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US3671412A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the removal of ionic contaminants from an electrocoating bath

Assignee: EIDP Inc
•
Filing: 1970-04-28
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Granted: 1972-06-20
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Expires: 1990-04-28
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Abstract

Abstract An electrolysis cell for the removal of ionic contaminants from an electrocoating bath and the utilization of this electrolysis cell in an electrocoating process are the subjects of this invention; the electrolysis cell comprises an anode assembly of a frame having attached thereto a metal anode and an anion permeable membrane that is held by the frame in close relationship with the anode and forms a compartment between the membrane and the anode; a cathode is positioned in a close relationship to the anode assembly; the electrocoating bath is brought into contact with the membrane and anionic impurities that are present in the bath migrate toward the anode and are removed from the compartment in the anode assembly; the membrane is impermeable to the film-forming polymeric materials and pigments utilized in the electrocoating bath and is selectively permeable to the water-soluble anionic impurities in the bath; the electrolysis cell can be positioned directly in the electrocoating bath utilized in the electrocoating process or may be positioned outside of the bath and have the bath passed through the electrolysis cell and recycles into the bath. It is also possible to remove cationic contaminants from the bath by using a cation permeable membrane positioned in a cathode assembly similar to the above anode assembly in the electrolysis cell.

Inventors

  • 👤 James E Lohr

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 01:42
CPC Classifications
C; C25; C25D; C25D13/00; C25D13/22; C25D13/24

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 60 words
The process of claim 1 in which the membrane comprises a woven fabric of a polyester fiber coated with an anion exchange resin and the membrane has an anion perm-selectivity of 80-95 percent, an anion exchange capacity of about 0.7 to 1.3 milliequivalents per gram of membrane, a gel/water content of about 15-30 percent and a thickness of 3-6 mils.
Claim 2
Dependent Claim 26 words
The process of claim 1 in which the electrolysis cell is positioned in the electrocoating cell and operated when the electrocoating cell is not in use.
Claim 3
Dependent Claim 40 words
The process of claim 1 in which the electrolysis cell is separate from the electrocoating cell and the electrocoating bath is continuously pumped into the electrolysis cell and recycled into the electrocoating cell after the ionic impurities have been removed.
Claim 4
Dependent Claim 90 words
The process of claim 1 in which the electrolysis cell comprises a second frame wherein the cathode is positioned and said cathode is coupled to a separate negative electrical source and a cation permeable membrane is attached to the frame and forms a compartment between the cathode and the membrane, said membrane being impermeable to the film-forming polymeric material and pigments of the bath and being selectively permeable to the water-soluble cationic impurities in the bath and comprises a cation exchange resin, and means for removing cations from the compartment.

References Cited (Backward Citations)

US3419488A Cited
US3444063A Cited
US3444064A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-06-20 1975-12-20 1976-06-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-06-20 1979-12-20 1980-06-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-06-20 1983-12-20 1984-06-20 $7700.00 Window Closed / Lapsed

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