US4411742A
Expired / Lapsed
US
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Electrolytic codeposition of zinc and graphite and resulting product
Assignee: Ford Global Technologies LLC
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Filing: 1982-12-01
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Granted: 1983-10-25
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Expires: 2002-12-01
Abstract
Abstract A high lubricity codeposit of zinc and graphite, and an improved method for depositing the codeposit, is disclosed. The coating is characterized by a coefficient of friction equal to or less than 0.130, and a high resistance to corrosion evidenced by no red rust in a salt spray environment for 72 hours and no destruction due to corrosion in an industrial environment, containing sulphur dioxide, for four months. When the codeposit additionally has a chromate outer coating, the system has a coefficient of friction equal to or less than 0.112 and has no red rust in a salt spray environment for at least 120 hours. The codeposit is applied by immersing a cleansed metallic substrate in an acidic zinc plating electrolyte containing at least 40 g/l zinc ions and 30-110 g/l insoluble bulk graphite, with a pH of 5-5.7. The cell of which the electrolyte is a part is energized to plate out a co-deposit; the graphite is continuously agitated while in solution, the agitation being periodically interrupted to allow the graphite to settle and saturate the zinc interface as it is plating out.
Inventors
- 👤 William A. Donakowski
- 👤 John R. Morgan
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 19:51
CPC Classifications
C; C25; C25D; C25D15/00; C25D15/02; C25D5/00; C25D5/48
Claims Analysis
Total Claims: 27
Claim 1
Independent Claim
83 words
An electrolytic codeposit of zinc and graphite useful as a composite coating on parts subject to sliding friction, said codeposit containing uniformly distributed graphite in an amount of 30-48% by weight of the codeposit, a coefficient of friction equal to or less than 0.130, at a plated thickness of about 0.0005", showing (a) no red rust in a salt spray environment for at least 72 hours, and (b) no destruction due to corrosion in an industrial environment containing sulphur dioxide after four months.
Claim 2
Dependent Claim
83 words
An electrolytic codeposit of zinc and graphite useful as a composite coating on parts subject to sliding friction, said codeposit containing uniformly distributed graphite in an amount of 30-48% by weight of the codeposit, a coefficient of friction equal to or less than 0.130, at a plated thickness of about 0.0005", showing (a) no red rust in a salt spray environment for at least 72 hours, and (b) no destruction due to corrosion in an industrial environment containing sulphur dioxide after four months.
Claim 3
Dependent Claim
22 words
The codeposit of claim 1, wherein the codeposit is effectively solderable using either a resin solder cord or zinc chloride containing flux.
Claim 4
Dependent Claim
59 words
The codeposit of claim 1, electrodeposited on a threaded fastener and subsequently coated with zinc chromate in a thickness of about 0.00002", said coated fastener exhibiting consistent torque performance at a torque load of 40 pounds, a coefficient of friction of about 0.112 or less, and no red rust in a salt spray environment for at least 120 hours.
Claim 5
Independent Claim
71 words
A method of electrodepositing zinc and graphite onto at least a vertical conductive metal substrate by the use of an electrolytic cell having a zinc anode and the metal substrate connected as a cathode, comprising the steps: (a) immersing said substrate in a cleansed condition into an acid/zinc plating electrolyte containing at least 40 g/l zinc ions and 30-110 g/l insoluble bulk graphite, said electrolyte having a pH of 5-5.7; and
Claim 6
Independent Claim
71 words
A method of electrodepositing zinc and graphite onto at least a vertical conductive metal substrate by the use of an electrolytic cell having a zinc anode and the metal substrate connected as a cathode, comprising the steps: (a) immersing said substrate in a cleansed condition into an acid/zinc plating electrolyte containing at least 40 g/l zinc ions and 30-110 g/l insoluble bulk graphite, said electrolyte having a pH of 5-5.7; and
Claim 7
Dependent Claim
54 words
(b) energizing said electrolytic cell at a sufficient current density to plate out zinc onto said surface without burning while continuously agitating said graphite into uniform suspension throughout said electrolyte, said agitation being periodically interrupted to allow said graphite to settle and comingle with said zinc as it is plating out on said cathode.
Claim 8
Dependent Claim
54 words
(b) energizing said electrolytic cell at a sufficient current density to plate out zinc onto said surface without burning while continuously agitating said graphite into uniform suspension throughout said electrolyte, said agitation being periodically interrupted to allow said graphite to settle and comingle with said zinc as it is plating out on said cathode.
Claim 9
Dependent Claim
26 words
The method as in claim 4, in which said agitation is periodically interrupted for 15 to 60 second periods at intervals of 15 to 180 seconds.
Claim 10
Dependent Claim
22 words
The method as in claim 4, in which said bulk graphite has an average particle size of 1-25 microns and is colloidal.
Claim 11
Dependent Claim
47 words
The method as in claim 4, in which said electrolyte is of the acid chloride type constituted by either adding 70-85 g/l zinc chloride with 100-150 g/l potassium chloride, or 45-110 g/l zinc chloride with 100-200 g/l sodium chloride, said electrolyte also containing 26-40 g/l boric acid.
Claim 12
Dependent Claim
15 words
The method as in claim 6, in which said electrolyte additionally contains 0.4-0.1 g/l gelatin.
Claim 13
Dependent Claim
26 words
The method as in claim 6, in which said electrolyte additionally contains 0.1-4.0 g/l cocamine acetate having the formula C 12 H 25 NH 3 .
Claim 14
Dependent Claim
27 words
The method as in claim 4, in which said electrolytic cell is energized by a current density of 1-20 amps per square foot (0.1-2.0 amps/dm 2 ).
Claim 15
Dependent Claim
22 words
The method as in claim 4, in which said agitation is carried out by the use of air pulses into said electrolyte.
Claim 16
Dependent Claim
18 words
The method as in claim 4, in which said electrolyte is maintained at a temperature of 75°-90° F.
Claim 17
Dependent Claim
31 words
The method as in claim 4, in which said metal substrate is selected from the group consisting of steel, copper, nickel, brass, bronze, zinc, and aluminum, as well as conductive plastics.
Claim 18
Dependent Claim
41 words
The method as in claim 4, in which said process additionally comprises the step of dipping said codeposited material into a chromate solution for a period of 10-30 seconds to form a conversion coating on said codeposit consisting of zinc chromate.
Claim 19
Independent Claim
164 words
A method of electroplating a batch of threaded metal fasteners by the use of a barrel plating apparatus having a perforated barrel within which is introduced the electroplating electrolyte solution with the fasteners contacted to constitute a cathode and a suspended zinc anode, the method comprising: (a) dipping said barrel contained fasteners sequentially through a series of tanks, the tanks including a caustic cleaning solution, water rinse, a pickling solution for removing oxides, a water rinse, a zinc/graphite plating solution, and a water rinse; (b) energizing said zinc/graphite plating electrolyte when said barrel contained fasteners are immersed in said solution, said energization being carried out at a level to plate out zinc on said fasteners without burning, said plating being carried out the injection of jet streams of compressed air to maintain the graphite continuously in suspension within said solution; (c) interrupting said barrel rotation and air agitation periodically to allow said graphite to migrate and plate out with said zinc on the cathode.
Claim 20
Independent Claim
164 words
A method of electroplating a batch of threaded metal fasteners by the use of a barrel plating apparatus having a perforated barrel within which is introduced the electroplating electrolyte solution with the fasteners contacted to constitute a cathode and a suspended zinc anode, the method comprising: (a) dipping said barrel contained fasteners sequentially through a series of tanks, the tanks including a caustic cleaning solution, water rinse, a pickling solution for removing oxides, a water rinse, a zinc/graphite plating solution, and a water rinse; (b) energizing said zinc/graphite plating electrolyte when said barrel contained fasteners are immersed in said solution, said energization being carried out at a level to plate out zinc on said fasteners without burning, said plating being carried out the injection of jet streams of compressed air to maintain the graphite continuously in suspension within said solution; (c) interrupting said barrel rotation and air agitation periodically to allow said graphite to migrate and plate out with said zinc on the cathode.
Claim 21
Dependent Claim
26 words
The method as in claim 15, in which said barrel rotation and air agitation is interrupted for periods of 15/60 seconds at intervals of 15/180 seconds.
Claim 22
Dependent Claim
47 words
A high lubricity coating material consisting of electrocodeposited zinc and graphite uniformly distributed, said graphite being present in an amount of at least 30% by weight of the coating, said coating having a coefficient of friction equal to or less than 0.113 at 40 ft/lb torque loading.
Claim 23
Dependent Claim
47 words
A high lubricity coating material consisting of electrocodeposited zinc and graphite uniformly distributed, said graphite being present in an amount of at least 30% by weight of the coating, said coating having a coefficient of friction equal to or less than 0.113 at 40 ft/lb torque loading.
Claim 24
Dependent Claim
39 words
The coating material as in claim 15, in which said electrodeposited coating has a chemically applied outer layer of zinc chromate in a thickness of 0.00002", said codeposited coating having a high degree of resistance to salt spray corrosion.
Claim 25
Dependent Claim
61 words
An electroplated threaded fastener comprising: (a) a substrate of a metal selected from the group consisting of steel, copper, nickel, bronze, brass, zinc, and aluminum; (b) a tightly adherent electrodeposited composite material consisting of zinc and graphite, the graphite being present in an amount of at least 30% by weight of the material; and (c) a conversion zinc chromate outer layer.
Claim 26
Dependent Claim
61 words
An electroplated threaded fastener comprising: (a) a substrate of a metal selected from the group consisting of steel, copper, nickel, bronze, brass, zinc, and aluminum; (b) a tightly adherent electrodeposited composite material consisting of zinc and graphite, the graphite being present in an amount of at least 30% by weight of the material; and (c) a conversion zinc chromate outer layer.
Claim 27
Dependent Claim
54 words
The electroplated threaded fastener of claim 19, in which said coefficient of friction is equal to or less than 0.113, and has a corrosion resistance performance which will provide at least 120 hours of exposure to salt spray environment with no visible red or white corrosion products and exhibit a consistent torque tension relationship.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-10-24 | 1987-04-25 | 1987-10-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-10-24 | 1991-04-25 | 1991-10-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-10-24 | 1995-04-25 | 1995-10-25 | $7700.00 | Window Closed / Lapsed |