US4104133A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of in situ plating of an active coating on cathodes of alkali halide electrolysis cells
Assignee: ELECTRODE Corp A CORP OF
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Filing: 1977-07-27
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Granted: 1978-08-01
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Expires: 1997-07-27
Abstract
Abstract An active metal coating which lowers the hydrogen discharge overpotential at the cathode in the electrolysis of aqueous alkali metal halide solutions is deposited on the cathode tubes of a cathode can of an electrolysis cell without the removal of the tubes from the can. Plating solution and anodes of plating metal are placed inside a cathode can and the components are electrically connected so as to deposit an active coating onto the cathode tubes. The plating metal is preferably an alloy of nickel and zinc and the process involves the final step of leaching the zinc component of the alloy deposit from the plated cathode tubes to provide a porous, active nickel surface which results in a reduction of the hydrogen discharge overpotential for the electrolysis of alkali metal halides, particularly sodium chloride.
Inventors
- 👤 James R. Brannan
- 👤 Irving Malkin
- 👤 Claude M. Brown
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 08:50
CPC Classifications
C; C25; C25D; C25D5/00; C25D5/02; C25B; C25B11/00; C25B11/04; C25B11/051; C25B11/073; C25B11/075; C25D5/48; C25D7/00; C25D7/04
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
211 words
A method of in situ electrodeposition of a nickel-zinc alloy coating onto surfaces of cathode tubes disposed within a cathode can of an electrolysis cell for the production of ahlogens and alkali metal hydroxides, said cathode tubes each having a pair of vertically oriented parallel foraminous planar side walls each having outside surfaces and facing inside surfaces and a catholyte space intermediate said inside surfaces and a plurality of horizontally disposed spacer members connecting said inside surfaces of each of said pair of foraminous side walls and having vertically aligned openings therethrough, the method which comprises: cleaning and rinsing said cathode can; immersing said cathode can in a plating solution containing nickel ions and zinc ions; immersing plating anodes within said cathode can and parallel to said cathode tubes; electrically connecting said plating anodes and said cathode tubes to a source of direct current so that said plating anodes are anodic and said cathode tubes are cathodic; electrodepositing a nickel-zinc alloy coating on said inside and outside surfaces of said cathode tubes; removing said anodes and said plating solution from said electrolysis cell, and leaching said coating to remove at least some zinc therefrom whereby said cell may be placed in use for the production of halogens and alkali metal hydroxides.
Claim 2
Independent Claim
211 words
A method of in situ electrodeposition of a nickel-zinc alloy coating onto surfaces of cathode tubes disposed within a cathode can of an electrolysis cell for the production of ahlogens and alkali metal hydroxides, said cathode tubes each having a pair of vertically oriented parallel foraminous planar side walls each having outside surfaces and facing inside surfaces and a catholyte space intermediate said inside surfaces and a plurality of horizontally disposed spacer members connecting said inside surfaces of each of said pair of foraminous side walls and having vertically aligned openings therethrough, the method which comprises: cleaning and rinsing said cathode can; immersing said cathode can in a plating solution containing nickel ions and zinc ions; immersing plating anodes within said cathode can and parallel to said cathode tubes; electrically connecting said plating anodes and said cathode tubes to a source of direct current so that said plating anodes are anodic and said cathode tubes are cathodic; electrodepositing a nickel-zinc alloy coating on said inside and outside surfaces of said cathode tubes; removing said anodes and said plating solution from said electrolysis cell, and leaching said coating to remove at least some zinc therefrom whereby said cell may be placed in use for the production of halogens and alkali metal hydroxides.
Claim 3
Dependent Claim
28 words
The method as described in claim 1 wherein the step of immersing said plating metal anodes includes the step of positioning said anodes internally of said cathode tubes.
Claim 4
Dependent Claim
64 words
The method as described in claim 2 wherein the step of immersing said anodes includes the step of positioning a plurality of rod form plating metal anodes vertically intermediate said inside surfaces of said cathode tubes, said anodes passing through said openings in said spacer members whereby a large portion of the deposited metal is located on the inside surfaces of the cathode tubes.
Claim 5
Dependent Claim
36 words
The method as described in claim 2 wherein the step of immersing said anodes comprises the steps of opening said cathode can and positioning bar form plating metal anodes horizontally within each of said cathode tubes.
Claim 6
Dependent Claim
33 words
The method as described in claim 1 wherein the step of immersing said anodes includes the step of aligning a sheet form anode along each of the exterior faces of said cathode tubes.
Claim 7
Independent Claim
310 words
A method of in situ electrodeposition of a nickel-zinc alloy coating, said coating comprising about 25 to 75 percent nickel and about 75 to 25 percent zinc, onto surfaces of cathode tubes disposed within a cathode can of an electrolysis cell for the production of halogens and alkali metal hydroxides, said cathode tubes each having a pair of vertically oriented, parallel foraminous planar side walls each having outside surfaces and facing inside surfaces and a catholyte space intermediate said inside surfaces and a plurality of horizontally disposed spacer members connecting said inside surfaces of each of said pair of foraminous side walls, each of said of horizontally disposed spacer members having vertically aligned openings therethrough, the method which comprises: cleaning and rinsing said cathode can; immersing said cathode can in a plating solution comprising an aqueous solution of 150 to 300 grams per liter of nickel chloride, 30to 60 grams per liter zinc chloride and having a temperature of 30° to 65° C and a pH ranging from about 1.5 to 5.5; positioning plating metal anodes within said cathode can and parallel to said sidewalls of said cathode tubes; electrically connecting said plating metal anodes and said cathode can to a source of direct current so that said plating metal anodes are anodic and said cathode can is cathodic; electrodepositing a nickel-zinc alloy coating on said inside and outside surfaces of said cathode tubes at a current density ranging from about 0.2 to 2.0 amperes per square inch; electrically disconnecting said plating anodes and said cathode can and separating said cathode can from said anodes and said plating solution, and leaching said coating in a solution of sodium hydroxide so as to remove at least some zinc from said coating whereby said cathode can may be assembled into an electrolytic cell for the production of halogens and alkali metal hydroxides.
Claim 8
Independent Claim
310 words
A method of in situ electrodeposition of a nickel-zinc alloy coating, said coating comprising about 25 to 75 percent nickel and about 75 to 25 percent zinc, onto surfaces of cathode tubes disposed within a cathode can of an electrolysis cell for the production of halogens and alkali metal hydroxides, said cathode tubes each having a pair of vertically oriented, parallel foraminous planar side walls each having outside surfaces and facing inside surfaces and a catholyte space intermediate said inside surfaces and a plurality of horizontally disposed spacer members connecting said inside surfaces of each of said pair of foraminous side walls, each of said of horizontally disposed spacer members having vertically aligned openings therethrough, the method which comprises: cleaning and rinsing said cathode can; immersing said cathode can in a plating solution comprising an aqueous solution of 150 to 300 grams per liter of nickel chloride, 30to 60 grams per liter zinc chloride and having a temperature of 30° to 65° C and a pH ranging from about 1.5 to 5.5; positioning plating metal anodes within said cathode can and parallel to said sidewalls of said cathode tubes; electrically connecting said plating metal anodes and said cathode can to a source of direct current so that said plating metal anodes are anodic and said cathode can is cathodic; electrodepositing a nickel-zinc alloy coating on said inside and outside surfaces of said cathode tubes at a current density ranging from about 0.2 to 2.0 amperes per square inch; electrically disconnecting said plating anodes and said cathode can and separating said cathode can from said anodes and said plating solution, and leaching said coating in a solution of sodium hydroxide so as to remove at least some zinc from said coating whereby said cathode can may be assembled into an electrolytic cell for the production of halogens and alkali metal hydroxides.
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) | 1981-07-31 | 1982-01-30 | 1982-08-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-07-31 | 1986-01-30 | 1986-08-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-07-31 | 1990-01-30 | 1990-08-01 | $7700.00 | Window Closed / Lapsed |