Abstract: An enzyme resistant starch type III having a melting point or endothermic peak of at least about 140° C. as determined by differential scanning calorimetry (DSC) is produced in yields of at least about 25% by weight, based upon the weight of the original starch ingredient. A gelatinization stage, nucleation/propagation stage, and preferably a heat-treatment stage are used to produce reduced calorie starch-based compositions which contain the enzyme resistant starch type III. The high melting point of the enzyme resistant starch permits its use in baked good formulations without substantial loss of enzyme resistance upon baking. A gelatinized, starch-based bulking agent having at least 30% by weight of the enzyme-resistant starch may be used in bar-type, extruded, sheeted, or rotary molded food products. The melting enthalpy of the bulking agent may be from about 0.5 to about 4 Joules/g and its water-holding capacity may be less than 3 grams.

Abstract: The present invention is directed to an edible, bakeable moisture barrier composition that is effective for reducing moisture migration between food components. The moisture barrier includes at least one crystalline carbohydrate, a highly crystalline fat and a crystalline food fiber.

Abstract: An extruded, directly expanded, high fiber reduced calorie food product, such as a ready-to-eat (RTE) cereal or sweet or savory snack, is produced at high production rates without substantial loss of extrusion functionality and extrudability by replacing a substantial portion of at least one flour with a gelatinized, enzyme-resistant starch type III ingredient or bulking agent as a reduced-calorie, high fiber flour replacer. The resistant starch type III ingredient or bulking agent contains an enzyme-resistant starch type III having a melting point with an endothermic peak temperature of at least about 140° C., and may have a water-holding capacity of less than 3 grams water per gram of the starch-based bulking agent. The total dietary fiber retention of the gelatinized, starch-based bulking agent may be at least about 90% by weight after the extrusion using a die temperature of least about 100° C., and a die pressure of at least about 150 psig.

Abstract: Methods for providing cooked rice with enhanced levels of fiber, wherein the fiber-containing cooked rice is suitable and especially adapted for use in preparing fiber-containing rice-based cereal products and especially for preparing fiber-containing puffed rice-based cereal products, are provided.

Abstract: Low-carbohydrate compositions derived from mixtures of sugar alcohols are described herein. The compositions of the present invention advantageously maintain a sufficiently high glass transition temperature useful for avoiding cold flow. The food products herein generally retain pleasing organoleptic properties and may be used with any number of snack bars, including nut and/or seed snack bars.

Abstract: The present invention is directed to an edible, bakeable moisture barrier composition that is effective for reducing moisture migration between food components. The moisture barrier includes at least one crystalline carbohydrate, a highly crystalline fat and a crystalline food fiber.

Abstract: An enzyme resistant starch type III which has a melting point or endothermic peak of at least about 140° C. as determined by differential scanning calorimetry (DSC) is produced in yields of at least about 25% by weight, based upon the weight of the original starch ingredient. A gelatinization stage, nucleation/propagation stage, and preferably a heat-treatment stage are used to produce reduced calorie starch-based compositions which contain the enzyme resistant starch type III. The enzyme resistant starch is produced using crystal nucleation and propagation temperatures which avoid substantial production of lower melting amylopectin crystals, lower melting amylose crystals, and lower melting amylose-lipid complexes. The nucleating temperature used is above the melting point of amylopectin crystals. The propagating temperature used is above the melting point of any amylose-lipid complexes but below the melting point of the enzyme resistant starch.

Abstract: An enzyme resistant starch type III which has a melting point or endothermic peak of at least about 140° C. as determined by differential scanning calorimetry (DSC) is produced in yields of at least about 25% by weight, based upon the weight of the original starch ingredient. A gelatinization stage, nucleation/propagation stage, and preferably a heat-treatment stage are used to produce reduced calorie starch-based compositions which contain the enzyme resistant starch type III. The high melting point of the enzyme resistant starch permits its use in baked good formulations without substantial loss of enzyme resistance upon baking. Agelatinezed, starch-based bulking agent having at least 30% by weight of the enzyme-resistant starch may be used in bar-type, extruded, sheeted, or rotary molded food products. The melting enthalypy of the bulking agent may be from about 0.5 to about 4 Joules/g and its water-holding capacity may be less than 3 grams.

Abstract: An enzyme resistant starch type III which has a melting point or endothermic peak of at least about 140° C. as determined by differential scanning calorimetry (DSC) is produced in yields of at least about 25% by weight, based upon the weight of the original starch ingredient. A gelatinization stage, nucleation/propagation stage, and preferably a heat-treatment stage are used to produce reduced calorie starch-based compositions which contain the enzyme resistant starch type III. The enzyme resistant starch is produced calf using crystal nucleation and propagation temperatures which avoid substantial production of lower melting amylopectin crystals, lower melting amylose crystals, and lower melting amylose-lipid complexes. The nucleating temperature used is above the melting point of e amylopectin crystals. The propagating temperature used is above the melting point of any amylose-lipid complexes but below the melting point of the enzyme resistant starch.

Abstract: An enzyme resistant starch type III which has a melting point or endothermic peak of at least about 140° C. as determined by differential scanning calorimetry (DSC) is produced in yields of at least about 25% by weight, based upon the weight of the original starch ingredient. A gelatinization stage, nucleation/propagation stage, and preferably a heat-treatment stage are used to produce reduced calorie starch-based compositions which contain the enzyme resistant starch type III. The enzyme resistant starch is produced using crystal nucleation and propagation temperatures which avoid substantial production of lower melting amylopectin crystals, lower melting amylose crystals, and lower melting amylose-lipid complexes. The nucleating temperature used is above the melting point of amylopectin crystals. The propagating temperature used is above the melting point of any amylose-lipid complexes but below the melting point of the enzyme resistant starch.

Abstract: An enzyme resistant starch type III which has a melting point or endothermic peak of at least about 140.degree. C. as determined by differential scanning calorimetry (DSC) is produced in yields of at least about 25% by weight, based upon the weight of the original starch ingredient. A gelatinization stage, nucleation/propagation stage, and preferably a heat-treatment stage are used to produce reduced calorie starch-based compositions which contain the enzyme resistant starch type III. The enzyme resistant starch is produced using crystal nucleation and propagation temperatures which avoid substantial production of lower melting amylopectin crystals, lower melting amylose crystals, and lower melting amylose-lipid complexes. The nucleating temperature used is above the melting point of amylopectin crystals. The propagating temperature used is above the melting point of any amylose-lipid complexes but below the melting point of the enzyme resistant starch.

Abstract: The stack height and moisture content of baked goods produced continuously in a multi-zone oven, such as a gas-fired band oven, is controlled and adjusted using microwave energy. Color development, flavor development, texture, and appearance of the baked products are not adversely affected by the replacement of a substantial amount of the non-microwave energy input with microwave energy. The stack height and moisture content of the baked product may be controlled or adjusted with the microwave energy to be within predetermined ranges or specifications independently of each other. Upon detection of product which is not within specifications, the microwave energy may be used to rapidly adjust stack height and/or moisture content so that they quickly return to their predetermined acceptable levels thereby substantially reducing product waste or recycling. The stack height of the baked pieces is controlled and adjusted using microwave energy early in the baking process.