US2236861A - Cataphoretic coating apparatus - Google Patents
Cataphoretic coating apparatus Download PDFInfo
- Publication number
- US2236861A US2236861A US187632A US18763238A US2236861A US 2236861 A US2236861 A US 2236861A US 187632 A US187632 A US 187632A US 18763238 A US18763238 A US 18763238A US 2236861 A US2236861 A US 2236861A
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- US
- United States
- Prior art keywords
- wire
- cylinder
- coating
- particles
- coating apparatus
- Prior art date
- 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.)
- Expired - Lifetime
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- 239000011248 coating agent Substances 0.000 title description 21
- 238000000576 coating method Methods 0.000 title description 21
- 239000002245 particle Substances 0.000 description 16
- 239000000463 material Substances 0.000 description 12
- 239000000725 suspension Substances 0.000 description 8
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- 238000003756 stirring Methods 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 238000000151 deposition Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000001464 adherent effect Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- NEDFZELJKGZAQF-UHFFFAOYSA-J strontium;barium(2+);dicarbonate Chemical class [Sr+2].[Ba+2].[O-]C([O-])=O.[O-]C([O-])=O NEDFZELJKGZAQF-UHFFFAOYSA-J 0.000 description 3
- 230000008021 deposition Effects 0.000 description 2
- 230000005012 migration Effects 0.000 description 2
- 238000013508 migration Methods 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 229920001342 Bakelite® Polymers 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 239000004637 bakelite Substances 0.000 description 1
- AYJRCSIUFZENHW-UHFFFAOYSA-L barium carbonate Chemical class [Ba+2].[O-]C([O-])=O AYJRCSIUFZENHW-UHFFFAOYSA-L 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 210000002445 nipple Anatomy 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D13/00—Electrophoretic coating characterised by the process
- C25D13/12—Electrophoretic coating characterised by the process characterised by the article coated
- C25D13/16—Wires; Strips; Foils
Definitions
- An object of my invention is to provide cataphoretic coating apparatus which may be used in continuous factory production for uniformly coating large quantities of cathodes, and which is easy and inexpensive to operate.
- the apparatus shown for purposes of illustration in Figure 1 for continuously coating a cathode wire I comprises a container 2, preferably of glass or non-metallic walls, with a tubulation '3 in the bottom of the container.
- the tubulation is closed at its inner end by a rubber nipple 4 having a small opening in which the cathode wire fits liquid-tight and through which strip metal such as wire is drawn upwardly through the suspension 5 containing in the desired concentration the particles of coating material, such as barium-strontium carbonates.
- the negative terminal of a source of voltage 6 is connected through a sliding contact to the moving wire and its positive terminal is connected to a perforated hollow cylinder 1, concentric with the wire and preferably of metal such as nickel to function as an anode.
- a negative potential on the cathode causes'the positively charged particles to migrate to the cathode where they deposit in a smooth adherent coating.
- the wire is preferably drawn through a furnace to dry the coating, and then reeled on a spool.
- a tungsten wire .0005 inch in diameter has been coated with .001 inch layer of barium-strontium carbonates by moving the wire at the rate of 25 feet per. minute vertically through a methanol suspension 3 inches deep containing 5 grams of barium-strontium carbonates per cubic centimeters, ground to a particle size of about 5 microns.
- the cylindrical anode was about 1 inch in diameter and uniformly perforated with one-eighth inch holes. A potential of about 25 volts was applied between the anode and wire, and the layer or coating was smooth, adherent and even.
- the cylinder with small perforations throughout its length prevents the generation of disturbing eddy currents immediately surrounding the wire and yet at the same time permits the migration of carbonate particles through the perforations to the wire.
- Even mass rotational movement of the body of liquid within the perforated cylinder will not disturb electron material deposited on the wire because the velocity of the solution is substantially zero at the wire located along the center of rotation of the cylinder.
- the concentration of the material in the suspending solution, because of stirring, is uniform throughout the solution, insuring uniform deposition of the particles on the wire.
- the perforated cylinder in Figure 1 has been described as of nickel and connected as the anode for cataphoretically coating wire i, the cylinder may, if desired, be non-metallic, of Bakelite, for example.
- an anode may be placed inside or outside the cylinder, and this anode may be cylindrical, concentric with the wire and perforated like cylinder I, or it obviously may be one or more metal rods parallel with the wire.
- the wire to be coated may, if desired, be moved horizontally through the suspending solution as shown in Figure 2 with the wire drawn into and out of the surface of the solution to obviate the necessity of a liquid-tight bushing below the surface level 01 me solution.
- Wire I is drawn from a reel over an idling pulley downward into the suspension 5 in tank Hi to a second idling pulley positioned at the center of perforated cylinder I I.
- the wire is drawn centrally through the cylinder, slightly inclined with its right hand end above the level of the liquid, and through an electrically heated drying furnace I! on to a reel.
- One terminal of battery 6 is electrically connected to the wire and the other terminal may be connected to cylinder ll, if metal, or to anode I3 mounted parallel to the wire.
- the particles in suspension are continuously agitated by the motor driven propeller M to distribute them uniformly through the suspension inside and outside the perforated cylinder so that the particles are evenly deposited on the wire as it moves longitudinally along the center of the cylinder.
- the small perforations in the cylinder ll prevent the generation of convection currents immediately surrounding the wire and at the same time permit the migration of the particles through the perforations to the wire.
- My improved device-for cataphoretically coating cathodes with a layer of electron emissive material is particularly useful in continuous factory production for rapidly coating large quantities of cathodes with a smooth and uniform coating of electron emissive material, and is easy and inexpensive to operate.
- Apparatus for cataphoretically coating a wire with a material comprising a liquid container for holding particles of said material in suspension, a perforated metal cylinder journalled to rotate about a vertical line in said container with the lower end of the cylinder adjacent the bottom of the container, stirring fins attached to the exterior lower end of said cylinder for agitating the liquid in the container, means for rotating said cylinder and attached fins, a liquidtightbushing in the bottom of said container, and means for drawing said wire throughsaid bushing and upward along said center line of the cylinder.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
April 1, 1941. E. e. WIDELL 2,236,861
CAI'APHORETIG COATING APPARATUS Filed Jan. 29, 1938 INVENTOR. EM/L G. W/DELL ATTORNEY.
Patented Apr. 1, 1941 CATAPHORETIC COATING APPARATUS Emil G. Widell, Bloomfield, N. 3., assignor, by mesne assignments, to Radio Corporation oi America, New York, N. Y., a corporation of Delaware Application January 29, 1938, Serial No. 187,632
1 Claim. ((71.
My invention relates to means for cataphoretically coating metal, particularly apparatus for depositing electron emissive compounds on cathodes.
Electron emitting material may be cataphoretically deposited on a metal cathode core by dispersing finely divided particles of the mate rial, such as barium carbonates, in a suspending medium from which the charged'particles may migrate to the core. For rapid deposition of a smooth adherent coating on the core the particles should be crystalline and larger than colloidal particles. Crystalline particles tend to settle, which makes uniform coating of cathodes difficult in continuous factory production. Stirring or agitating the suspension to prevent settling of the particles produces convection currents in the solution which cause the coating to be uneven.
An object of my invention is to provide cataphoretic coating apparatus which may be used in continuous factory production for uniformly coating large quantities of cathodes, and which is easy and inexpensive to operate.
A better understanding of my invention ma be obtained by referring to the description of preferred embodiments in the following specification and accompanying drawing in which Figures 1 and 2 show means for stirring the suspension of coating material and for depositing the material on cathode cores.
The apparatus shown for purposes of illustration in Figure 1 for continuously coating a cathode wire I comprises a container 2, preferably of glass or non-metallic walls, with a tubulation '3 in the bottom of the container. The tubulation is closed at its inner end by a rubber nipple 4 having a small opening in which the cathode wire fits liquid-tight and through which strip metal such as wire is drawn upwardly through the suspension 5 containing in the desired concentration the particles of coating material, such as barium-strontium carbonates. The negative terminal of a source of voltage 6 is connected through a sliding contact to the moving wire and its positive terminal is connected to a perforated hollow cylinder 1, concentric with the wire and preferably of metal such as nickel to function as an anode. A negative potential on the cathode causes'the positively charged particles to migrate to the cathode where they deposit in a smooth adherent coating. From the solution the wire is preferably drawn through a furnace to dry the coating, and then reeled on a spool.
For stirring the solution to keep the particles 204-300) I of coating material uniformly distributed through the suspension and for preventing convection 'be attached 'to the lower end of the cylinder,
which is journalled at its upper end and, connected'to a driving pulley.
With this apparatus a tungsten wire .0005 inch in diameter has been coated with .001 inch layer of barium-strontium carbonates by moving the wire at the rate of 25 feet per. minute vertically through a methanol suspension 3 inches deep containing 5 grams of barium-strontium carbonates per cubic centimeters, ground to a particle size of about 5 microns. The cylindrical anode was about 1 inch in diameter and uniformly perforated with one-eighth inch holes. A potential of about 25 volts was applied between the anode and wire, and the layer or coating was smooth, adherent and even.
The cylinder with small perforations throughout its length prevents the generation of disturbing eddy currents immediately surrounding the wire and yet at the same time permits the migration of carbonate particles through the perforations to the wire. Even mass rotational movement of the body of liquid within the perforated cylinder will not disturb electron material deposited on the wire because the velocity of the solution is substantially zero at the wire located along the center of rotation of the cylinder. The concentration of the material in the suspending solution, because of stirring, is uniform throughout the solution, insuring uniform deposition of the particles on the wire. While the perforated cylinder in Figure 1 has been described as of nickel and connected as the anode for cataphoretically coating wire i, the cylinder may, if desired, be non-metallic, of Bakelite, for example. When a non-metallic perforated cylinder is used, an anode may be placed inside or outside the cylinder, and this anode may be cylindrical, concentric with the wire and perforated like cylinder I, or it obviously may be one or more metal rods parallel with the wire.
The wire to be coated may, if desired, be moved horizontally through the suspending solution as shown in Figure 2 with the wire drawn into and out of the surface of the solution to obviate the necessity of a liquid-tight bushing below the surface level 01 me solution. Wire I is drawn from a reel over an idling pulley downward into the suspension 5 in tank Hi to a second idling pulley positioned at the center of perforated cylinder I I. The wire is drawn centrally through the cylinder, slightly inclined with its right hand end above the level of the liquid, and through an electrically heated drying furnace I! on to a reel. One terminal of battery 6 is electrically connected to the wire and the other terminal may be connected to cylinder ll, if metal, or to anode I3 mounted parallel to the wire. The
particles in suspensionare continuously agitated by the motor driven propeller M to distribute them uniformly through the suspension inside and outside the perforated cylinder so that the particles are evenly deposited on the wire as it moves longitudinally along the center of the cylinder. As in Figure 1 the small perforations in the cylinder ll prevent the generation of convection currents immediately surrounding the wire and at the same time permit the migration of the particles through the perforations to the wire.
My improved device-for cataphoretically coating cathodes with a layer of electron emissive material is particularly useful in continuous factory production for rapidly coating large quantities of cathodes with a smooth and uniform coating of electron emissive material, and is easy and inexpensive to operate.
I claim:
Apparatus for cataphoretically coating a wire with a material comprising a liquid container for holding particles of said material in suspension, a perforated metal cylinder journalled to rotate about a vertical line in said container with the lower end of the cylinder adjacent the bottom of the container, stirring fins attached to the exterior lower end of said cylinder for agitating the liquid in the container, means for rotating said cylinder and attached fins, a liquidtightbushing in the bottom of said container, and means for drawing said wire throughsaid bushing and upward along said center line of the cylinder.
EMIL G. WIDELL.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US187632A US2236861A (en) | 1938-01-29 | 1938-01-29 | Cataphoretic coating apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US187632A US2236861A (en) | 1938-01-29 | 1938-01-29 | Cataphoretic coating apparatus |
Publications (1)
Publication Number | Publication Date |
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US2236861A true US2236861A (en) | 1941-04-01 |
Family
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Family Applications (1)
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US187632A Expired - Lifetime US2236861A (en) | 1938-01-29 | 1938-01-29 | Cataphoretic coating apparatus |
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2442863A (en) * | 1944-11-23 | 1948-06-08 | Sylvania Electric Prod | Electrophoresis coating of electron tube parts |
US2500878A (en) * | 1947-11-03 | 1950-03-14 | Dale H Sieling | Cataphoretic apparatus |
US2556257A (en) * | 1942-07-31 | 1951-06-12 | Denes Peter | Method for manufacturing electric condensers |
US2561462A (en) * | 1944-11-30 | 1951-07-24 | Bell Telephone Labor Inc | Electromagnetic core and manufacture thereof |
US2576362A (en) * | 1947-10-08 | 1951-11-27 | Westinghouse Electric Corp | Electrophoretic method of coating wire with graphite |
US2615822A (en) * | 1946-02-21 | 1952-10-28 | William C Huebner | Method of making sheet or web material |
US3024184A (en) * | 1958-09-29 | 1962-03-06 | Sylvania Electric Prod | Electrophoretic article coating machine |
US3211639A (en) * | 1964-03-27 | 1965-10-12 | Mcneill William | Apparatus for electrophoretic deposition of lamellar fluorphlogopite mica sheets |
US4322280A (en) * | 1979-12-11 | 1982-03-30 | Siemens Aktiengesellschaft | Electrolysis device for the galvanic reinforcement of tape-shaped plastic foils which are precoated to be conductive |
US4676881A (en) * | 1986-01-13 | 1987-06-30 | Aluminum Company Of America | Electrocoating cell |
-
1938
- 1938-01-29 US US187632A patent/US2236861A/en not_active Expired - Lifetime
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2556257A (en) * | 1942-07-31 | 1951-06-12 | Denes Peter | Method for manufacturing electric condensers |
US2442863A (en) * | 1944-11-23 | 1948-06-08 | Sylvania Electric Prod | Electrophoresis coating of electron tube parts |
US2561462A (en) * | 1944-11-30 | 1951-07-24 | Bell Telephone Labor Inc | Electromagnetic core and manufacture thereof |
US2615822A (en) * | 1946-02-21 | 1952-10-28 | William C Huebner | Method of making sheet or web material |
US2576362A (en) * | 1947-10-08 | 1951-11-27 | Westinghouse Electric Corp | Electrophoretic method of coating wire with graphite |
US2500878A (en) * | 1947-11-03 | 1950-03-14 | Dale H Sieling | Cataphoretic apparatus |
US3024184A (en) * | 1958-09-29 | 1962-03-06 | Sylvania Electric Prod | Electrophoretic article coating machine |
US3211639A (en) * | 1964-03-27 | 1965-10-12 | Mcneill William | Apparatus for electrophoretic deposition of lamellar fluorphlogopite mica sheets |
US4322280A (en) * | 1979-12-11 | 1982-03-30 | Siemens Aktiengesellschaft | Electrolysis device for the galvanic reinforcement of tape-shaped plastic foils which are precoated to be conductive |
US4676881A (en) * | 1986-01-13 | 1987-06-30 | Aluminum Company Of America | Electrocoating cell |
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