assembly being pressed between the lip 20 of cap l0 and a sealing washer 22 which abuts against the end 8 of the nipple 5.
  • the spray plate and swirl plate shown in Fig. 1 appear in detail in Figs. 2, 3 and 4.
  • Each of these plates is in the form of a disk of sheet metal, for instance, of 0.015" brass.
  • each plate is bored part way through, for instance with a number 52 drill, to form the respective concavities 24 and 26.
  • the concavity 26 forms a swirl chamber, as will presently bedescribed.
  • the spray plate I2 is bored through at the apex of the concavity 24 to form the spray hole 28. For a nozzle to atomize 2 or 3 quarts per hour the size of the spray hole should be from 0.004 to 20 0.012" in diameter.
  • the edge of this spray hole should be of knife-edge sharpness for best results, since any substantial width' of surface will cause the issuing mist to coalesce and drip.
  • An exactly round spray hole gives a symmetrical 25 spray free from irregularities.
  • the small burr formed at the edge of the spray hole in the drilling may be polished off if desired.
  • the boring of the swirl plate l4 with the number 52 drill should be stopped about the time it bulges out 30 the metal at the point 30.
  • Swirl passages 32 are then drilled into the concavity 26, for a nozzle of this capacity with a drill having a diameter of "0.004" to 0.006".
  • the passages 32 should be directed, as indicated by dotted lines 34, so as to cause the jets issuing-from them to strike the edge of the spray hole. I have found that this direction of the jets gives the most perfect atomization with a minimum pressure; if the direction of the jets is changed so that they strike further from the edge of the spray hole the pressure required for atomization
  • the angle of the jets with reference to the central axis of the spray hole is preferably and 45 should not be less than 35 nor more than If the angle is less than 35 the swirling of the liquid in the swirl chamber 26 is not sufllciently violent to atomize the liquid, while if the angle is more than 55 the through velocity is decreased.
  • the 45 jets directed toward the edge of the spray orifice give the best results, probably because they combine high through velocity with vigorous swirling within the swirl chamber 26, causing good atomization.
  • the swirl pas- 55 sages I! are preferably directed tangentially to thesprayholainordertoproduceaswirlins motion of the liquid in the swirl chamber with a minimum of eddy currents.
  • the distance between the sprayhole and the plane of the swirl holes should be within the range of 0.008! to 0.040
  • Fig. 5 I have shown the simplest possible means of adjustment, in the form of a spacer ring of requisite thickness between the spray plate a and swirl plate I la. This figure also illustrates the possibility of directing the swirl holes its at an angle different from with reference to the axis of the spray hole, the angle inthiscasebelng". Inaccordancewiththe increased angle the swirl passages 32a are spaced further apart than in Fig. 2, so that the Jets a will be directed substantially toward the edge 01' the spray hole 28.
  • Fig. 6 shows a pair of nome plates, the swirl plate having eight swirl passages Ilb all directed tangentially to the spray hole It in the spray plate.
  • the larger number of swirl passages gives a more perfectly cone-shaped Jet from the spray hole and also provides a continuance of the spray in case of ppose of one or more swirl passages.
  • this nosale for atomizing fuel aieaeoa oilataveryslowratehasalreadybeenmmtioned.
  • the same characteristic is of importance whenusingthenossleasanatomiserof agricultural sprays.
  • the primary object is to produce a spray which will completely cover the surfaces to be sprayed with a minimum of waste.
  • a nossle capable of atomising the spray liquid at a slow rate is least wasteful.
  • a nozzle having forward and rearward walls enclosing a swirl chamber, the forward wall of said swirl chamber being traversed by a spray orifice defined by a knife edge, the rearward wall of said nozzle having swirl passages communicating with said swirl chamber behind said forward wall, said swirl passages being oppositely inclined toward opposed sides of said spray orifice, and means for conducting a liquid under pressure into the rear of said swirl passages.
  • a pair of plates means confining said plates so as to form between them a swirl chamber, one of said plates being traversed by a spray orifice defined by a knife edge, the other of said plates having at least two swirl passages therethrough located symmetrically with respect to the axis of said spray orifice and oppositely inclined toward opposed sides of said spray orifice, and means for conducting a liquid under pressure to said swirl passages.
  • a spray plate traversed by a spray orifice defined by a knife edge, and a swirl plate mounted closely parallel to said spray plate and having a concavity on its side facing said spray orifice, said swirl plate having swirl passages oppositely inclined toward opposed sides of said spray orifice, and means for conducting a liquid under pressure tosaid swirl passages.

Description

Jan. 9, 1940. w. F. HAMILTON NOZZLE Filed Nov. 4, 1937 INVENTOR I f TOES;
Patented Jan. 9, 1940 UNITED STATES NOZZLE William Fownes Hamilton, Altadena, Calif., aa-
signor of one-half to Walter R. Allen, Los
Angeles, Calif.
Application November 4, 1937, Serial No. 172,753
3 Claims.
This invention relates to an atomizer of the mechanical atomization type; that is, one which is capable of converting a liquid into a fine mist without the aid of compressed gas.
A particular advantage of the invention is that it makes possible atomization with a flow con siderably below the minimumflow of mechanically atomizing nozzles in use at the present time. The minimum flow available heretofore was approximately 2.5 gallons per hour, whereas nozzles have been made according to the principles of my invention which atomized liquids at the rate of 2 or 3 quarts per hour. It may be possible to achieve even slower rates of atomization with nozzles constructed according tomy invention, while higher rates can be handled equally well by simply enlarging the dimensions of the nozzle.
One application of the invention is in the atgo omization of oil, such as fuel oil, into sufficiently fine mist for smokeless combustion, for instance for orchard heating purposes.
The invention has the advantage of requiring only a moderate pressure to effect atomization. The invention will be explained in detail with reference to several illustrative forms shown in the accompanying drawing. The dimensions referred to in this description have been found satisfactory for a nozzle designed for a flow of about 2 or 3 quarts per hour; for different rates of flow the dimensions should be modified conformably.
In the drawing Fig. l is an axial section of an atomizing nozzle in accordance with the invention, showing the same inserted in the end of a pipe which appears partly in elevation;
Fig. 2 is an axial section of the two nozzle plates of the atomizing nozzle shown in Fig. 1;
Fig. 3 is an elevational view of the central portion of the nozzle plates seen from the right in Fig. 2;
Fig. 4 is an elevation of the central portion of the spray plate, indicating the direction of the 45 jets from the swirl plate;
Fig. 5 is a view similar to Fig. 2 of a slightly modified form of the nozzle plate unit; and
Fig. 6 is an elevation of the central portion of another modification of the nozzle plates.
As shown in Fig. 1, the nozzle may be designed to screw into the end of a pipe 2 to which liquid 4 is supplied under pressure from a source not shown in the drawing. The nozzle in this case comprises a threaded nipple 5 having an end 6 55 which screws into the pipe 2 and an end 8 onto which is screwed a cap III which holds the nozzle parts in place. A spray plate l2 and a swirl plate M are held in a cup l6 by a washer l8, the assembly being pressed between the lip 20 of cap l0 and a sealing washer 22 which abuts against the end 8 of the nipple 5.
The spray plate and swirl plate shown in Fig. 1 appear in detail in Figs. 2, 3 and 4. Each of these plates is in the form of a disk of sheet metal, for instance, of 0.015" brass. In the example shown each plate is bored part way through, for instance with a number 52 drill, to form the respective concavities 24 and 26. When the plates are placed together, as shown in Figs. 1 and 2, the concavity 26 forms a swirl chamber, as will presently bedescribed. The spray plate I2 is bored through at the apex of the concavity 24 to form the spray hole 28. For a nozzle to atomize 2 or 3 quarts per hour the size of the spray hole should be from 0.004 to 20 0.012" in diameter. The edge of this spray hole should be of knife-edge sharpness for best results, since any substantial width' of surface will cause the issuing mist to coalesce and drip. An exactly round spray hole gives a symmetrical 25 spray free from irregularities. The small burr formed at the edge of the spray hole in the drilling may be polished off if desired. The boring of the swirl plate l4 with the number 52 drill should be stopped about the time it bulges out 30 the metal at the point 30. Swirl passages 32 are then drilled into the concavity 26, for a nozzle of this capacity with a drill having a diameter of "0.004" to 0.006". The passages 32 should be directed, as indicated by dotted lines 34, so as to cause the jets issuing-from them to strike the edge of the spray hole. I have found that this direction of the jets gives the most perfect atomization with a minimum pressure; if the direction of the jets is changed so that they strike further from the edge of the spray hole the pressure required for atomization is increased.
Another important factor is the angle of the jets with reference to the central axis of the spray hole. This angle is preferably and 45 should not be less than 35 nor more than If the angle is less than 35 the swirling of the liquid in the swirl chamber 26 is not sufllciently violent to atomize the liquid, while if the angle is more than 55 the through velocity is decreased. The 45 jets directed toward the edge of the spray orifice give the best results, probably because they combine high through velocity with vigorous swirling within the swirl chamber 26, causing good atomization. The swirl pas- 55 sages I! are preferably directed tangentially to thesprayholainordertoproduceaswirlins motion of the liquid in the swirl chamber with a minimum of eddy currents.
l'branoasletoatomisefltoflquartsperhour the distance between the sprayhole and the plane of the swirl holes should be within the range of 0.008! to 0.040",
As previously stated, the direction of the Jets from the swirl passages I! toward the edgeof the spray hole is essential to the best atomization. Since it is not always possible in mass production methods to drill the passages II accurately, it is desirable to provide means for adjusting the spacing between the plates l2 and II. Any suitable means for this purpose may be ployed. In Fig. 5 I have shown the simplest possible means of adjustment, in the form of a spacer ring of requisite thickness between the spray plate a and swirl plate I la. This figure also illustrates the possibility of directing the swirl holes its at an angle different from with reference to the axis of the spray hole, the angle inthiscasebelng". Inaccordancewiththe increased angle the swirl passages 32a are spaced further apart than in Fig. 2, so that the Jets a will be directed substantially toward the edge 01' the spray hole 28.
It is advantageous to increase the number of swirl passages above two. Fig. 6 shows a pair of nome plates, the swirl plate having eight swirl passages Ilb all directed tangentially to the spray hole It in the spray plate. The larger number of swirl passages gives a more perfectly cone-shaped Jet from the spray hole and also provides a continuance of the spray in case of ppose of one or more swirl passages.
The usefulness of this nosale for atomizing fuel aieaeoa oilataveryslowratehasalreadybeenmmtioned. The same characteristic is of importance whenusingthenossleasanatomiserof agricultural sprays. In this work the primary object is to produce a spray which will completely cover the surfaces to be sprayed with a minimum of waste. A nossle capable of atomising the spray liquid at a slow rate is least wasteful.
I claim:
1. In an atomizer, a nozzle having forward and rearward walls enclosing a swirl chamber, the forward wall of said swirl chamber being traversed by a spray orifice defined by a knife edge, the rearward wall of said nozzle having swirl passages communicating with said swirl chamber behind said forward wall, said swirl passages being oppositely inclined toward opposed sides of said spray orifice, and means for conducting a liquid under pressure into the rear of said swirl passages.
2. In an atomizer, a pair of plates, means confining said plates so as to form between them a swirl chamber, one of said plates being traversed by a spray orifice defined by a knife edge, the other of said plates having at least two swirl passages therethrough located symmetrically with respect to the axis of said spray orifice and oppositely inclined toward opposed sides of said spray orifice, and means for conducting a liquid under pressure to said swirl passages.
3. In an atomizer, a spray plate traversed by a spray orifice defined by a knife edge, and a swirl plate mounted closely parallel to said spray plate and having a concavity on its side facing said spray orifice, said swirl plate having swirl passages oppositely inclined toward opposed sides of said spray orifice, and means for conducting a liquid under pressure tosaid swirl passages.
WILLIAM FOWNES HAMILTON.
US172753A 1937-11-04 1937-11-04 Nozzle Expired - Lifetime US2186804A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2480459A (en) * 1944-12-08 1949-08-30 Babcock & Wilcox Co Fuel burning apparatus wherein air is supplied in one or more streams of elongated cross section
US3012760A (en) * 1957-03-01 1961-12-12 Carrier Corp Air conditioning units
EP0155971A1 (en) * 1983-12-01 1985-10-02 Ernst Bröker Shower head
FR2838069A1 (en) * 2002-04-08 2003-10-10 Saint Gobain Ceramiques Avance SPRAY NOZZLE
US20100116909A1 (en) * 2006-08-01 2010-05-13 Hassan Abduljalil Nozzle and dispenser incorporating a nozzle

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2480459A (en) * 1944-12-08 1949-08-30 Babcock & Wilcox Co Fuel burning apparatus wherein air is supplied in one or more streams of elongated cross section
US3012760A (en) * 1957-03-01 1961-12-12 Carrier Corp Air conditioning units
EP0155971A1 (en) * 1983-12-01 1985-10-02 Ernst Bröker Shower head
FR2838069A1 (en) * 2002-04-08 2003-10-10 Saint Gobain Ceramiques Avance SPRAY NOZZLE
WO2003084669A1 (en) * 2002-04-08 2003-10-16 Saint Gobain Ceramiques Avancees Desmarquest Spray nozzle
US20050224602A1 (en) * 2002-04-08 2005-10-13 Saint Gobain Ceramiques Avancees Desmarquest Spray nozzle
US7243861B2 (en) 2002-04-08 2007-07-17 Saint Gobain Ceramiques Avancees Desmarquest Spray nozzle
US20100116909A1 (en) * 2006-08-01 2010-05-13 Hassan Abduljalil Nozzle and dispenser incorporating a nozzle

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