IP Library Granted Patent US 7,659,316
Granted Patent B2
US 7,659,316 · App. 11/787,049 · Granted Feb 9, 2010

Foam composition

Assignee: Rusmar Incorporated
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Quick Facts
Patent No.
US 7,659,316
App. No.
11/787,049
Granted
Feb 9, 2010
Kind
B2
Abstract

Foams suitable for such uses as landfill coverage, frost protection, volatile emission control, gas control in mining, are composed of a hydrolyzable protein and a pre-gelatinized cationic modified starch along with other ingredients. The foam concentrate can be made at ambient temperature, is stable over time, can be easily tailored to achieve a desired foam stiffness and drain time characteristic over wide ranges, and can be easily diluted at ambient temperature to produce a foamable composition.

Claims (23)

1. A method of making a foamable concentrate comprising the steps of adding to water a pre-gelatinized cationic modified starch having a degree of substitution of at least approximately 0.02 and a nitrogen content of at least approximately 0.15%, and a stabilized hydrolyzed protein.

2. The method according to claim 1 , in which, when the pre-gelatinized cationic modified starch is added to the water, the water is at a temperature in the range from approximately 10° C. to 60° C.

3. The method according to claim 1 , in which, when the pre-gelatinized cationic modified starch is added to the water, the water is at a temperature in the range from approximately 15° C. to 30° C.

4. The method according to claim 1 , in which the pre-gelatinized cationic modified starch, when added to the water, has a particle size distribution such that not more than about 25% by weight of the starch would pass through a 200 mesh screen.

5. A method of making a stiff foam having a slow drain time comprising the steps of:

making a foamable concentrate by adding to water a pre-gelatinized cationic modified starch having a degree of substitution of at least approximately 0.02 and a nitrogen content of at least approximately 0.15%, and a stabilized hydrolyzed protein;

diluting said foamable concentrate with water to produce a foamable liquid; and

introducing a gas into the foamable liquid to produce a foam.

6. The method according to claim 5 , in which, when the pre-gelatinized cationic modified starch is added to the water, the water is at a temperature in the range from approximately 10° C. to 60° C.

7. The method according to claim 5 , in which, when the pre-gelatinized cationic modified starch is added to the water, the water is at a temperature in the range from approximately 15° C. to 30° C.

8. The method according to claim 5 , in which the pre-gelatinized cationic modified starch, when added to the water, has a particle size distribution such that not more than about 25% by weight of the starch would pass through a 200 mesh screen.

9. The method according to claim 5 , in which, when said foamable concentrate is diluted with water, the water with which said foamable concentrate is diluted is at ambient temperature.

10. The method according to claim 5 , in which the pre-gelatinized cationic-modified starch has a degree of substitution in the range from approximately 0.02 to 0.2.

11. The method according to claim 5 , in which the pre-gelatinized cationic-modified starch has a nitrogen content in the range from approximately 0.15% to 2.0%.

12. The method according to claim 5 , in which the pre-gelatinized cationic-modified starch has a degree of substitution in the range from approximately 0.02 to 0.2 and a nitrogen content in the range from approximately 0.15% to 2.0%.

13. The method according to claim 5 , in which the pre-gelatinized cationic-modified starch has a degree of substitution of approximately 0.04.

14. The method according to claim 5 , in which the pre-gelatinized cationic-modified starch has a nitrogen content of approximately 0.35%.

15. The method according to claim 5 , in which the pre-gelatinized cationic-modified starch has a degree of substitution of approximately 0.04 and a nitrogen content of approximately 0.35%.

16. The method according to claim 5 , in which the foamable concentrate, when diluted with water in the dilution step, also comprises ferrous sulfate.

17. The method according to claim 5 , in which the foamable concentrate, when diluted with water in the dilution step, also comprises a dispersant.

18. The method according to claim 5 , in which the foamable concentrate, when diluted with water in the dilution step, also comprises a dispersant composed of a combination of ammonium lignosulfonate and sodium lignosulfonate.

19. The method according to claim 5 , in which the foamable concentrate, when diluted with water in the dilution step, also comprises ammonium hydroxide.

20. The method according to claim 5 , in which the foamable concentrate, when diluted with water in the dilution step, also comprises ferrous sulfate, a biocide, ammonium hydroxide, ammonium lignosulfonate and sodium lignosulfonate.

Assignments (3)
RELEASE OF SECURITY INTEREST Recorded Sep 13, 2018
From: MANUFACTURERS AND TRADERS TRUST COMPANY
To: L.C. GROUP INC
Reel/Frame 046865/0476 →
SECURITY INTEREST Recorded May 20, 2015
From: LC GROUP, INC.; CROWLEY CHEMICAL COMPANY, INC.; CROWLEY TAR PRODUCTS COMPANY, INC.; CROWLEY REAL ESTATE LLC; RUSMAR SOLUTIONS, INC.; RUSMAR HOLDING CORPORATION; RUSMAR INCORPORATED
To: M&T BANK
Reel/Frame 035677/0637 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 12, 2007
From: KITTLE, PAUL A.; DEHM, DAVID C.
To: RUSMAR INCORPORATED
Reel/Frame 020104/0401 →
Continuity (1)
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