Production of surface active material

Claim 2

A process for the preparation of a surface active material comprising reacting solid particulate sucrose with at least one alkyl ester of a fatty acid having 1 to 6 carbon atoms in the alkyl moiety and at least 8 carbon atoms in the fatty acid moiety, in the presence of a basic trans-esterification catalyst, at a temperature from 110° to 140° C., at atmospheric pressure without intentionally distilling alcohol by-product and in the absence of any solvent.

Claim 3

A process according to claim 1 in which the fatty acid ester has a fatty acid moiety with 10 to 22 carbon atoms.

Claim 4

A process according to claim 1 in which the fatty acid ester has a fatty acid moiety with 16 to 18 carbon atoms, in which the catalyst is used at a concentration of 5 to 12%, in which the temperature is about 125° C., and in which the sucrose is of a particle size less than 250 microns.

Claim 5

A process according to claim 1 in which the alkyl fatty acid ester is a mixed ester derived from a naturally occurring mixture of triglycerides.

Claim 6

A process according to claim 1 in which the alkyl moiety of the ester is a methyl group.

Claim 7

A process according to claim 1 in which the basic catalyst is selected from the group consisting of alkali metal carbonates and alkoxides and is present as at least 2% of the reaction mixture.

Claim 8

A process according to claim 6 effected at a temperature of 120° to 130° C.

Claim 9

A process according to claim 1 effected with high-shear mixing.

Claim 10

A process according to claim 1 effected in the presence of a surfactant selected from the group consisting of (a) a previously prepared product of the process or the same process using a triglyceride in place of the alkyl ester; (b) a diglyceride; and (c) a monoglyceride.

Claim 11

A process according to claim 9 in which the surfactant is present at a concentration of 5 to 10% by weight.

Claim 12

A process for the purification of the reaction product obtained after reacting solid particulate sucrose with at least one alkyl ester of a fatty acid having 1 to 6 carbon atoms in the alkyl moiety and at least 8 carbon atoms in the fatty acid moiety, in the presence of a basic trans-esterification catalyst, at a temperature from 110° to 140° C., at atmospheric pressure, without intentionally distilling alcohol by-product and in the absence of any solvent, comprising (a) treating the crude reaction product with an aqueous salt of a metal capable of forming an insoluble salt (soap) with a fatty acid, and separating the insoluble material; (b) extracting the separated insoluble material with an organic solvent in which lower alkyl esters of fatty acids are soluble but sucrose mono- and di-esters are substantially insoluble; and (c) extracting the insoluble residue from (b) with a polar solvent for sucrose mono- and di-esters, but in which fatty acid soaps are substantially insoluble.

Claim 13

A process for the purification of the reaction product obtained after reacting solid particulate sucrose with at least one alkyl ester of a fatty acid having 1 to 6 carbon atoms in the alkyl moiety and at least 8 carbon atoms in the fatty acid moiety, in the presence of a basic trans-esterification catalyst, at a temperature from 110° to 140° C., at atmospheric pressure, without intentionally distilling alcohol by-product and in the absence of any solvent, comprising (a) treating the crude reaction product with an aqueous salt of a metal capable of forming an insoluble salt (soap) with a fatty acid, and separating the insoluble material; (b) extracting the separated insoluble material with an organic solvent in which lower alkyl esters of fatty acids are soluble but sucrose mono- and di-esters are substantially insoluble; and (c) extracting the insoluble residue from (b) with a polar solvent for sucrose mono- and di-esters, but in which fatty acid soaps are substantially insoluble.

Claim 14

A process according to claim 11 in which the aqueous salt used is a salt of a Group 2 metal and in which the solvent in step (b) is a ketone or an ester and the solvent in step (c) is a lower alcohol with 1 to 4 carbon atoms.

Claim 15

A process according to claim 12 in which the salt is a calcium salt.

Claim 16

A process according to claim 11 in which the slurry obtained in step (a) is gently stirred at a moderately elevated temperature before separation.

Claim 17

A process according to claim 12 in which the solvent in step (b) is selected from the group consisting of acetone, methyl ethyl ketone and ethyl acetate and in step (c) is selected from the group consisting of ethanol and isopropanol.

Claim 18

A process for the preparation of a surface active material comprising reacting solid particulate sucrose with at least one alkyl ester of a fatty acid having 1 to 6 carbon atoms in the alkyl moiety and 16 to 18 carbon atoms in the fatty acid moiety, in the presence of a basic trans-esterification catalyst at a temperature of about 120° to about 130° C. at atmospheric pressure, without intentionally distilling alcohol by-product and in the absence of any solvent; the reaction being effected in the presence of a surfactant selected from (a) a previously prepared product of the process or of the same process using a triglyceride instead of the alkyl ester; (b) a diglyceride; or (c) a monoglyceride; and then purifying the reaction product by (a) treating the crude reaction product with an aqueous salt of a Group 2 metal selected from the group consisting of calcium, magnesium, barium and zinc and separating the insoluble material from the slurry so formed; (b) extracting the separated insoluble material with an organic solvent selected from the group consisting of ketone and ester solvents to remove lower alkyl esters of fatty acids and leave an insoluble residue; and (c) extracting the insoluble residue from step (b) with a polar solvent selected from the group consisting of lower alcohols with 1 to 4 carbon atoms and evaporating the extract to dryness.

Claim 19

A process for the preparation of a surface active material comprising reacting solid particulate sucrose with at least one alkyl ester of a fatty acid having 1 to 6 carbon atoms in the alkyl moiety and 16 to 18 carbon atoms in the fatty acid moiety, in the presence of a basic trans-esterification catalyst at a temperature of about 120° to about 130° C. at atmospheric pressure, without intentionally distilling alcohol by-product and in the absence of any solvent; the reaction being effected in the presence of a surfactant selected from (a) a previously prepared product of the process or of the same process using a triglyceride instead of the alkyl ester; (b) a diglyceride; or (c) a monoglyceride; and then purifying the reaction product by (a) treating the crude reaction product with an aqueous salt of a Group 2 metal selected from the group consisting of calcium, magnesium, barium and zinc and separating the insoluble material from the slurry so formed; (b) extracting the separated insoluble material with an organic solvent selected from the group consisting of ketone and ester solvents to remove lower alkyl esters of fatty acids and leave an insoluble residue; and (c) extracting the insoluble residue from step (b) with a polar solvent selected from the group consisting of lower alcohols with 1 to 4 carbon atoms and evaporating the extract to dryness.