US3566833A - Continuous coating apparatus - Google Patents
- ️Tue Mar 02 1971
US3566833A - Continuous coating apparatus - Google Patents
Continuous coating apparatus Download PDFInfo
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Publication number
- US3566833A US3566833A US3566833DA US3566833A US 3566833 A US3566833 A US 3566833A US 3566833D A US3566833D A US 3566833DA US 3566833 A US3566833 A US 3566833A Authority
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- United States Prior art keywords
- chamber
- wire
- coating
- powder
- cloud Prior art date
- 1968-06-28 Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 238000000576 coating method Methods 0.000 title description 44
- 239000011248 coating agent Substances 0.000 title description 43
- 239000007921 spray Substances 0.000 claims abstract description 29
- 239000002245 particle Substances 0.000 claims abstract description 27
- 239000000843 powder Substances 0.000 abstract description 24
- 239000004033 plastic Substances 0.000 abstract description 10
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 abstract description 6
- 239000004593 Epoxy Substances 0.000 abstract description 3
- 238000009413 insulation Methods 0.000 abstract description 3
- 239000012530 fluid Substances 0.000 description 13
- 239000000463 material Substances 0.000 description 9
- 239000000758 substrate Substances 0.000 description 5
- 238000007610 electrostatic coating method Methods 0.000 description 4
- 239000006223 plastic coating Substances 0.000 description 4
- 238000009503 electrostatic coating Methods 0.000 description 3
- 230000003014 reinforcing effect Effects 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- 241000512668 Eunectes Species 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 210000003813 thumb Anatomy 0.000 description 2
- 230000001464 adherent effect Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 210000003298 dental enamel Anatomy 0.000 description 1
- 238000003618 dip coating Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000004070 electrodeposition Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000007665 sagging Methods 0.000 description 1
- 238000005029 sieve analysis Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
- B05D7/20—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to wires
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D1/00—Processes for applying liquids or other fluent materials
- B05D1/02—Processes for applying liquids or other fluent materials performed by spraying
- B05D1/04—Processes for applying liquids or other fluent materials performed by spraying involving the use of an electrostatic field
- B05D1/06—Applying particulate materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D1/00—Processes for applying liquids or other fluent materials
- B05D1/18—Processes for applying liquids or other fluent materials performed by dipping
- B05D1/22—Processes for applying liquids or other fluent materials performed by dipping using fluidised-bed technique
- B05D1/24—Applying particulate materials
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B13/00—Apparatus or processes specially adapted for manufacturing conductors or cables
- H01B13/0033—Apparatus or processes specially adapted for manufacturing conductors or cables by electrostatic coating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D1/00—Processes for applying liquids or other fluent materials
- B05D1/007—Processes for applying liquids or other fluent materials using an electrostatic field
Definitions
- Electrostatic coating has been widely used to provide a coating of plastic on a substrate using apparatuses such as those described in U.S. Pat. No. 2,893,893, and U.S. Pat. No. 2,893,894 to Crouse and to Ransburg, respectively. These apparatuses electrostatically atomize finely divided discrete particles of liquid as a spray and electrostatically disperse and deposit the particles on the substrate while still in a liquid state.
- plastic in the form of finely divided solid particles has also been successfully electrostatically coated on a substrate by dipping the substrate into a-fluidized bed of charged and finely divided plastic powder.
- An example of the solid electrostatic coating method is described in U.S. Pat. No. 3,019,126 to Bartholomew. Electrostatic coating methods described above, however, cannot be controlled readily for coating a very thin and even deposition of plastic on a substrate such as that required in the manufacturing of magnet wires.
- a modified fluid bed electrostatic coating method which uses a DC high voltage supply to create a potential within the chamber sufficient to create a cloud of charged particles above the fluid bed of charged plastic powder and to deposit the powder evenly on the wire passing through the charged cloud.
- This method and the apparatus for practicing the same are described in U.S. Pat. application Ser. No. 588,511, filed on Oct. 2!, 1966, now U.S. Pat. No. 3,396,699, and assigned to Anaconda Wire and Cable Company, the assignee 'of this application.
- Magnet wires manufactured by this modified fluid bed electrostatic coating method are acceptable for commercial application.
- the insulation thereon lacks the smoothness when compared with magnet wires prepared by the more conventional dip-coating method using an enamel solution.
- the apparatus comprises an enclosed chamber having an inlet and an outlet for the metallic member such as a wire to pass therethrough.
- an electrostatic spray gun which has at least one spray nozzle positioned within the chamber and spaced apart from but adjacent to the metallic member passing through the chamber.
- the spray gun is connected to a DC high voltage supply source for generating a high electrical potential within the chamber and is also connected to a source of plastic coating material.
- the spray gun has pressure means for delivering the plastic coating material to the nozzle and for projecting the material into the chamber in the form of finely divided charged particles.
- the apparatus has means for continuously feeding the metallic member into the chamber through its inlet and withdrawing the metallic member therefrom through the outlet at a predetermined rate. While passing through the enclosed chamber, the metallic member is surrounded by the cloud of the electrostatically charged particles created by the high electrical potential generated by the spray gun or in combination with the electrodes.
- the metallic member is advantageously grounded to create a potential difference between the charged particles and the metallic member to cause the finely divided and charged coating particles to deposit evenly thereon.
- FIG. 1 is a side view, partly in section, of the apparatus of this invention.
- FIG. 2 is a cross-sectional view of the coating chamber
- FIG. 3 is a partial cross section taken along line 33 of FIG. 2.
- the continuous coating apparatus 10 of this invention as shown in FIG. 1 comprises an enclosed coating chamber 11 and an oven 12.
- the coating chamber 11 is generally in the form of a rectangular box having an upstream wall 13 and a downstream wall 14 as shown more clearly in FIG. 2.
- a wire inlet 15 in the form of a tube is provided on the upstream wall 13.
- the tubular wire inlet 15 is slidably mounted on a bushing 16 which in turn is bolted to the upstream wall 13 by a reinforcing plate 17.
- the tubular wire inlet l5 can be locked into place by a thumb screw 18.
- the outlet I9 is also in the form of a tube with a slightly larger diameter than the inlet about 5 to l0 times the diameter or the maximum width of the member and is slidably mounted on a bushing 20 bolted to the downstream wall 14 by a reinforcing plate 21. It is also locked into place by a thumb screw 22.
- the hollow ring 23 is connected to an air supply (not shown) by an air hose 25. The function of the hollow ring and the inwardly directed jets will be described in more detail hereinbelow.
- an electrostatic spray gun 26 Secured to one of the sidewalls 28 of the coating chamber ii] is an electrostatic spray gun 26 whose spray nozzle protrudes into the coating chamber llI as shown more clearly in FIG. 3. Similar to the inlet and outlet tubes, the spray gun is advantageously slidably mounted on a bushing 27 which, in turn, is bolted to the sidewall 28 by a reinforcing plate 29. Connected to the spray gun are an airand powdered-coatingmaterial-supply line 30 and an electrical wire 3i connected to a high DC voltage source (not shown). A number of electrostatic spray guns available commercially are suitable for the apparatus of this invention.
- These guns are capable of spraying finely divided particles, such as plastic powder, by initially mixing the powder with a gas, such as air, and then delivering the powder and air mixture to the spray nozzle.
- a gas such as air
- One of such electrostatic spray guns that we found to be eminently suitable is Ransburg Electropowder Gun REP Model 322AB, manufactured by Ransburg Electro-Coating Corp.
- the coating chamber 11 has a gas permeable false bottom 32 formed of a sheet of porous ceramic, and an impermeable plate 33 spaced apart from the false bottom 32 to form a gas passage 34 into which dried air is blown through a pipe 35 connected to a pressurized air supply (not shown).
- a fluid bed 36 of dielectric powder coating material which may be similar to the coating material from the spray gun 26 and is maintained in the fluidized state by the air through the porous bottom 32.
- Embedded in the plate 32 are a large number of electrodes 37 which are evenly distributed and spaced apart over the entire upper surface of the plate 32.
- the electrodes 37 are all electrically connected to a high voltage generator 61 (see FIG.
- an air outlet 60 is provided thereon to release the pressure buildup caused by the air admitted into the chamber from the spray gun and from the fluid bed.
- the air outlet 60 is preferably positioned at or adjacent to the top above the charged cloud 59 to avoid the removal of an excess amount of charged powder. A certain amount of powder will escape through the air outlet 60 which may be recovered by a filter connected to the air outlet. The recovered powder may be recycled to the coating material supply for reintroduction into the chamber.
- the elongated metallic member 39 which when used for the preparation of magnet wires may be a copper wire, is paid off from a supply reel 40 over a supporting sheave 41 through the inlet tube and into the coating chamber 11.
- a felt plug 42 which allows the wire 39 to pass therethrough but seals the tube to avoid the leakage of the coating powder.
- the copper wire 39 exits the coating chamber 11 through the outlet tube 19 which is aligned with the inlet tube 15 and into the oven 12 through inlet 43.
- a bank of heating elements 44 and 45 which may be infrared lamps, the coated copper wire exits through an oven outlet 46, over a supporting sheave 47 onto a takeup reel 48 which is driven by a motor 49.
- the chamber 11 is mounted on rubber or other flexible footing 50 and is vibrated by a vibrator 51 which can be of a number of known types such as air or electric vibrators.
- the speed and amplitude of the vibrators 51 are preferably variable and are set to establish optimum conditions for a fluid bed which are determined by trial.
- the infrared lamps 44 and 45 should be sufficient in number to provide a temperature high enough to thoroughly fuse the coating on the wire.
- the sheave 47 should be spaced downstream of the oven 12 at a distance long enough to allow the coating to cool to a substantially nontacky state before passing thereover.
- a fluid bed is used to assist the electrostatic spray gun to create a charged cloud for electrostatic coating, it should be understood that such a fluid bed is not essential for the success of the coating operation.
- the electrodes 37 to control the charged cloud.
- a DC voltage applied to the electrodes 37 should be higher than the voltage applied to the spray gun.
- the coating thickness of the magnet wire is controlled by a number of variables which include the amount of powder sprayed into the chamber, the magnitude of the potential applied to the spray gun and on the electrodes 37 and the air velocity through the porous plate 32 which affect the density of the cloud 52, the speed of the wire 39, and the relative positions of tubes 15 and 19.
- the speed of the wire 39 in commercial practice should be maintained as high as the oven 12 can satisfactorily fuse the resultant coated wire.
- the voltages of the electrodes and of the spray gun have a definite upper limit determined by the capacity of the high voltage generator and the danger of arcing between the electrodes and the wire, and a lower limit below which the cloud 52 will be irregular and will not completely surround the wire.
- the wire 39 may be fed at a speed from 10 to 50 feet per minute to apply a coating 0.0005 to .0025 inches thick. This speed is many times faster than the speed used for coating by wet methods with multiple passes. To achieve this speed the oven 12 is preferably about 9 feet long. Since the oven uses infrared energy sources (the lamps 44 and 45) the actual air temperature in the oven is not the important factor in fusing the coating.
- the fluid bed is maintained between about 25 inches deep and the wire 39 is passed 15 to 18 inches above the porous plate 32 and the spray gun is positioned below the wire and about 6 to 10 inches away from the wire.
- the volume of the fluid bed should not be much greater, possibly 20 percent, than the volume 00' cupied by the powder in an unfluidized condition.
- the electrodes 37 and applied voltage would be used for the purpose of generating the cloud 59 from the spray gun.
- the length of wire exposed to the cloud 59 can be from 6 inches to about 2 feet.
- the applied potential on the electrodes 37 was kilovolts and on the spray gun was 50 kilovolts.
- the wire 39 and oven 12 and all external parts of the chamber 11 were grounded.
- the epoxy powder used has particle size distribution determined by sieve analysis as follows:
- An apparatus for coating an insulating film on a continuously travelling elongated metallicmember which apparatus comprises:
- an electrostatic gun having at least one spray nozzle positioned within the chamber and spaced apart from but adjacent to the metallic member passing through the chamber, said spray gun being connected to a source of plastic coating material and having pressure means for delivering the plastic coating material to the nozzle and projecting said material into the chamber in the form of finely divided particles and being connected to a high voltage supply source to create a high electrical potential within said chamber and to electrostatically charge the finely divided coating particles thereby creating a dense cloud of said charged particles within the chamber; means for forming and maintaining a fluidized bed of finely divided coating particles within the coating chamber and wherein electrodes are provided and are connected to a high voltage supply source to create a high electrical potential within the chamber and to electrostatically charge the finely divided coating particles;
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- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Manufacturing & Machinery (AREA)
- Electrostatic Spraying Apparatus (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
Abstract
A magnet wire is prepared by first passing a copper wire through a dense cloud of electrostatically charged and finely divided plastic particles such as epoxy powder held within a confined chamber and being created by a spray gun positioned within the chamber and below the elongated member and in combination with a fluidized bed of a similar or a different plastic powder and then passing the electrostatically coated wire through an oven maintained at a temperature sufficiently high to fuse the electrostatically deposited plastic particles thereon to form an insulation film on the wire.
Description
United States Patent [72] Inventors Norman Percy Beebe Ferrysburg; Bruce Aubert Madeley, Manistee, Mich. 121 1 Appl. No. 741,093 [22] Filed June 28, 1968 [45] Patented Mar. 2, 1971 [73] Assignee Anaconda Wire and Cable Company New York, N.Y.
[54]
CONTINUOUS COATING APPARATUS3 Claims, 3 Drawing Figs.
[52 I US. Cl 118/634, 1 18/304, 118/405 [51 Int. Cl B05b 5/00 [50] Field of Search 118/637, 1 623, 624, 629, 630, 634; l l7/(1nquired), 17, 17.5, 16+
[56] References Cited UNITED STATES PATENTS 2,711,481 6/1955 Phillips 118/637X 2,817,765 12/1957 Hayford et a1. (118/637UX) l layford 2,859,129 11/1958 118/637X 2,862,472 12/1958 Carlson ....(l 17/bud digest) 2,914,221 1 H1959 Rosenthal l l8/637X 2,111,853 3/1938 Fourness et al.. 118/405X 3,248,253 4/1966 Barford et al.... l l8/630X 3,336,903 8/1967 Point 1 18/624 FOREIGN PATENTS 993,566 5/ 1965 Great Britain Primary Examiner-Morris Kaplan Attorney-Pennie, Edmonds, Morton, Taylor and Adams 21
l42 I6 I I f g (I i W a 5 .1
' l'l'l-lf j -j f 52.
PATENIED "AR 2 I97! H/I4 I 7438, I
AIR POWDER FIG. 3
INVENTORS NORMAN P' BEEBE BRUCE A. MADELEY BY $2.: 104 Hi4. V1.3.
ATTORNEYS CONTINUOUS COATING APPARATUS BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to an apparatus for continuously coating elongated metallic members and more specifically to the manufacturing of magnet wires.
2. Description of the Prior Art Electrostatic coating has been widely used to provide a coating of plastic on a substrate using apparatuses such as those described in U.S. Pat. No. 2,893,893, and U.S. Pat. No. 2,893,894 to Crouse and to Ransburg, respectively. These apparatuses electrostatically atomize finely divided discrete particles of liquid as a spray and electrostatically disperse and deposit the particles on the substrate while still in a liquid state. Alternatively, plastic in the form of finely divided solid particles has also been successfully electrostatically coated on a substrate by dipping the substrate into a-fluidized bed of charged and finely divided plastic powder. An example of the solid electrostatic coating method is described in U.S. Pat. No. 3,019,126 to Bartholomew. Electrostatic coating methods described above, however, cannot be controlled readily for coating a very thin and even deposition of plastic on a substrate such as that required in the manufacturing of magnet wires.
To improve the deposition, a modified fluid bed electrostatic coating method has been recently developed which uses a DC high voltage supply to create a potential within the chamber sufficient to create a cloud of charged particles above the fluid bed of charged plastic powder and to deposit the powder evenly on the wire passing through the charged cloud. This method and the apparatus for practicing the same are described in U.S. Pat. application Ser. No. 588,511, filed on Oct. 2!, 1966, now U.S. Pat. No. 3,396,699, and assigned to Anaconda Wire and Cable Company, the assignee 'of this application. Magnet wires manufactured by this modified fluid bed electrostatic coating method are acceptable for commercial application. The insulation thereon, however, lacks the smoothness when compared with magnet wires prepared by the more conventional dip-coating method using an enamel solution.
SUMMARY OF THE INVENTION We have discovered quite unexpectedly that the smoothness of the insulation on the magnet wire can be substantially improved by using an electrostatic spray gun either alone or in combination with a fluid bed to generate an electrostatic cloud of a plastic powder in a modified electrostatic coating apparatus similar to the aforesaid copending application. Broadly stated, the apparatus comprises an enclosed chamber having an inlet and an outlet for the metallic member such as a wire to pass therethrough. Associated with the coating chamber, is an electrostatic spray gun which has at least one spray nozzle positioned within the chamber and spaced apart from but adjacent to the metallic member passing through the chamber. The spray gun is connected to a DC high voltage supply source for generating a high electrical potential within the chamber and is also connected to a source of plastic coating material. The spray gun has pressure means for delivering the plastic coating material to the nozzle and for projecting the material into the chamber in the form of finely divided charged particles.
Preferably, there is a plurality of electrodes which are positioned within the chamber and are also connected to a DC high voltage supply source for generating a high electrical potential within the chamber. The apparatus has means for continuously feeding the metallic member into the chamber through its inlet and withdrawing the metallic member therefrom through the outlet at a predetermined rate. While passing through the enclosed chamber, the metallic member is surrounded by the cloud of the electrostatically charged particles created by the high electrical potential generated by the spray gun or in combination with the electrodes. The metallic member is advantageously grounded to create a potential difference between the charged particles and the metallic member to cause the finely divided and charged coating particles to deposit evenly thereon.
An oven which also has an inlet and an outlet is positioned 1 BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a side view, partly in section, of the apparatus of this invention;
FIG. 2 is a cross-sectional view of the coating chamber; and
FIG. 3 is a partial cross section taken along
line33 of FIG. 2.
DESCRIPTION OF THE PREFERRED EMBODIMENTS The continuous coating apparatus 10 of this invention as shown in FIG. 1 comprises an enclosed
coating chamber11 and an
oven12. The
coating chamber11 is generally in the form of a rectangular box having an
upstream wall13 and a
downstream wall14 as shown more clearly in FIG. 2. A
wire inlet15 in the form of a tube is provided on the
upstream wall13. The
tubular wire inlet15 is slidably mounted on a bushing 16 which in turn is bolted to the
upstream wall13 by a reinforcing
plate17. The tubular wire inlet l5 can be locked into place by a
thumb screw18.
Similar to the
wire inlet15, the outlet I9 is also in the form of a tube with a slightly larger diameter than the inlet about 5 to l0 times the diameter or the maximum width of the member and is slidably mounted on a bushing 20 bolted to the
downstream wall14 by a reinforcing
plate21. It is also locked into place by a
thumb screw22. Mounted on the downstream of the
wire outlet19, there is a
hollow ring23 with a plurality of
jet nozzles24 directed inwardly into the tube. The
hollow ring23 is connected to an air supply (not shown) by an
air hose25. The function of the hollow ring and the inwardly directed jets will be described in more detail hereinbelow.
Secured to one of the
sidewalls28 of the coating chamber ii] is an
electrostatic spray gun26 whose spray nozzle protrudes into the coating chamber llI as shown more clearly in FIG. 3. Similar to the inlet and outlet tubes, the spray gun is advantageously slidably mounted on a bushing 27 which, in turn, is bolted to the
sidewall28 by a reinforcing
plate29. Connected to the spray gun are an airand powdered-coatingmaterial-
supply line30 and an electrical wire 3i connected to a high DC voltage source (not shown). A number of electrostatic spray guns available commercially are suitable for the apparatus of this invention. These guns are capable of spraying finely divided particles, such as plastic powder, by initially mixing the powder with a gas, such as air, and then delivering the powder and air mixture to the spray nozzle. One of such electrostatic spray guns that we found to be eminently suitable is Ransburg Electropowder Gun REP Model 322AB, manufactured by Ransburg Electro-Coating Corp.
As shown in FIG. 2 the
coating chamber11 has a gas permeable false bottom 32 formed of a sheet of porous ceramic, and an
impermeable plate33 spaced apart from the false bottom 32 to form a
gas passage34 into which dried air is blown through a
pipe35 connected to a pressurized air supply (not shown). Above the porous plate 32 is a
fluid bed36 of dielectric powder coating material which may be similar to the coating material from the
spray gun26 and is maintained in the fluidized state by the air through the porous bottom 32. Embedded in the plate 32 are a large number of
electrodes37 which are evenly distributed and spaced apart over the entire upper surface of the plate 32. The
electrodes37 are all electrically connected to a high voltage generator 61 (see FIG. 1) which supplies a high negative DC voltage to the electrodes in the order to 40-100 kilovolts. The application of the high electrical potential causes the formation of a dense charged cloud of the dielectric powder from the electrostatic spray gun and from the fluid bed which is above the fluidized bed and is sufficiently high to surround the wire coming into the chamber through the
inlet tube15. The charged cloud is prevented from escaping from the coating chamber by a
cover38.
Since the coating chamber is enclosed by the
cover38, an
air outlet60 is provided thereon to release the pressure buildup caused by the air admitted into the chamber from the spray gun and from the fluid bed. The
air outlet60 is preferably positioned at or adjacent to the top above the charged
cloud59 to avoid the removal of an excess amount of charged powder. A certain amount of powder will escape through the
air outlet60 which may be recovered by a filter connected to the air outlet. The recovered powder may be recycled to the coating material supply for reintroduction into the chamber.
The elongated
metallic member39, which when used for the preparation of magnet wires may be a copper wire, is paid off from a supply reel 40 over a supporting
sheave41 through the inlet tube and into the
coating chamber11. At the downstream of the
inlet tube15 there is a felt
plug42 which allows the
wire39 to pass therethrough but seals the tube to avoid the leakage of the coating powder. The
copper wire39 exits the
coating chamber11 through the
outlet tube19 which is aligned with the
inlet tube15 and into the
oven12 through
inlet43. After passing through a bank of
heating elements44 and 45 which may be infrared lamps, the coated copper wire exits through an
oven outlet46, over a supporting
sheave47 onto a
takeup reel48 which is driven by a
motor49.
Once the wire enters into the coating chamber it is free from any contact until it leaves the
oven12. It is, therefore, apparent that inlets and outlets of the oven and the coating chamber must be properly aligned and that the sagging of the wire is controlled by adjusting the tension between the two
sheaves41 and 47.
Since the coating chamber is enclosed, particles that collect on the
top plate38 may fall on the wire causing loosely deposited particles thereon. These loosely held particles are removed by the
jets24 directed inwardly into the
chamber11.
The
chamber11 is mounted on rubber or other
flexible footing50 and is vibrated by a
vibrator51 which can be of a number of known types such as air or electric vibrators. The speed and amplitude of the
vibrators51 are preferably variable and are set to establish optimum conditions for a fluid bed which are determined by trial.
The
infrared lamps44 and 45 should be sufficient in number to provide a temperature high enough to thoroughly fuse the coating on the wire. The
sheave47 should be spaced downstream of the
oven12 at a distance long enough to allow the coating to cool to a substantially nontacky state before passing thereover.
Although in the apparatus just described a fluid bed is used to assist the electrostatic spray gun to create a charged cloud for electrostatic coating, it should be understood that such a fluid bed is not essential for the success of the coating operation. When the fluid bed is not used we prefer to use the
electrodes37 to control the charged cloud. In general we found a DC voltage applied to the
electrodes37 should be higher than the voltage applied to the spray gun. The coating thickness of the magnet wire is controlled by a number of variables which include the amount of powder sprayed into the chamber, the magnitude of the potential applied to the spray gun and on the
electrodes37 and the air velocity through the porous plate 32 which affect the density of the cloud 52, the speed of the
wire39, and the relative positions of
tubes15 and 19. The speed of the
wire39 in commercial practice should be maintained as high as the
oven12 can satisfactorily fuse the resultant coated wire. The voltages of the electrodes and of the spray gun have a definite upper limit determined by the capacity of the high voltage generator and the danger of arcing between the electrodes and the wire, and a lower limit below which the cloud 52 will be irregular and will not completely surround the wire.
The proper conditions for obtaining the most effective cloud should be experimentally determined for each type of powder to be applied. However, we have found that a most delicate control of the effective length of the
chamber11 is obtainable by means of the
tubes15 and 19 which can be separated or brought together to determine the length of the
wire39 exposed to the cloud 52. This exposure could be controlled by adjusting only one of the
tubes15 and 19 but we have found that when both tubes are adjustable it is possible to select an optimum portion of the cloud formation for exposure of the
wire39. The tubes allow much higher voltages resulting in higher cloud densities which permit the application of denser coatings.
We have found also that although the powder deposit on the
wire39 which is, at least temporarily, adherent due to the electrostatic charge, is uniformly distributed on the wire, there are, in addition, loose particles, such as agglomerates which may fall from the wall or cover, which if they are permitted to remain on the wire, would fuse into an uneven, lumpy coating in the
oven12. An air current generally will remove these excess particles and lumps, and still will not disturb the desired coating layer. By placing the
air ring23 at the downstream end of the
tube19, it serves the triple purposes of removing the loose aggregate, of freeing the
tube19 from any deposits of powder, and of controlling the cloud of charged particles.
When a continuous wire is passed through the cloud 52 access to the top of the wire is available only from the sides, not from the back and front as when an individual article is dipped into the cloud. Yet we have found that flat wires held in a horizontal plane can be satisfactorily coated in our apparatus, and we have coated thousands of pounds of copper wire .065 to .31 inches with an epoxy powder.
The
wire39 may be fed at a speed from 10 to 50 feet per minute to apply a coating 0.0005 to .0025 inches thick. This speed is many times faster than the speed used for coating by wet methods with multiple passes. To achieve this speed the
oven12 is preferably about 9 feet long. Since the oven uses infrared energy sources (the
lamps44 and 45) the actual air temperature in the oven is not the important factor in fusing the coating.
In the preferred operating conditions, the fluid bed is maintained between about 25 inches deep and the
wire39 is passed 15 to 18 inches above the porous plate 32 and the spray gun is positioned below the wire and about 6 to 10 inches away from the wire. The volume of the fluid bed should not be much greater, possibly 20 percent, than the volume 00' cupied by the powder in an unfluidized condition. In the absence of fluidization, the
electrodes37 and applied voltage would be used for the purpose of generating the
cloud59 from the spray gun. The length of wire exposed to the
cloud59 can be from 6 inches to about 2 feet.
In the application of epoxy resin to copper wire hereinabove described to provide a coating thickness of 0.00l50.00l8 inches in one pass, the applied potential on the
electrodes37 was kilovolts and on the spray gun was 50 kilovolts. The
wire39 and
oven12 and all external parts of the
chamber11 were grounded.
The epoxy powder used has particle size distribution determined by sieve analysis as follows:
Perccnt on Mesh size: screen l 1.9 17.4 200 [9.0 230 19.0 270 20.7 325 8.9 Through 325 3.1
Testing this powder using a standard test for comparison shows that the powder will fuse and flow out adhering to a wire in 31 seconds at 230 C In practice, a higher temperature may be used leading to a shorter duration for fusing. We found a temperature in the range between 300350 C. to be particularly suitable. At this high temperature range the fusing period is shortened to about to 12 seconds.
We claim:
ll. An apparatus for coating an insulating film on a continuously travelling elongated metallicmember which apparatus comprises:
an enclosed chamber having an inlet and an outlet for said metallic member to pass therethrough;
an electrostatic gun having at least one spray nozzle positioned within the chamber and spaced apart from but adjacent to the metallic member passing through the chamber, said spray gun being connected to a source of plastic coating material and having pressure means for delivering the plastic coating material to the nozzle and projecting said material into the chamber in the form of finely divided particles and being connected to a high voltage supply source to create a high electrical potential within said chamber and to electrostatically charge the finely divided coating particles thereby creating a dense cloud of said charged particles within the chamber; means for forming and maintaining a fluidized bed of finely divided coating particles within the coating chamber and wherein electrodes are provided and are connected to a high voltage supply source to create a high electrical potential within the chamber and to electrostatically charge the finely divided coating particles;
means for continuously feeding the-metallic member into the chamber through its inlet and withdrawing the metallic member therefrom through the outlet at a predetermined rate and passing through said cloud fluidized bed;
means for grounding the metallic member to create a potential difference between the charged particles and the metallic member while it passes through the chamber thereby causing the finely-divided and charged coating particles to deposit evenly thereon; an oven positioned next to the chamber and having an inlet and an outlet for receiving the coated metallic member from the chamber, said oven being maintained at a temperature sufficient to cause the fusing of the coating on the metallic member to fotm said insulating film; and
means for continuously feeding and withdrawing the coated metallic member through the oven at a predetermined rate sufficient to allow the coating to fuse into the said insulating film. I
2. An apparatus according to claim 1 wherein the spray nozzle is positioned just below the metallic member.
3. An apparatus according to claim 2 wherein the inlet and the outlet of the chamber each is in the form of an elongated tube slidably mounted on the wall of the chamber and protruding thereinto, said tubes being adjustable to increase or to decrease the exposure of the metallic member within the chamber thereby controlling the thickness of the charged particles deposited on the metallic member.
Claims (2)
-
2. An apparatus according to claim 1 wherein the spray nozzle is positioned just below the metallic member.
-
3. An apparatus according to claim 2 wherein the inlet and the outlet of the chamber each is in the form of an elongated tube slidably mounted on the wall of the chamber and protruding thereinto, said tubes being adjustable to increase or to decrease the exposure of the metallic member within the chamber thereby controlling the thickness of the charged particles deposited on the metallic member.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US74109368A | 1968-06-28 | 1968-06-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3566833A true US3566833A (en) | 1971-03-02 |
Family
ID=24979368
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US3566833D Expired - Lifetime US3566833A (en) | 1968-06-28 | 1968-06-28 | Continuous coating apparatus |
Country Status (1)
Country | Link |
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US (1) | US3566833A (en) |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3853581A (en) * | 1972-06-02 | 1974-12-10 | Air Ind | Method of coating articles with electrostatically charged particles |
FR2310619A1 (en) * | 1975-05-05 | 1976-12-03 | Northern Telecom Ltd | METHOD FOR MANUFACTURING A THERMALLY INSULATED AND POLYMER-COATED ELECTRICAL CONDUCTOR AND CONDUCTOR SO OBTAINED |
US4008685A (en) * | 1976-04-20 | 1977-02-22 | Westinghouse Electric Corporation | Electrostatic fluidized bed build control |
US4011832A (en) * | 1975-02-26 | 1977-03-15 | Westinghouse Electric Corporation | Build control for fluidized bed wire coating |
US4035521A (en) * | 1975-02-26 | 1977-07-12 | Westinghouse Electric Corporation | Build control for fluidized bed wire coating |
US4051809A (en) * | 1976-09-22 | 1977-10-04 | Westinghouse Electric Corporation | Apparatus for cleaning and coating an elongated metallic member |
US4069792A (en) * | 1976-02-26 | 1978-01-24 | Canada Wire And Cable Limited | Electrostatic fluidized bed coating unit |
US4084019A (en) * | 1976-02-05 | 1978-04-11 | Armco Steel Corporation | Electrostatic coating grid and method |
US4100883A (en) * | 1976-10-18 | 1978-07-18 | General Electric Company | Apparatus for electrostatic deposition on a running conductor |
EP0007634A1 (en) * | 1978-07-31 | 1980-02-06 | Northern Telecom Limited | Apparatus and method for use in fluidized powder filling of multiple core unit cables |
EP0023238A1 (en) * | 1979-07-30 | 1981-02-04 | Philips Kommunikations Industrie AG | Method and device for manufacturing varnish-insulated winding wire, in particular thick wires |
US4271783A (en) * | 1978-01-20 | 1981-06-09 | General Electric Company | Apparatus for fluidized bed-electrostatic coating of indefinite length substrate |
EP0110542A1 (en) * | 1982-10-28 | 1984-06-13 | Florida Wire And Cable Company | Concrete strengthening members, particularly prestressing tendons, having improved corrosion resistance and/or bonding characteristics, and methods relating thereto |
US4606928A (en) * | 1985-03-07 | 1986-08-19 | Electrostatic Technology Incorporated | Vortex effect electrostatic fluidized bed coating method and apparatus |
US4808432A (en) * | 1986-08-18 | 1989-02-28 | Electrostatic Technology Incorporated | Electrostatic coating apparatus and method |
US6200678B1 (en) * | 1986-02-19 | 2001-03-13 | Florida Wire & Cable, Inc. | Corrosion resistant coated metal strand |
JP2014008486A (en) * | 2012-07-02 | 2014-01-20 | Kawanetsu Co Ltd | Method for manufacturing polyethylene terephthalate resin-coated metal filament |
US11260419B2 (en) * | 2018-03-02 | 2022-03-01 | Innovation Calumet Llc | Method for coating a structure with a fusion bonded material |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2111853A (en) * | 1935-10-16 | 1938-03-22 | Int Cellucotton Products | Cord coating machine |
US2711481A (en) * | 1954-06-09 | 1955-06-21 | Haloid Co | Xeroradiography method and device |
US2817765A (en) * | 1956-01-03 | 1957-12-24 | Haloid Co | Xerographic method |
US2859129A (en) * | 1956-01-11 | 1958-11-04 | Haloid Xerox Inc | Process for developing electrostatic images and apparatus therefor |
US2862472A (en) * | 1956-11-29 | 1958-12-02 | Battelle Development Corp | Electrostatic image development apparatus |
US2914221A (en) * | 1955-08-16 | 1959-11-24 | Haloid Xerox Inc | Aerosol bomb development |
GB993566A (en) * | 1961-01-10 | 1965-05-26 | Knapsack Ag | Process and apparatus for coating elongated objects |
US3248253A (en) * | 1962-06-22 | 1966-04-26 | Sames Sa De Machines Electrost | Electrostatic transfer method and apparatus for coating articles with a fluidized composition |
US3336903A (en) * | 1963-04-24 | 1967-08-22 | Sames Sa De Machines Electrost | Electrostatic coating apparatus |
-
1968
- 1968-06-28 US US3566833D patent/US3566833A/en not_active Expired - Lifetime
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2111853A (en) * | 1935-10-16 | 1938-03-22 | Int Cellucotton Products | Cord coating machine |
US2711481A (en) * | 1954-06-09 | 1955-06-21 | Haloid Co | Xeroradiography method and device |
US2914221A (en) * | 1955-08-16 | 1959-11-24 | Haloid Xerox Inc | Aerosol bomb development |
US2817765A (en) * | 1956-01-03 | 1957-12-24 | Haloid Co | Xerographic method |
US2859129A (en) * | 1956-01-11 | 1958-11-04 | Haloid Xerox Inc | Process for developing electrostatic images and apparatus therefor |
US2862472A (en) * | 1956-11-29 | 1958-12-02 | Battelle Development Corp | Electrostatic image development apparatus |
GB993566A (en) * | 1961-01-10 | 1965-05-26 | Knapsack Ag | Process and apparatus for coating elongated objects |
US3248253A (en) * | 1962-06-22 | 1966-04-26 | Sames Sa De Machines Electrost | Electrostatic transfer method and apparatus for coating articles with a fluidized composition |
US3336903A (en) * | 1963-04-24 | 1967-08-22 | Sames Sa De Machines Electrost | Electrostatic coating apparatus |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3853581A (en) * | 1972-06-02 | 1974-12-10 | Air Ind | Method of coating articles with electrostatically charged particles |
US4011832A (en) * | 1975-02-26 | 1977-03-15 | Westinghouse Electric Corporation | Build control for fluidized bed wire coating |
US4035521A (en) * | 1975-02-26 | 1977-07-12 | Westinghouse Electric Corporation | Build control for fluidized bed wire coating |
FR2310619A1 (en) * | 1975-05-05 | 1976-12-03 | Northern Telecom Ltd | METHOD FOR MANUFACTURING A THERMALLY INSULATED AND POLYMER-COATED ELECTRICAL CONDUCTOR AND CONDUCTOR SO OBTAINED |
US4084019A (en) * | 1976-02-05 | 1978-04-11 | Armco Steel Corporation | Electrostatic coating grid and method |
US4069792A (en) * | 1976-02-26 | 1978-01-24 | Canada Wire And Cable Limited | Electrostatic fluidized bed coating unit |
US4008685A (en) * | 1976-04-20 | 1977-02-22 | Westinghouse Electric Corporation | Electrostatic fluidized bed build control |
FR2348749A1 (en) * | 1976-04-20 | 1977-11-18 | Westinghouse Electric Corp | ELECTROSTATIC FLUIDIZED BED INSTALLATION |
US4051809A (en) * | 1976-09-22 | 1977-10-04 | Westinghouse Electric Corporation | Apparatus for cleaning and coating an elongated metallic member |
US4100883A (en) * | 1976-10-18 | 1978-07-18 | General Electric Company | Apparatus for electrostatic deposition on a running conductor |
US4271783A (en) * | 1978-01-20 | 1981-06-09 | General Electric Company | Apparatus for fluidized bed-electrostatic coating of indefinite length substrate |
EP0007634A1 (en) * | 1978-07-31 | 1980-02-06 | Northern Telecom Limited | Apparatus and method for use in fluidized powder filling of multiple core unit cables |
EP0023238A1 (en) * | 1979-07-30 | 1981-02-04 | Philips Kommunikations Industrie AG | Method and device for manufacturing varnish-insulated winding wire, in particular thick wires |
EP0110542A1 (en) * | 1982-10-28 | 1984-06-13 | Florida Wire And Cable Company | Concrete strengthening members, particularly prestressing tendons, having improved corrosion resistance and/or bonding characteristics, and methods relating thereto |
US4606928A (en) * | 1985-03-07 | 1986-08-19 | Electrostatic Technology Incorporated | Vortex effect electrostatic fluidized bed coating method and apparatus |
WO1986005127A1 (en) * | 1985-03-07 | 1986-09-12 | Electrostatic Technology, Inc. | Vortex effect electrostatic fluidized bed coating method and apparatus |
US6200678B1 (en) * | 1986-02-19 | 2001-03-13 | Florida Wire & Cable, Inc. | Corrosion resistant coated metal strand |
US4808432A (en) * | 1986-08-18 | 1989-02-28 | Electrostatic Technology Incorporated | Electrostatic coating apparatus and method |
JP2014008486A (en) * | 2012-07-02 | 2014-01-20 | Kawanetsu Co Ltd | Method for manufacturing polyethylene terephthalate resin-coated metal filament |
US11260419B2 (en) * | 2018-03-02 | 2022-03-01 | Innovation Calumet Llc | Method for coating a structure with a fusion bonded material |
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Legal Events
Date | Code | Title | Description |
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1982-01-18 | AS | Assignment |
Owner name: ATLANTIC RICHFIELD COMPANY, A PA CORP. Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:ANACONDA COMPANY THE, A DE CORP;REEL/FRAME:003992/0218 Effective date: 19820115 |