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US4032415A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for promoting reduction oxidation of electrolytically produced gas

Assignee: Mead Corp
•
Filing: 1976-09-30
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Granted: 1977-06-28
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Expires: 1996-09-30
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Abstract

Abstract Gaseous products which tend to form at the anode or cathode of an electrolytic or electrochemical system in which the electrolyte is an aqueous medium may be converted into a reduction-oxidation reaction product through the action of a Contacogen. In such electrolytic systems, hydrogen is usually produced at the cathode and oxygen or other gas may be produced at the anode. By placing a Contacogen in gas receiving relation with the electrode at which a gas tends to be produced, and externally introducing a second gas into contact with the electrode gas and the Contacogen in the presence of an aqueous medium, the two gases enter into a reduction-oxidation reaction to produce a product which is electrolytically noninterferring. The Contacogen is particulate in nature and maintained in a static condition and forms the situs of reaction between the two gases in the presence of an aqueous medium. The Contacogen is wetproofed to prevent flooding thereof by the aqueous medium and operates to increase the rate of reaction between the gaseous reactants in the aqueous medium over the possible at room temperatures and pressures absent the Contacogen. Thus the present invention provides a novel method and apparatus for substantally eliminating one or more gaseous products formed in electrolytic systems having an aqueous medium as the electrolyte.

Inventors

  • 👤 Frederick W. Sanders

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 20:48
CPC Classifications
C; C25; C25B; C25B1/00; C25B9/00; C25B9/40; C25B9/47; C25B9/70; C25B1/01; C25B1/02; C25B1/04

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 181 words
In a method of conducting electrolytic reactions by contacting an anode and cathode with an aqueous electrolyte and imposing a current flow from one electrode to the other through the electrolyte thereby producing chlorine gas at the anode, the improvement comprising: (a) positioning a fixed static bed of solid particles selected from the group consisting of carbon particles, activated carbon particles, and platinized compound particles, in a fixed, static condition adjacent the anode so as to receive the chlorine gas electrolytically produced at the anode, (b) introducing a second gas capable of reducing said chlorine gas directly into said fixed static bed of solid particles without disrupting the non-turbulent condition of said fixed static bed, and (c) introducing an aqueous solution into contact with said solid particles, said solid particles being essentially inert with respect to said chlorine gas, said second gas, said aqueous solution, and the reaction product of said reaction and each solid particle being wetproofed by treatment with a substance not wetted by said aqueous solution in order to effectively promote the non-electrolytic reduction of said chlorine gas.
Claim 2
Dependent Claim 181 words
In a method of conducting electrolytic reactions by contacting an anode and cathode with an aqueous electrolyte and imposing a current flow from one electrode to the other through the electrolyte thereby producing chlorine gas at the anode, the improvement comprising: (a) positioning a fixed static bed of solid particles selected from the group consisting of carbon particles, activated carbon particles, and platinized compound particles, in a fixed, static condition adjacent the anode so as to receive the chlorine gas electrolytically produced at the anode, (b) introducing a second gas capable of reducing said chlorine gas directly into said fixed static bed of solid particles without disrupting the non-turbulent condition of said fixed static bed, and (c) introducing an aqueous solution into contact with said solid particles, said solid particles being essentially inert with respect to said chlorine gas, said second gas, said aqueous solution, and the reaction product of said reaction and each solid particle being wetproofed by treatment with a substance not wetted by said aqueous solution in order to effectively promote the non-electrolytic reduction of said chlorine gas.
Claim 3
Dependent Claim 20 words
A method as set forth in claim 1 wherein said solid particles are carbon particles wetproofed with a fluorocarbon resin.
Claim 4
Dependent Claim 36 words
A method as set forth in claim 1 wherein said solid particles are carbon particles above about 9 millimicrons in size and wetproofed with 0.1 to 100% by weight of said carbon particles of polytetrafluoroethylene resin.

References Cited (Backward Citations)

US3645863A Cited
US3966571A Cited
US3970531A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-06-27 1980-12-27 1981-06-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-06-27 1984-12-27 1985-06-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-06-27 1988-12-27 1989-06-28 $7700.00 Window Closed / Lapsed

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