Abstract: The present invention relates to flavored confectionery compositions which comprise a flavor enhancing amount of a flavor component, from 25% to 45% of a fat component and from about 55 to about 75% other nonfat confectionery ingredients. The fat component of the flavored confectionery compositions of the present invention comprises at least about 70% of a reduced calorie fat, up to about 15% milkfat, up to about 20% cocoa butter and no more than about 4% diglycerides.The reduced calorie fat comprising the fat component of the chocolate confectionery compositions herein comprises mixtures of reduced calorie triglycerides which are enriched in long chain fatty acid 2-position isomers (MLM triglycerides). In particular, the reduced calorie fats utilized in the chocolate confectionery compositions herein comprise at least about 40% of the long chain fatty acid 2-position isomer.

Abstract: The present invention relates to an infusion product for making a beverage comprising an infusible material and a soluble additive material packaged in an infusion bag, wherein the soluble additive material comprises a co-agglomerate of a creamer base and a sweetener base. The present invention also relates to a process for making an infusion product comprising packaging an infusion material and a co-agglomerate of a creamer base and a sweetener base in an infusion bag. The present invention further relates to a method of preparing an individual serving of a beverage such as coffee, tea or the like, comprising immersing in a receptacle of hot water such an infusion product.

Abstract: The present invention relates to reduced calorie fats comprising mixtures of reduced calorie triglycerides which are enriched in long chain fatty acid 2-position isomers (MLM triglycerides). In particular, the reduced calorie fats comprise at least about 40% of the long chain fatty acid 2-position isomer. The reduced calorie fats according to the present invention further comprise at least about 85% combined MML and MLM triglycerides, no more than about 5% combined LLM and LML triglycerides, no more than about 2% LLL triglycerides, no more than about 4% MMM triglycerides and no more than about 6% other triglycerides; wherein M=fatty acids selected from the group consisting of C.sub.6 to C.sub.10 saturated fatty acids, and mixtures thereof, and L=fatty acids selected from the group consisting of C.sub.17 to C.sub.26 saturated fatty acids, and mixtures thereof. The reduced calorie fats of the present invention have the following fatty acid composition by weight percent:(a) from about 15% to about 70% C.sub.

Abstract: The present invention relates to a flavored instant coffee product comprising a creamer base, a sweetener base, and a flavor base, wherein the creamer base is agglomerated to the sweetener base, and the flavor base is coated on the agglomerated creamer and sweetener bases, and wherein the flavor base comprises instant coffee and flavorings. The present invention further relates to a process for making such a flavored instant coffee product.

Abstract: A fast, three-stage, low temperature process for the conversion of fatty acids into food grade-anhydrides is disclosed. The process comprises as a first step the reaction of a higher fatty acid with a dehydrating agent under mild conditions. A second process step comprises the further conversion of mixed anhydrides to symmetrical anhydrides by continuous removal of the dehydrating agent and by-product acid from the reaction mixture under vacuum. In a third process step, the symmetrical anhydrides are purified under mild conditions, preferably using thin-film short path evaporation. The resulting anhydrides have minimal by-products and good color and odor.

Abstract: Reduced calorie 1,2-propylene glycol diesters, where one ester group contains a medium chain C.sub.6 -C.sub.12 saturated fatty acid radicals(s), and where the other ester group contains a long chain C.sub.20 -C.sub.24 saturated fatty acid radical(s) are disclosed. These diesters are preferably obtained by the selective esterification of long chain saturated fatty acid monoesters of propylene glycol with the respective medium chain saturated fatty acids or anhydrides. Certain preferred diesters where the medium chain radicals are C.sub.8 and/or C.sub.10 radicals and where the long chain radicals are C.sub.20 and/or C.sub.22 radicals are particularly useful as reduced calorie cocoa butter substitutes and hard butters. Chocolate-flavored products formulated from these preferred diesters, when properly crystallized, are bloom resistant, even when subjected to thermal stress.

Abstract: A process for the selective esterification of long chain length fatty acid monoglycerides, particularly monobehenin, with medium chain length fatty acids, particularly a mixture of C.sub.8 and C.sub.10 saturated fatty acids, is disclosed. In this process, an at least about 60% pure C.sub.18 -C.sub.24 fatty acid monoglyceride or mixture thereof is esterified with an at least about 90% pure C.sub.6 -C.sub.10 fatty acid or mixture thereof at a temperature of from about 140.degree. to about 250.degree. C. in the substantial absence of an esterification catalyst. The mole ratio of fatty acid to monoglyceride used in this monoglyceride esterification is at least about 3:1. Water generated during this monoglyceride esterification is also continuously removed.

Abstract: A process for the selective esterification of long chain length fatty acid monoglycerides, particularly monobehenin, with medium chain length fatty acid anhdyrides, particularly a mixture of C.sub.8 and C.sub.10 saturated fatty acid anhdyrides is disclosed. In this process, an at least about 60% pure C.sub.18 -C.sub.24 fatty acid monoglyceride or mixture thereof is esterified with an at least about 50% pure C.sub.6 -C.sub.10 fatty acid anhydride or mixture thereof at a temperature of from about 90.degree. to aobut 190.degree. C. in the substantial absence of an esterificastion catalyst. The mole ratio of fatty acid anhydride to monoglyceride used in this monoglyceride esterification is at least about 2:1.

Abstract: Processes of the present invention provide economical methods for preparing derivatives 5-C-hydroxymethyl-D-aldohexose and their bicyclic anhydro tautomeric forms. The 5-C-hydroxymethylation process comprises an enzymic oxidation reaction followed by a condenation reaction with formaldehyde.

Abstract: Low viscosity orange juice concentrates which are useful in preparing high Brix concentrate products that are less pseudoplastic at freezer temperatures and are more highly dispersible when reconstituted with water are disclosed. These low viscosity orange juice concentrates are obtained by subjecting concentrated orange juice to high shear treatment for a period of time sufficient to reduce the mean particle of the sinking pulp at least about 40 microns and thus lower the viscosity of the concentrated juice. The mean particle size of the sinking pulp in these low viscosity orange juice concentrates is typically about 125 microns or less.

Abstract: A method for obtaining commercial feed juices having textural, aroma and flavor properties more like hand-squeezed orange juice is disclosed. This method involves gentle extraction of orange fruit with commercial juice extractors, gentle and quick removal of rag, seeds and peel from the extracted juice, substantially complete removal of sensible pulp, and removal of at least some of the sinking pulp. The feed juices obtained have a relatively low viscosity and sinking pulp level, minimized levels of peel oil and flavanoid glycosides and a relatively high ratio of more desirable orange compounds to less desirable orange compounds.

Abstract: A method for the direct condensation of gaseous food volatiles, such as coffee aroma, on a food substrate, such as coffee, at cryogenic temperatures. A bed of particulated solid substrate is placed in a vessel cooled by a cryogenic fluid such as liquid nitrogen. The substrate is fluidized to provide an adsorbent bed thereof. Gaseous aroma volatiles are then adsorbed onto the cooled and fluidized bed of substrate having a temperature preferably below -150.degree. F. The aromatized substrate formed is preferably equilibrated to insure uniformity of aromatization, binding of volatiles to the substrate and storage stability. The resultant aromatized substrate can then be added to unaromatized food material for aroma and/or flavor enhancement.