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US3615862A Expired / Lapsed US ⏱️ 0.0 years remaining

Fuel cell electrodes

Assignee: RTX Corp
•
Filing: 1967-02-20
•
Granted: 1971-10-26
•
Expires: 1987-02-20
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Abstract

Abstract Activated fuel cell electrodes are prepared by electrodeposition of a noble metal catalyst on a solid foil or porous electrode substrate. The electrodeposition is effected from an alkali metal hydroxide solution, preferably molten alkali metal hydroxide. The electrolysis is generally carried out at temperatures of about 300* to 500* F. at current densities of about 5 to 150 ma./cm.2 by passing a direct electrical current to the electrode substrate through the alkali metal hydroxide electrolyte solution. Palladium-black is a preferred noble metal catalyst, and palladium or palladium-silver alloy foils and porous sintered nickel structures are the preferred electrode substrates.

Inventors

  • 👤 Hilton A Roth
  • 👤 William R Lasko

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 13:34
CPC Classifications
H; H01; H01M; H01M4/00; H01M4/86; H01M4/88; H01M4/8825; H01M4/8853; H01M4/90; H01M4/92; H01M4/921; Y; Y02; Y02E; Y02E60/00; Y02E60/30; Y02E60/50

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 39 words
The process of claim 1, in which the alkali metal hydroxide electrolyte solution is maintained at a temperature not greater than about 25* F. above the temperature to which the activated electrode is to be subjected in subsequent use.
Claim 2
Dependent Claim 20 words
The process of claim 1, in which the electrolyte solution is an 85 percent by weight solution of potassium hydroxide.
Claim 3
Dependent Claim 14 words
The process of claim 1 in which the electrode is a transition metal electrode.
Claim 4
Dependent Claim 31 words
The process of claim 4 in which electrolysis of the transition metal electrode is carried out at a current density between 5 and 150 milliamps per cm.2 of electrode surface area.
Claim 5
Dependent Claim 27 words
The process of claim 5, in which electrolysis is carried out at a current density between about 10 and 25 milliamps per cm.2 of electrode surface area.
Claim 6
Dependent Claim 25 words
The process of claim 1, in which the noble metal catalyst is selected from the group consisting of Pd, Ru, Pt, Re, Rh, and Os.
Claim 7
Dependent Claim 13 words
The process of claim 7, in which the noble metal catalyst is Pd.
Claim 8
Dependent Claim 34 words
The process of claim 4, in which the transition metal electrode is constructed of a metal selected from the group consisting of Zr, Ti, Mo, Pd, Fe, Ni, and alloys of Pd and Ag.
Claim 9
Dependent Claim 11 words
The process of claim 4, in which the electrode is Pd.
Claim 10
Dependent Claim 13 words
The process of claim 4, in which the electrode is a Pd-Ag alloy.
Claim 11
Dependent Claim 105 words
A process for activating Pd or Pd-Ag fuel cell electrodes to improve and stabilize the hydrogen transfer rate through such electrodes during cell operation, which comprises: inserting a Pd or Pd-Ag foil electrode into an electrolyte solution consisting essentially of molten KOH and containing about 1 to 3 percent Pd by weight of the solution in the form of an ionizable salt of Pd; maintaining the electrolyte solution at a temperature of about 450* F.; and applying an electric current of about 15 milliamps per cm.2 of electrode surface area to said electrode to cause precipitation of the Pd onto the surface of the electrode.
Claim 12
Dependent Claim 25 words
The process of claim 12, in which the ionizable Pd salt is PdC12 and the electrolyte solution contains about 2 percent by weight of Pd.
Claim 13
Dependent Claim 167 words
A process for activating fuel cell electrodes and using the activated electrodes in a fuel cell to generate electrical current and improve and stabilize the hydrogen transfer rate through the electrodes during cell operation which comprises: inserting an electrode to be activated into a molten alkali meTal hydroxide electrolyte solution containing a minor amount of a salt of a noble metal catalyst, the temperature of the electrolyte solution being between about 300* F. to 500* F., said temperature being below the boiling point of the electrolyte solution but at least as great as the temperature to which the activated electrode is to be subjected in subsequent use, passing an electric current to the electrode through the molten alkali metal hydroxide solution to cause precipitation of the noble metal catalyst onto the surface of the electrode to form an activated electrode, and then inserting said activated electrode in a fuel cell and operating the fuel cell at a temperature not greater than the temperature of the electrolyte solution.

References Cited (Backward Citations)

No citation records indexed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1974-10-25 1975-04-26 1975-10-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1978-10-25 1979-04-26 1979-10-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1982-10-25 1983-04-26 1983-10-26 $7700.00 Window Closed / Lapsed

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