US4767560A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Toilet soap bars made from topped, distilled coco fatty acid and processes for manufacture thereof
Assignee: Colgate Palmolive Co
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Filing: 1986-10-02
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Granted: 1988-08-30
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Expires: 2006-10-02
Abstract
Abstract Toilet soap bars, preferably milled and plodded, made from topped, distilled coco fatty acid, which is partially saponified, are superior to tallow-coco soaps and palm oil - palm kernel oil soaps in foaming properties and lather generation, especially in cold water, and are milder to the hands. Yet, such soaps, despite being made entirely from topped, distilled coco fatty acid, are desirably plastic, which improves ease of manufacture and inhibits development of brittleness and any accompanying tendency of soap bars made to crack during drying ater use. The invented soaps are milder than the "control" soaps, made from mixtures of coconut oil with tallow or palm kernel oil, which may be due in part to an appreciably low pH. Also within the inventin are processes for the manufacture of the invented soap bars, which processes include partially saponifying the topped, distilled coco fatty acid, so as to produce a superfatted soap, containing free topped, distilled coco fatty acid, removing water from the partially saponified topped, distilled, coco fatty acid, mixing the superfatted soap with adjuvant(s), plodding to bar form, cutting the bar to lengths and pressing individual lengths to final bar or cake form.
Inventors
- 👤 Gregorio C. Gervasio
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 05:07
CPC Classifications
C; C11; C11D; C11D13/00; C11D13/02; C11D9/00; C11D9/007
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
249 words
A process for manufacturing a toilet soap bar of improved cold water lathering properites, improved stability on storage and improved plasticity, which is mild to the skin and which does not slough excessively when deposited wet on a soap dish, which bar comprises at least 70% of sodium soap of topped, distilled coco fatty acid from which all caproic and caprylic acids have been removed, and in which fatty acid the capric content is less than 2%, 4 to 14% of such topped, distilled free coco fatty acid, 6 to 16% of water and no more than 8% of adjuvant(s), which manufacturing process comprises pre-heating the topped, distilled coco fatty acid, caustic soda solution and brine solution, separately feeding the heated topped, distilled coco fatty acid, caustic soda solution and brine solution to a proportioning pump, discharging them from said proportioning pump to a shear pump in which they are initially intimately mixed and the coco fatty acid and caustic soda are reacted, heating the mixture in an autoclave, recycling a high proportion of the reaction mixture back to such autoclave, while feeding to such autoclave a low proportion of previously unrecycled material discharged from the shear pump, removing the resulting superfatted soap from the autoclave, drying it to a moisture content in the range of 6 to 16%, mixing it with no more than 8% of adjuvant(s), plodding such mixture to bar form, cutting the bar to lengths and pressing such lengths to final bar or cake form.
Claim 2
Dependent Claim
249 words
A process for manufacturing a toilet soap bar of improved cold water lathering properites, improved stability on storage and improved plasticity, which is mild to the skin and which does not slough excessively when deposited wet on a soap dish, which bar comprises at least 70% of sodium soap of topped, distilled coco fatty acid from which all caproic and caprylic acids have been removed, and in which fatty acid the capric content is less than 2%, 4 to 14% of such topped, distilled free coco fatty acid, 6 to 16% of water and no more than 8% of adjuvant(s), which manufacturing process comprises pre-heating the topped, distilled coco fatty acid, caustic soda solution and brine solution, separately feeding the heated topped, distilled coco fatty acid, caustic soda solution and brine solution to a proportioning pump, discharging them from said proportioning pump to a shear pump in which they are initially intimately mixed and the coco fatty acid and caustic soda are reacted, heating the mixture in an autoclave, recycling a high proportion of the reaction mixture back to such autoclave, while feeding to such autoclave a low proportion of previously unrecycled material discharged from the shear pump, removing the resulting superfatted soap from the autoclave, drying it to a moisture content in the range of 6 to 16%, mixing it with no more than 8% of adjuvant(s), plodding such mixture to bar form, cutting the bar to lengths and pressing such lengths to final bar or cake form.
Claim 3
Dependent Claim
216 words
A process according to claim 1 wherein the topped, distilled coco fatty acid comprises 0.0% of caproic acid, 0.0% of caprylic acid, 0.0 to 0.8% of capric acid, 50 to 60% of lauric acid, 20 to 25% of myristic acid, 8 to 12% of palmitic acid, 0.0 to 0.3% of palmitoleic acid, 1 to 4% of stearic acid, 5 to 10% of oleic acid, 0 to 3% of linoleic acid, 0 to 0.2% of linolenic acid, and 0.0 to 0.3% of arachidic acid, and is of an iodine value in the range of 8 to 12, the caustic soda solution is an aqueous solution of 40 to 50% caustic soda content, the brine solution is an aqueous solution of 15 to 20% sodium chloride content, the topped, distilled coco fatty acid, the caustic soda solution and the brine solution are pre-heated individually to temperature(s) in the range of 40° to 80° C., the proportioning pump to which they are fed is of the Bran & Lubbe type, the discharges from the proportioning pump are into a common header immediately prior to the inlet to the shear pump, the shear pump is of the Waukesha type, the autoclave is of the Mazzoni type, and the autoclave recycle feed ratio is in the range of 20:1 to 30:1.
Claim 4
Dependent Claim
245 words
A process for manufacturing a toilet soap bar of improved cold water lathering properties, improved stability on storage and improved plasticity, which is mild to the skin and which does not slough excessively when deposited wet on a soap dish, which bar consists essentially of at least 70% of sodium soap of topped, distilled coco fatty acid, 4 to 14% of such topped, distilled free coco fatty acid, 6 to 16% of water and no more than 8% of adjuvant(s), which comprises pre-heating an aqueous solution of sodium hydroxide, brine and topped, distilled coco fatty acid, separately feeding the pre-heated sodium hydroxide solution, brine and coco fatty acid to a proportioning pump, feeding the discharge from the pump to a manifold and thence to a shear pump, in which the sodium hydroxide and coco fatty acid are intimately mixed and reacted in the presence of the brine, after which the reaction mixture resulting is passed through an in-line static mixer to an autoclave for further reaction, and a high proportion of the saponification mixture resulting is recycled to the autoclave to saponify 85 to 94% of the coco fatty acid, with the balance of the coco fatty acid being available as free coco fatty acid, drying the sodium coco soap--free coco fatty acid mixture to a moisture content in the range of 6 to 16%, mixing such drived soap--fatty acid mixture with no more than 8% of adjuvant(s) and plodding such mixture to bar form.
Claim 5
Dependent Claim
245 words
A process for manufacturing a toilet soap bar of improved cold water lathering properties, improved stability on storage and improved plasticity, which is mild to the skin and which does not slough excessively when deposited wet on a soap dish, which bar consists essentially of at least 70% of sodium soap of topped, distilled coco fatty acid, 4 to 14% of such topped, distilled free coco fatty acid, 6 to 16% of water and no more than 8% of adjuvant(s), which comprises pre-heating an aqueous solution of sodium hydroxide, brine and topped, distilled coco fatty acid, separately feeding the pre-heated sodium hydroxide solution, brine and coco fatty acid to a proportioning pump, feeding the discharge from the pump to a manifold and thence to a shear pump, in which the sodium hydroxide and coco fatty acid are intimately mixed and reacted in the presence of the brine, after which the reaction mixture resulting is passed through an in-line static mixer to an autoclave for further reaction, and a high proportion of the saponification mixture resulting is recycled to the autoclave to saponify 85 to 94% of the coco fatty acid, with the balance of the coco fatty acid being available as free coco fatty acid, drying the sodium coco soap--free coco fatty acid mixture to a moisture content in the range of 6 to 16%, mixing such drived soap--fatty acid mixture with no more than 8% of adjuvant(s) and plodding such mixture to bar form.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1991-08-30 | 1992-02-29 | 1992-08-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-08-30 | 1996-02-29 | 1996-08-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-08-30 | 2000-02-29 | 2000-08-30 | $7700.00 | Window Closed / Lapsed |