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US3935121A Expired / Lapsed US ⏱️ 0.0 years remaining

Foam control compositions for aqueous systems, its preparation, and process using same

Assignee: Veolia WTS USA Inc
•
Filing: 1973-06-29
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Granted: 1976-01-27
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Expires: 1993-06-29
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Abstract

Abstract A foam control composition, and methods for its production and use, is disclosed, which comprises a liquid hydrocarbon carrier, an organic emulsifier, an amide of a fatty acid, and, optionally, a silicone oil. Composition is useful in controlling foam encountered in preparation of paper pulp, resinous materials, and in the treatment of waste systems and cooling towers. The foam control composition is prepared by (a.) combining the amide, emulsifier and from about 1/5 to about 1/2 of the liquid hydrocarbon carrier, (b.) heating until a clear melt is obtained, (c.) rapidly adding to said melt the remainder of said liquid hydrocarbon carrier to cool the melt to a temperature of from ca. 150°F. to ca. 200°F., and (d.) allowing the cooled mixture to further cool to a temperature of from about ambient to about 135°F.

Inventors

  • 👤 Hillel Lieberman
  • 👤 Anthony J. Graffeo
  • 👤 John S. Kucsan

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 05:00
CPC Classifications
B; B01; B01D; B01D19/00; B01D19/02; B01D19/04; B01D19/0404

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 190 words
A process for preparing a foam control composition for aqueous systems, said composition consisting essentially of from about 1% to about 10% of an amide, from about 1% to about 10% of an emulsifier, from about 88% to about 98% of a liquid hydrocarbon carrier, and from 0% to about 2% of a silicone oil, which process comprises: a. Combining the amide, the emulsifier, and from about 1/5 to about 1/2 of said liquid hydrocarbon carrier; b. Heating the amide, emulsifier, and the liquid hydrocarbon carrier amount until a clear melt is obtained; c. Rapidly adding to said melt the remainder of said liquid hydrocarbon carrier to cool the melt to a temperature of from about 150°F. to about 200°F.; d. Allowing the cooled mixture to further cool to a temperature of from about ambient to about 135°F.; all said percentages being on a weight basis and wherein said amide is obtained by the reaction of a polyamine containing an alkylene group of from 2 to 6 carbons, with a fatty acid or a mixture of fatty acids, having an average composition of 6 to 22 carbons per acid molecule.
Claim 2
Dependent Claim 190 words
A process for preparing a foam control composition for aqueous systems, said composition consisting essentially of from about 1% to about 10% of an amide, from about 1% to about 10% of an emulsifier, from about 88% to about 98% of a liquid hydrocarbon carrier, and from 0% to about 2% of a silicone oil, which process comprises: a. Combining the amide, the emulsifier, and from about 1/5 to about 1/2 of said liquid hydrocarbon carrier; b. Heating the amide, emulsifier, and the liquid hydrocarbon carrier amount until a clear melt is obtained; c. Rapidly adding to said melt the remainder of said liquid hydrocarbon carrier to cool the melt to a temperature of from about 150°F. to about 200°F.; d. Allowing the cooled mixture to further cool to a temperature of from about ambient to about 135°F.; all said percentages being on a weight basis and wherein said amide is obtained by the reaction of a polyamine containing an alkylene group of from 2 to 6 carbons, with a fatty acid or a mixture of fatty acids, having an average composition of 6 to 22 carbons per acid molecule.
Claim 3
Dependent Claim 22 words
The process of claim 1 further comprising a final step of adding up to 2% of a silicone oil to the mixture.
Claim 4
Dependent Claim 8 words
The product of the process of claim 2.
Claim 5
Dependent Claim 25 words
A process for controlling the foam of an aqueous system, which comprises adding to said system an effective amount of the product of claim 3.

References Cited (Backward Citations)

US2603599A Cited
US3677963A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-01-26 1979-07-28 1980-01-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-01-26 1983-07-28 1984-01-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-01-26 1987-07-28 1988-01-27 $7700.00 Window Closed / Lapsed

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