Electrolytic purification of aqueous liquids in the presence of silver ions

• US 4,048,032 A
• Filed: 08/27/1975
• Issued: 09/13/1977
• Est. Priority Date: 09/03/1974
• Status: Expired due to Term

• Current Assignee: Sachs-Systemtechnik GmbH
• Original Assignee: Sachs-Systemtechnik GmbH
• Inventors: Eibl, Volker
• Primary Examiner(s): Prescott, Arthur C.
• Application Number:
  US05/608,244
• Time in Patent Office: 748 Days
• Field of Search: 204/149, 204/151, 204/212, 204/130, 426/322, 426/323, 426/301
• US Class Current: 205/701
• CPC Class Codes: A61L 2/035 Electrolysis
• CPC Class Codes: C02F 1/4606 for producing oligodynamic substances to disinfect the water
• CPC Class Codes: C02F 1/4672 by electrooxydation
• CPC Class Codes: C02F 2305/026 Fenton's reagent

Abstract

Silver ions are used more economically in the electrolytic purification of water by anodic oxidation when the water is electrolyzed between inert electrodes, and the silver ions are generated by separate silver anodes, than by employing the silver anodes also for generating oxygen.

Claims

1. A method of destroying oxidizable contaminants in an aqueous liquid which comprises:

a. adding silver ions to said liquid in a first zone;

b. conveying said liquid from said first zone to a second zone;

c. passing electrolyzing current through said liquid in said second zone in the presence of said silver ions and said contaminants between an anode and a cathode, said anode being in direct contact with said liquid and insoluble in said liquid during said passing of said current;

d. independently controlling the magnitude of said current and the amount of said silver ions to respective values jointly sufficient to destroy said contaminants in said second zone; and

e. withdrawing said liquid in purified condition from said second zone.

2. A method as set forth in claim 1, wherein said silver ions are added to said liquid by passing another electric current between a silver anode and a counterelectrode through said liquid, and the amount of the silver ions added by said passing of the other electric current is controlled by controlling the magnitude of said other current.

3. A method as set forth in claim 2, which further comprises passing depositing current through said purified liquid and thereby precipitating silver values from said liquid outside said second zone.

4. A method as set forth in claim 2, wherein said liquid is fed continuously to said first zone and withdrawn continuously from said second zone, whereby a continuous sequential flow of liquid is maintained through said zones, said liquid being conveyed from said first to said second zone through a conduit having a smaller flow section than the flow section of each of said zones.