Synthesis of higher polyol fatty acid polyesters

Claim 2

A solvent-free, low temperature process for synthesizing polyol fatty acid polyesters consisting essentially of: 1. Heating a mixture of a polyol selected from the group consisting of monosaccharides, disaccharides and sugar alcohols, a fatty acid C 1-2 alkyl ester, an alkali metal fatty acid soap, and a basic catalyst selected from the group consisting of alkali metal, alloys of alkali metals, alkali metal hydrides and alkali metal alkoxides to a temperature of from about 110°C to about 180°C at a pressure of from about 0.1 mm of Hg to about 760 mm of Hg to form a homogenous melt of partially esterified polyol and unreacted starting materials; 2. Under the conditions of Step (1) adding excess fatty acid lower alkyl esters to the reaction product of Step (1) to form the polyol fatty acid polyester; and 3. Separating the polyol fatty acid polyester from the reaction product of Step (2).

Claim 3

A process according to claim 1 wherein the polyol is a disaccharide.

Claim 4

A process according to claim 1 wherein the polyol is selected from the group consisting of sucrose, xylitol, and sorbitol.

Claim 5

A process according to claim 1 wherein the temperature is from about 135°C to about 145°C.

Claim 6

A process according to claim 1 wherein the fatty acid C 1-2 alkyl esters are fatty acid methyl esters.

Claim 7

A process according to claim 5 wherein the methyl esters are derived from natural oils selected from the group consisting of soybean oil, sunflower oil, safflower oil and corn oil.

Claim 8

A process according to claim 1 wherein the catalyst is selected from the group consisting of potassium hydride, sodium hydride, a dispersion of potassium in sucrose octaester, a dispersion of potassium in mineral oil, potassium t-butoxide and sodium methoxide.

Claim 9

A solvent-free, low temperature process for synthesizing polyol fatty acid polyesters consisting essentially of: 1. Heating a mixture comprising (i) from about 10% to about 50% by weight of a polyol selected from the group consisting of monosaccharides, disaccharides and sugar alcohols, (ii) from about 40% to about 80% by weight of fatty acid C 1-2 alkyl esters, (iii) from about 1% to about 30% by weight of an alkali metal fatty acid soap, and (iv) from about 0.05% to about 5% by weight of a basic catalyst selected from the group consisting of alkali metals, alloy of two or more alkali metals, alkali metal alkoxides, and alkali metal hydrides to a temperature from about 110°C to about 180°C at a pressure of from about 0.1 mm of Hg to about 760 mm of Hg to form a homogenous melt of partially esterified polyol and unreacted starting materials; 2. Under the conditions of Step (1) adding excess fatty acid C 1-2 alkyl esters to the reaction product of Step (1) to form the polyol fatty acid polyester; and 3. Separating the polyol fatty acid polyester from the reaction product of Step (2.).

Claim 10

A solvent-free, low temperature process for synthesizing polyol fatty acid polyesters consisting essentially of: 1. Heating a mixture comprising (i) from about 10% to about 50% by weight of a polyol selected from the group consisting of monosaccharides, disaccharides and sugar alcohols, (ii) from about 40% to about 80% by weight of fatty acid C 1-2 alkyl esters, (iii) from about 1% to about 30% by weight of an alkali metal fatty acid soap, and (iv) from about 0.05% to about 5% by weight of a basic catalyst selected from the group consisting of alkali metals, alloy of two or more alkali metals, alkali metal alkoxides, and alkali metal hydrides to a temperature from about 110°C to about 180°C at a pressure of from about 0.1 mm of Hg to about 760 mm of Hg to form a homogenous melt of partially esterified polyol and unreacted starting materials; 2. Under the conditions of Step (1) adding excess fatty acid C 1-2 alkyl esters to the reaction product of Step (1) to form the polyol fatty acid polyester; and 3. Separating the polyol fatty acid polyester from the reaction product of Step (2.).

Claim 11

A process according to claim 8 wherein the polyol is sucrose.

Claim 12

A solvent-free, low temperature process for synthesizing poly fatty polyesters consisting essentially of: 1. Heating a mixture of a fatty acid C 1-2 alkyl ester and an alkali metal hydroxide to a temperature of from about 100°C to about 140°C under atmospheric pressure to form an emulsion comprising from about 5% to about 30%, by weight, of the corresponding alkali metal fatty acid soap and C 1-2 alkyl ester; 2. Adding to the reaction product of Step (1) from about 10% to about 50% by weight of a polyol and from about 0.05% to about 5% by weight of a basic catalyst selected from the group consisting of alkali metals, alloys of two or more alkali metals, alkali metal alkoxides, and alkali metal hydrides to form a heterogenous mixture; 3. Heating the heterogenous mixture formed in Step (2) to a temperature of from about 110°C to about 180°C under a pressure of from about 0.1 mm Hg to about 760 mm Hg to form a homogeneous melt of partially esterified polyol and unreacted starting materials; 4. Under the conditions of Step (3), adding excess fatty acid C 1-2 alkyl esters to the reaction product ot Step ( 3) to form the polyol fatty acid polyester; and 5. Separating the polyol fatty acid polyester from the reaction mixture.

Claim 13

A solvent-free, low temperature process for synthesizing poly fatty polyesters consisting essentially of: 1. Heating a mixture of a fatty acid C 1-2 alkyl ester and an alkali metal hydroxide to a temperature of from about 100°C to about 140°C under atmospheric pressure to form an emulsion comprising from about 5% to about 30%, by weight, of the corresponding alkali metal fatty acid soap and C 1-2 alkyl ester; 2. Adding to the reaction product of Step (1) from about 10% to about 50% by weight of a polyol and from about 0.05% to about 5% by weight of a basic catalyst selected from the group consisting of alkali metals, alloys of two or more alkali metals, alkali metal alkoxides, and alkali metal hydrides to form a heterogenous mixture; 3. Heating the heterogenous mixture formed in Step (2) to a temperature of from about 110°C to about 180°C under a pressure of from about 0.1 mm Hg to about 760 mm Hg to form a homogeneous melt of partially esterified polyol and unreacted starting materials; 4. Under the conditions of Step (3), adding excess fatty acid C 1-2 alkyl esters to the reaction product ot Step ( 3) to form the polyol fatty acid polyester; and 5. Separating the polyol fatty acid polyester from the reaction mixture.

Claim 14

A process according to claim 10 wherein the alkali metal hydroxide is potassium hydroxide.

Claim 15

A process according to claim 10 wherein the polyol is sucrose.

Claim 16

A process according to claim 10 wherein the fatty acid C 1-2 alkyl esters are fatty acid methyl esters derived from natural oils selected from the group consisting of soybean oil, sunflower oil, safflower oil, and corn oil.