US4832876A
Expired / Lapsed
US
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Process for the manufacture of higher fatty monoglyceride monosulfate detergents
Assignee: Colgate Palmolive Co
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Filing: 1987-09-14
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Granted: 1989-05-23
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Expires: 2007-09-14
Abstract
Abstract A process for the manufacture of water soluble higher fatty monoglyceride monosulfate detergents is described which includes reacting a sulfating agent, such as chlorosulfuric acid, with glycerol dissolved in an organic solvent, such as chloroform, to trisulfate the glycerol, reacting the glycerol trisulfuric acid made with a higher fatty acid or a higher fatty acid methyl ester in such a solvent, extracting the reaction mixture with a solvent for the monoglyceride disulfuric acid, such as aqueous lower alkanol, and neutralizing the extracted monoglyceride disulfuric acid with an aqueous neutralizing agent to make the water soluble detergent salt. Among preferable detergent salts made are sodium hydrogenated coco fatty monoglyceride sulfate, sodium hydrogenated palm kernel fatty monoglyceride sulfate, sodium hydrogenated palm fatty monoglyceride sulfate, sodium hydrogenated tallow fatty monoglyceride sulfate, and mixtures of two or more thereof. In modifications of the processes the extraction and neutralization operations are effected simultaneously, preferably with a slurry of sodium bicarbonate, as neutralizing agent, in aqueous lower alkanol. The products resulting are of improved quality and of higher detergent content and the processes are more efficient, requiring only stoichiometric amounts of reagents, reducing formation of sodium sulfate and improving the yields of detergent, compared to similar prior art products and processes for the production thereof.
Inventors
- 👤 Fahim U. Ahmed
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 02:24
CPC Classifications
C; C07; C07C; C07C303/00; C07C303/24
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
201 words
A process for the manufacture of sodium higher fatty monoglyceride monosulfate, in which the higher fatty moiety is cocoyl or palm kerneloyl, which comprises reacting about three molar proportions of chlorosulfuric acid with one molar proportion of glycerol, dissolved in chloroform, at a temperature in the range of 10° to 60° C., so that the glycerol is completely sulfated to glycerol trisulfuric acid, reacting the glycerol trisulfuric acid, dissolved in chloroform, with coco or palm kernel fatty acid, or coco or palm kernel fatty acid methyl ester for 30 minutes to five hours at a temperature in the range of 30° to 60° C., extracting the reaction mixture resulting with an aqueous n-butanol solvent at a temperature in the range of 10° to 60° C., to extract the coco or palm kernel monoglyceride disulfuric acid made and neutralizing and hydrolyzing such monoglyceride disulfuric acid extract with a neutralizing agent which is aqueous sodium hydroxide, sodium carbonate or sodium bicarbonate, or a plurality thereof, to produce sodium cocoyl or palm kerneloyl monoglyceride sulfate, and removing water, n-butanol and chloroform from such sodium cocoyl or palm kerneloyl monoglyceride monosulfate by evaportion, to produce sodium cocoyl or palm kerneloyl monoglyceride monosulfate in improved yield.
Claim 2
Dependent Claim
201 words
A process for the manufacture of sodium higher fatty monoglyceride monosulfate, in which the higher fatty moiety is cocoyl or palm kerneloyl, which comprises reacting about three molar proportions of chlorosulfuric acid with one molar proportion of glycerol, dissolved in chloroform, at a temperature in the range of 10° to 60° C., so that the glycerol is completely sulfated to glycerol trisulfuric acid, reacting the glycerol trisulfuric acid, dissolved in chloroform, with coco or palm kernel fatty acid, or coco or palm kernel fatty acid methyl ester for 30 minutes to five hours at a temperature in the range of 30° to 60° C., extracting the reaction mixture resulting with an aqueous n-butanol solvent at a temperature in the range of 10° to 60° C., to extract the coco or palm kernel monoglyceride disulfuric acid made and neutralizing and hydrolyzing such monoglyceride disulfuric acid extract with a neutralizing agent which is aqueous sodium hydroxide, sodium carbonate or sodium bicarbonate, or a plurality thereof, to produce sodium cocoyl or palm kerneloyl monoglyceride sulfate, and removing water, n-butanol and chloroform from such sodium cocoyl or palm kerneloyl monoglyceride monosulfate by evaportion, to produce sodium cocoyl or palm kerneloyl monoglyceride monosulfate in improved yield.
Claim 3
Dependent Claim
107 words
A process according to claim 1 wherein the higher fatty moiety of the fatty monoglyceride monosulfuric acid is hydrogenated cocoyl, the glycerol is dissolved in about twice its weigh of chloroform..rm, the temperature of the chloroform is maintained in the range of 30° to 50° C. during the sulfation of the glycerol, the reaction of the glycerol trisulfuric acid is with hydrogenated coco fatty acid, the extraction of the reaction mixture is with an n-butanol-water mixture in which the weight of water is about equal to that of n-butanol, and the neutralization and hydrolysis of the monoglyceride disulfuric acid is with an aqueous solution of sodium hydroxide.
Claim 4
Dependent Claim
109 words
A process according to claim 1 wherein the higher fatty moiety of the fatty monoglyceride monosulfuric acid is hydrogenated palm kerneloyl, the glycerol is dissolved in about twice its weight of chloroform, the temperature of the chloroform is maintained in the range of 30° to 50° C. during the sulfation of the glycerol, the reaction of the glycerol trisulfuric acid is with hydrogenated palm kerneloyl fatty acid, the extraction of the reaction mixture is with an n-butanol-water mixture in which the weight of water is about equal to that of n-butanol, and the neutralization and hydrolysis of the monoglyceride disulfuric acid is with an aqueous solution of sodium hydroxide.
Claim 5
Dependent Claim
92 words
A process according to claim 1 wherein the extraction, neutralization and hydrolysis are carried out simultaneously, utilizing a slurry of sodium bicarbonate, as neutralizing agent, in an aqueous lower alcohol medium, which is stirred vigorously while the pH thereof is maintained in the range of 6.0 to 7.0, insoluble inorganic salt is removed, after such extraction, neutralization and hydrolysis, by filtration, and water, lower alkanol and the organic solvent are removed by evaporation, resulting in the production of sodium higher monoglyceride monosulfate in improved yield and of active detergent content over 60%.
Claim 6
Dependent Claim
149 words
A process according to claim 1 wherein the higher fatty moiety of the fatty monoglyceride monosulfuric acid is hydrogenated cocoyl, the glycerol is dissolved in twice its weight of chloroform, the temperature of the chloroform is maintained in the range of 20° to 40° C. during the sulfation of the glycerol, the reaction of the glycerol trisulfuric acid made is with hydrogenated coco fatty acid, the extraction, neutralization and hydrolysis are carried out simultaneously, utilizing a slurry of sodium bicarbonate, as neutralizing agent, in the aqueous lower alcoholic medium, which is stirred vigorously while the pH thereof is maintained in the range of 6.0 to 7.0, insoluble inorganic salt is removed by filtration after extraction, neutralization and hydrolysis, and water, lower alkanol and chloroform are removed by evaporation, resulting in the production of sodium hydrogenated cocoyl monoglyceride monosulfate in high yield and of an active ingredient content over 90%.
Claim 7
Dependent Claim
152 words
A process according to claim 3 wherein the higher fatty moiety of the fatty monoglyceride monosulfuric acid is hydrogenated palm kerneloyl, the glycerol is dissolved in twice its weight of chloroform, the temperature of the chloroform is maintained in the range of 20° to 40° C. during the sulfation of the glycerol, the reaction of the glycerol trisulfuric acid made is with hydrogenated palm kernel fatty acid, the extraction, neutralization and hydrolysis are carried out simultaneously, utilizing a slurry of sodium bicarbonate, as neutralizing agent, in the aqueous lower alcoholic medium, which is stirred vigorously while the pH thereof is maintained in the range of 6.0 to 7.0, insoluble inorganic salt is removed by filtration after extraction, neutralization and hydrolysis, and water, lower alkanol and chloroform are removed by evaporation, resulting in the production of sodium hydrogenated palm kerneloyl monoglyceride monosulfate in improved yield and of an active detergent content over 65%.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1992-05-22 | 1992-11-21 | 1993-05-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-05-22 | 1996-11-21 | 1997-05-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-05-22 | 2000-11-21 | 2001-05-23 | $7700.00 | Window Closed / Lapsed |