Patent classifications
A23L29/35
A COMPOSITION SUITABLE FOR THE REPLACEMENT OF GLUCOSE-SYRUP
The invention relates to a glucose(-containing) syrup replacement composition for use in food applications, such as in bakery, beverages, ice cream, confectionery and the like. The glucose(-containing) syrup replacement composition comprises at least 80 wt % of maltodextrin having a dextrose equivalence (DE) of from 15 to 20 and up to 20 wt % of sorbitol and glycerol. The invention also covers the use of the composition in a food product to replace at least partially or completely nutritive mono- and disaccharides having an energy density of 4 kcal/g, preferably to replace at least partially or completely glucose, sucrose and/or fructose, generally in the form of syrups.
FOOD PRODUCT WITH REDUCED SUGAR GRAIN BINDER COMPOSITION
A method for preparing a food product and a food product thereof including a grain-based binder and being essentially free of added sugar. The method includes preparing or providing a cooked and/or pre-gelatinized grain flour, coating the grain flour with a fat or oil, and then hydrating the fat coated grain flour with at least one liquid to form a binder composition. The binder composition and one or more dry food ingredients are combined to form an agglomerate, and the agglomerate is thermally processed to activate the binder composition and to obtain the food product.
CORN SWEET STEEPING
Described is a process for releasing soluble starch hydrolysates or hydrolysed starch syrup from substantially intact corn kernels during high temperature steeping at a temperature at or above the gelatinization temperature of starch in the corn kernels, and the recovery of protein and oil-enhanced, carbohydrate-depleted residuals that are ideally suited for use as high quality animal feed or other food-grade products.
Process for sugar modulation
The present invention relates to a method for producing a food product comprising hydrolysed starch, as well as to products obtainable by the method. The method has the advantage of reducing the amount of sugar (i.e. maltose) produced by hydrolysis as compared to conventional methods of starch hydrolysis and present the additional advantage of providing good processability for the food product.
Barley protein production process
A process to produce a protein concentrate from grain, specifically barley protein concentrate (BPC) through mechanical and biochemical intervention while producing multiple sugar streams as co-products. The resulting BPC preferably contains 54%-95% protein derived exclusively from the enzymatically processed barley and has a pH>5.0. The BPC may contain approximately 10% oil, less than 5% crude fiber, less than 1% residual glucose, and less than 0.5% phytic acid. The BPC contains no ethanol, organic acid, fermentation products, or microbial cells or cell mass. No fermentation occurs in the production of the BPC. The BPC has unique applications in formulations for aquaculture or livestock feed, and other pet food as well as for food formulations intended for human consumption. The sugar co-products, including glucose, have applications in industry and science and are particularly suitable for use as feedstocks for fermentation processes, livestock feeds, or biochemical conversion processes.
Oral cannabinoid delivery formulations with mouthfeel experience enhancers
Oral formulations comprising at least one cannabinoid and at least one mouthfeel experience enhancer are described. For example, methods and materials for preparing a dissolvable lozenge comprising a combination of THC and CBD and Szechuan peppercorn or an extract thereof are provided.
Pelletized colorants comprising a pigment-protein complex and food products including the same
According to embodiments, a dry powdered composition which may be reconstituted to provide a gelatin product includes powdered gelatin and a pelletized colorant. The pelletized colorant includes a pigment-protein complex and at least one encapsulating agent for encapsulating the pigment-protein complex. The pelletized colorant has a rate of dissolution a rate of dissolution of less than 2 grams/minute in water having an initial temperature of from about 95° C. to about 100° C. Methods of making food products with the pelletized colorant are also disclosed. In embodiments, when the food products are measured on the L*a*b* color space, the food products have an L* value of about 49 to about 57, an a* value of about −10 to about −16, and a b* value of from about −11 to about −20.5.
SYSTEM AND METHOD FOR PRODUCING A SUGAR STREAM
An improved dry grind system and method for producing a sugar stream from grains or similar carbohydrate sources and/or residues, such as for biochemical production. In particular, after saccharification and prior to a sugar conversion process, a sugar/carbohydrate stream is removed from a saccharified stream. The sugar/carbohydrate stream includes a desired Dextrose Equivalent (DE) where DE describes the degree of conversion of starch to dextrose can be produced, with the such sugar stream being available for biochemical production, e.g., alcohol production, or other processes. In addition, the systems and methods also can involve the removal of certain grain components, e.g., corn kernel components, including protein and/or fiber. Sugar stream production occurs on the front end of the system and method.
Highly soluble Stevia sweetener
A method for making highly soluble Stevia sweetener compositions is described. The resulting sweetener compositions readily provide high concentration solutions, and also possess superior taste qualities. The compositions can be used as sweeteners, sweetness enhancers, and flavor enhancers in foods, beverages, cosmetics and pharmaceuticals.
Dual-spray reduced sugar coating system and method
A system and method for applying a reduced sugar coating to a food product is provided. The system uses separate applications (simultaneous or sequential) of a non-sucrose carbohydrate syrup from a first applicator and a sucrose syrup from a second applicator. The dual applications of the syrups are applied without an active drying step between applications. The process results in a coated food product with reduced clumping and a desired crystallized appearance even with the reduced levels of sugar.