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US3663401A Expired / Lapsed US ⏱️ 0.0 years remaining

Control of water-soluble acids in an electrodeposition bath

Assignee: PPG Industries Inc
•
Filing: 1970-10-13
•
Granted: 1972-05-16
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Expires: 1990-10-13
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Abstract

Abstract This invention relates to a method of controlling water-soluble acids present in a base-solubilized electrodepositable composition, which comprises subjecting the bath to a selective filtration process such as ultrafiltration and thereby removing water-soluble acids from the bath.

Inventors

  • 👤 Roger M Christenson
  • 👤 Louis R Lebras

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 17:29
CPC Classifications
C; C25; C25D; C25D13/00; C25D13/22; C25D13/24

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 67 words
In a method of operating a continuous electrocoating operation wherein electrically-conductive objects are provided with an organic coating by electrically-induced deposition of organic coating material in which said objects are passed through an aqueous dispersion of said coating material retained in a coating bath, the improvement comprising employing as at least a portion of said aqueous dispersion an aqueous dispersion treated by the method of claim 1.
Claim 2
Dependent Claim 42 words
A method as in claim 1 wherein the ultrafiltration process is operated at a pressure gradient between about 10 and about 150 p.s.i. and the ultrafiltration membrane has a flux rate of at least about 4.5 gallons per square foot per day.
Claim 3
Dependent Claim 18 words
A method as in claim 1 wherein the water-soluble acid salt removed is a salt of formic acid.
Claim 4
Dependent Claim 67 words
In a method of operating a continuous electrocoating operation wherein electrically-conductive objects are provided with an organic coating by electrically-induced deposition of organic coating material in which said objects are passed through an aqueous dispersion of said coating material retained in a coating bath, the improvement comprising employing as at least a portion of said aqueous dispersion an aqueous dispersion treated by the method of claim 4.
Claim 5
Dependent Claim 15 words
A method as in claim 1 wherein the polyacid resin is a carboxylic acid resin.
Claim 6
Dependent Claim 17 words
A method as in claim 6 wherein the electrodeposition bath has been previously utilized to electrocoat articles.
Claim 7
Dependent Claim 42 words
A method as in claim 7 wherein the ultrafiltration process is operated at a pressure gradient between about 10 and about 150 p.s.i. and the ultrafiltration membrane has a flux rate of at least about 4.5 gallons per square foot per day.
Claim 8
Dependent Claim 14 words
A method as in claim 8 wherein the ultrafiltration membrane is an anisotropic membrane.
Claim 9
Dependent Claim 18 words
A method as in claim 8 wherein the water-soluble acid salt removed is a salt of formIc acid.
Claim 10
Dependent Claim 67 words
In a method of operating a continuous electrocoating operation wherein electrically-conductive objects are provided with an organic coating by electrically-induced deposition of organic coating material in which said objects are passed through an aqueous dispersion of said coating material retained in a coating bath, the improvement comprising employing as at least a portion of said aqueous dispersion an aqueous dispersion treated by the method of claim 10.
Claim 11
Dependent Claim 14 words
A method as in claim 1 wherein the electrodeposition bath contains an aldehyde-derived resin.
Claim 12
Dependent Claim 42 words
A method as in claim 12 wherein the ultrafiltration process is operated at a pressure gradient between about 10 and about 150 p.s.i. and the ultrafiltration membrane has a flux rate of at least about 4.5 gallons per square foot per day.
Claim 13
Dependent Claim 67 words
In a method of operating a continuous electrocoating operation wherein electrically-conductive objects are provided with an organic coating by electrically-induced deposition of organic coating material in which said objects are passed through an aqueous dispersion of said coating material retained in a coating bath, the improvement comprising employing as at least a portion of said aqueous dispersion an aqueous dispersion treated by the method of claim 12.
Claim 14
Dependent Claim 15 words
A method as in claim 12 wherein the polyacid resin is a carboxylic acid resin.
Claim 15
Dependent Claim 67 words
In a method of operating a continuous electrocoating operation wherein electrically-conductive objects are provided with an organic coating by electrically-induced deposition of organic coating material in which said objects are passed through an aqueous dispersion of said coating material retained in a coating bath, the improvement comprising employing as at least a portion of said aqueous dispersion an aqueous dispersion treated by the method of claim 15.
Claim 16
Dependent Claim 14 words
A method as in claim 15 wherein the ultrafiltration membrane is an anisotropic membrane.
Claim 17
Dependent Claim 17 words
A method as in claim 15 wherein the electrodeposition bath has been previously utilized to electrocoat articles.
Claim 18
Dependent Claim 42 words
A method as in claim 18 wherein the ultrafiltration process is operated at a pressure gradient between about 10 and about 150 p.s.i. and the ultrafiltration membrane has a flux rate of at least about 4.5 gallons per square foot per day.
Claim 19
Dependent Claim 18 words
A method as in claim 19 wherein the water-soluble acid salt removed is a salt of formic acid.
Claim 20
Dependent Claim 67 words
In a method of operating a continuous electrocoating operation wherein electrically-conductive objects are provided with an organic coating by electrically-induced deposition of organic coating material in which said objects are passed through an aqueous dispersion of said coating material retained in a coating bath, the improvement comprising employing as at least a portion of said aqueous dispersion an aqueous dispersion treated by the method of claim 20.

References Cited (Backward Citations)

US3496083A Cited
US3444066A Cited
US3528901A Cited
US3556970A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-05-16 1975-11-15 1976-05-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-05-16 1979-11-15 1980-05-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-05-16 1983-11-15 1984-05-16 $7700.00 Window Closed / Lapsed

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