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Purified, moderately esterified polyol polyester fatty acid compositions and synthesis thereof

A technology of polyol fatty acid and polyol polyester, applied in the field of esterification of purified polyol fatty acid polyester and high-purity polyol fatty acid polyester

Inactive Publication Date: 2007-04-18
PROCTER & GAMBLE CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The above applications often require higher purity and / or higher predictability

Method used

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  • Purified, moderately esterified polyol polyester fatty acid compositions and synthesis thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0161] In this example, the starting reaction mixture contained 750 g (0.314 moles) of sucrose polyester based on oleic acid fatty acid with a degree of esterification of 96%; 11.5 g (0.0336 moles) of sucrose; 10 g (0.072 moles) of potassium carbonate; and 200 g Dimethylformamide solvent. Sucrose and catalyst were dried in a vacuum oven for 12 hours before being used in the starting reaction mixture. The first step reaction product was formed by reacting the starting reaction mixture at 100°C for 300 minutes in a double-baffled glass reactor. The starting reaction mixture was reacted with stirring to ensure uniform heat distribution of the reaction components.

[0162] A sample of the first step reaction product was analyzed by supercritical fluid chromatography (SFC), and the resulting composition is shown in Table 1A, wherein SEX represents a sucrose ester with X esterified hydroxyl groups. A suitable superfluid chromatography method of analysis is described in US Patent 6...

Embodiment 2

[0167] In this example, the starting reaction mixture contained 750 g (0.314 moles) of sucrose polyester with a degree of esterification of 96%; 31.3 g (0.0916 moles) of sucrose; 10 g (0.072 moles) of potassium carbonate; and 300 g of dimethylsulfoxide solvent. The first step reaction product was formed by reacting the starting reaction mixture at 100°C for 300 minutes in a double-baffled glass reactor. The starting reaction mixture was reacted with stirring to ensure uniform heat distribution of the reaction components.

[0168] soap

sucrose

SE 1

SE 2

SE 3

SE 4

SE 5

SE 6

SE 7

SE 8

0.5

<0.1%

-

-

0.7

5.5

21.0

36.0

28.0

8.4

[0169] Table 2A

[0170] The first step reaction product has a degree of esterification of about 75%.

[0171]The first step reaction product was then purified with 109 g of deionized water. This water wash step was carried o...

Embodiment 3

[0176] In this example, the starting reaction mixture contained 750 g (0.314 moles) of sucrose polyester with a degree of esterification of 96%; 59.1 g (0.1727 moles) of sucrose; 10 g (0.072 moles) of potassium carbonate; and 300 g of dimethylsulfoxide solvent. The first step reaction product was formed by reacting the starting reaction mixture at 100°C for 300 minutes in a double-baffled glass reactor. The starting reaction mixture was reacted with stirring to ensure uniform heat distribution of the reaction components.

[0177] soap

sucrose

SE 1

SE 2

SE 3

SE 4

SE 5

SE 6

SE 7

SE 8

0.5

<0.1%

0.1

1.4

7.0

19.5

32.6

27.7

9.6

1.3

[0178] Table 3A

[0179] The first step reaction product has a degree of esterification of about 62%.

[0180] The first step reaction product was then purified with 170 g of deionized water. This water wash step was carr...

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Abstract

The present invention relates to processes for the preparation of a purified moderately esterified polyol fatty acid polyester composition and purified moderately esterified polyol fatty acid polyester compositions derived from such processes. Processes include the steps of: (a) forming an initial reaction mixture, said initial reaction mixture containing: a polyol portion; a highly esterified polyol fatty acid polyester; a solvent; and, a catalyst, wherein the molar ratio of said polyol portion to said highly esterified polyol polyester is chosen such that the final ratio of total fatty acid esters to total polyol backbones is in the range from about 3.2:1 to about 6.4:1; wherein the molar ratio of said catalyst to said highly esterified polyol polyester is in the range of from about 0.01:1 to about 10:1, and wherein the weight ratio of said solvent to the combined weight of said polyol portion, said highly esterified polyol polyester, and said catalyst is in the range of from about 0.01:1 to about 2:1; and (b) forming an initial reaction product by reacting said initial reaction mixture in an inert atmosphere, in the presence of a sufficient amount of agitation, for a period of time in the range of from about 30 minutes to about 6 hours, and at a temperature in the range of from about 80 DEG C to about 140 DEG C.

Description

Brief description of the invention [0001] The present invention relates to the preparation of moderately esterified polyol fatty acid polyesters. More specifically, the present invention relates to mildly esterified purified polyol fatty acid polyesters prepared by a process comprising water and alcohol based purification steps. Background of the invention [0002] Due to their physical properties, moderately esterified polyol fatty acid polyesters can be used as surfactants and / or lubricants in various detergent, textile, lubricant and / or cosmetic compositions . [0003] Currently, there are various techniques available in the art for the synthesis of these moderately esterified polyol fatty acid polyesters. US Patent 4,927,920 to Wagner et al. discloses the preparation of sugar esters with a degree of substitution of less than two by the reaction of a sugar, an organic solvent, and a sugar ester with a degree of substitution greater than two. Solvent recovery may be per...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07H13/06C08G63/00C07H13/02
CPCC07H13/02
Inventor J·J·谢菲尔
Owner PROCTER & GAMBLE CO
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