Abstract: A composition for confectionery applications, which comprises: a fat composition having a solid fat content (SFC) with an N20 of at least 10% and N35 of at most 10% measured on stabilized fat stabilized at 20° C. for 40 hours according to ISO 8292-1; at least one emulsifier; and at least one bitterness inhibitor dispersed or dissolved in the fat composition.

Abstract: A process of preparing a fat composition comprises the steps of: a) providing a fat, preferably from a single natural source, comprising at least 25% by weight of StOSt triglycerides based on the total glycerides present in the fat, wherein St is stearic acid and O is oleic acid; b) fractionating the fat source obtained in step a) to form a stearin fraction comprising at least 60% by weight of StOSt triglycerides based on the total glycerides present in the fat, wherein St is stearic acid and O is oleic acid; and c) blending the fat source obtained in step a) and the stearin fraction obtained in step b) in a weight ratio of from 90:10 to 10:90 to form a fat composition.

Abstract: A fat composition comprises: from 10% to 30% by weight of diglycerides; and from 70% to 90% by weight of triglycerides, wherein the triglycerides comprise from 40% to 75% by weight of CN50 triglycerides and from 15% to 40% by weight of CN52 triglycerides; based on total triglycerides present in the composition; and wherein the fat composition has from 55 to 85 solid fat content at 10° C.; and from 35 to 70 solid fat content at 20° C.; and from 5 to 25 solid fat content at 30° C.; and from 0 to 10 solid fat content at 40° C.; measured on 20° C. stabilized fat according to ISO 8292-1.

Abstract: The invention provides a non-trans, non-hydrogenated fat composition comprising less than 45 wt. % saturated fatty acids (SAFA) based on the total fatty acids in the composition, and a solid fat content (SFC) melting curve wherein the change in solid fat content from N35-N25 is at least 15 and wherein N35 is less than 3.

Abstract: Process for refining vegetable oil, to suppress the formation of monochloropropanediol esters (MCPDe) and reduce the content of glycidyl esters, comprising first and second refinement stages, wherein the first refinement stage comprises: a) providing a crude vegetable oil having a combined MCPDe and glycidyl ester content below 0.2 ppm; b) degumming the crude vegetable oil to produced degummed vegetable oil; c) bleaching of the degummed vegetable oil with activated bleaching earth under reduced pressure to yield bleached vegetable oil; d) adding a base to the bleached vegetable oil and subsequent stripping and deodorizing under reduced pressure at a temperature below 255° C. to yield an intermediate refined vegetable oil; and a second refinement stage comprising the steps of: e) bleaching of the intermediate refined vegetable oil using activated bleaching earth under reduced pressure to yield a bleached vegetable oil; and f) deodorizing at a temperature below 220° C.

Abstract: Process for refining vegetable oil, to suppress the formation of monochloropropanediol esters (MCPDe) and reduce the content of glycidyl esters, comprising first and second refinement stages, wherein the first refinement stage comprises the steps of: a) providing a crude vegetable oil having a combined MCPDe and glycidyl ester content below 0.2 ppm, preferably below 0.1 ppm; b) degumming the crude vegetable oil to produced degummed vegetable oil; c) bleaching of the degummed vegetable oil with activated bleaching earth under reduced pressure to yield bleached vegetable oil, preferably at a reduced pressure of 80-800 mbar; d) adding a base to the bleached vegetable oil and subsequent stripping and deodorizing under reduced pressure at a temperature below 255° C.

Abstract: The invention provides a non-trans, non-hydrogenated fat composition comprising less than 45 wt. % saturated fatty acids (SAFA) based on the total fatty acids in the composition, and a solid fat content (SFC) melting curve wherein the change in solid fat content from N35-N25 is at least 15 and wherein N35 is less than 3.

Abstract: A method of removing glycidyl esters from a vegetable oil comprises contacting the oil with at least 0.5% by weight of the oil of an acid-activated bleaching earth and deodorizing the oil at a temperature of less than 200° C. for a time of at least 30 minutes.

Abstract: A fat composition comprises: greater than 70% by weight palmitic acid present in glycerides; and from 2 to 25% by weight P2O triglycerides, wherein P is palmitic acid and O is oleic acid; wherein the fat composition has a weight ratio of SSO:SOS triglycerides of greater than 0.3, and wherein S is stearic or palmitic acid and O is oleic acid.

Abstract: A method of removing glycidyl esters from a vegetable oil comprises contacting the oil with at least 0.5% by weight of the oil of an acid-activated bleaching earth and deodorising the oil at a temperature of less than 200° C. for a time of at least 30 30 minutes.

Abstract: A method of producing a refined, bleached and deodorised vegetable oil comprises degumming a vegetable oil, bleaching the degummed oil and deodorising the bleached oil, wherein the degumming, bleaching and deodorising conditions are selected to reduce the content of 3-chloropropane-1,2-diol and esters thereof in the deodorised oil to less than 8 ppm.