Abstract: Described herein is a corn protein concentrate comprising 55%-80% corn protein on a dry basis, an a* color value between about 0 and 4, and a b* color value between about 15 and 3, and less than about 2% oil on a dry basis; and a method of manufacturing the same.

Abstract: Aspects of the present invention provide a corn protein isolate, comprising at least about 85 wt % corn protein on a dry basis; an “a*” color value ranging from about ?0.5 and 1.5, and a “b” color value ranging from about 10 and 25; and less than about 1.5% oil on a dry basis. Further aspects include methods of making the same.

Abstract: Aspects of the present invention provide a corn protein isolate, comprising at least about 85 wt % corn protein on a dry basis; an “a*” color value ranging from about ?0.5 and 1.5, and a “b” color value ranging from about 10 and 25; and less than about 1.5% oil on a dry basis. Further aspects include methods of making the same.

Abstract: Disclosed herein is a method of maintaining corn protein yield during extraction and managing stickiness and viscosity comprising obtaining a corn material having a corn protein content and washing the corn material to remove non-protein components with an ethanol-water solvent comprising at least 85 wt % ethanol to obtain a corn protein isolate, wherein the loss of corn protein content during extraction is less than 10% of total corn protein.

Abstract: Described herein is a food product and methods of manufacturing the same, comprising a corn protein isolate or corn protein concentrate and a polysaccharide; wherein the food product has a density ranging from about 40 g/L to about 350 g/L.

Abstract: A method of preparing a refined zein-enriched protein hydrolysate composition and/or a refined zein-depleted protein hydrolysate composition comprising enzymatically hydrolyzing a refined zein-enriched protein composition and/or a refined zein-depleted protein composition that have been separated from a refined, destarched corn gluten meal. The refined zein-enriched protein hydrolysate composition has a protein solubility of from about 15% to about 20% at a pH selected from the group consisting of pH 3.4, pH 7.0, and of both pH 3.4 and pH 7.0. The refined zein-depleted protein hydrolysate composition has a protein solubility of from about 20% to about 35% at a pH selected from the group consisting of pH 3.4, pH 7.0, and of both pH 3.4 and pH 7.0. Alternatively, the refined zein-enriched protein composition and/or the refined zein-depleted protein composition have been separated from a corn protein isolate as described herein. Compositions are also provided.

Abstract: Described herein is a corn protein product comprising greater than about 20% corn protein on a dry weight basis and a free sulfite concentration of less than 150 ppm on an as-is basis. Also disclosed herein is a method to obtain this corn protein product including the steps of providing a protein-rich stream derived from a wet corn milling operation, wherein the protein-rich stream comprises greater than 20% corn protein on a dry weight basis, and treating the protein-rich stream with an oxidant, preferably hydrogen peroxide.

Abstract: Described herein is as method of reducing fumonisin in a corn protein product, comprising adjusting the pH of the corn protein product to a range between about 5.75 and about 7.5 to reduce fumonisin by at least 70%. The method can further comprise the addition of a divalent cationic salt.

Abstract: Described herein is a corn protein product comprising greater than about 20% corn protein on a dry weight basis and a free sulfite concentration of less than 150 ppm on an as-is basis. Also disclosed herein is a method to obtain this corn protein product including the steps of providing a protein-rich stream derived from a wet corn milling operation, wherein the protein-rich stream comprises greater than 20% corn protein on a dry weight basis, and treating the protein-rich stream with an oxidant, preferably hydrogen peroxide.

Abstract: A composition and method of preparing a corn protein hydrolysate includes obtaining a corn protein composition having a corn protein concentration of at least about 75 wt %, adding an enzyme to a corn protein suspension containing the corn protein composition at a ratio of from about 1:100 to about 1:20 by weight of enzyme to corn protein, controlling the pH and temperature of the corn protein suspension to hydrolyze the corn protein, and terminating the hydrolysis of the corn protein to provide a corn protein hydrolysate that has solubility of from about 7% to about 37% at a pH selected from the group consisting of pH 7.0, pH 3.4, pH 5, and all of pH 7.0, pH 5, and pH 3.4. The corn protein hydrolysate can be used in a variety of food, feed, beverage, and other applications.

Abstract: Described herein is a corn protein product, comprising a first fraction comprising 75 wt % to 95 wt % (dry solids) protein and a second fraction comprising 60 wt % to 80 wt % (dry solids) protein, wherein the first fraction is a zein-enriched fraction and the second fraction is a zein-depleted fraction and a method of achieving the same. Further described herein is a corn protein product derived from destarched corn gluten meal comprising a first fraction comprising 78 wt % to 83 wt % (dry solids) protein and a second fraction comprising 70 wt % to 80 wt % (dry solids) protein, wherein the first fraction is a zein-enriched fraction and the second fraction is a zein-depleted fraction.

Abstract: Described herein is a food product and methods of manufacturing the same, comprising a corn protein isolate or corn protein concentrate and a polysaccharide; wherein the food product has a density ranging from about 40 g/L to about 350 g/L.

Abstract: Described herein is as method of reducing fumonisin in a corn protein product, comprising adjusting the pH of the corn protein product to a range between about 5.75 and about 7.5 to reduce fumonisin by at least 70%. The method can further comprise the addition of a divalent cationic salt.

Abstract: Disclosed herein is a method of maintaining corn protein yield during extraction and managing stickiness and viscosity comprising obtaining a corn material having a corn protein content and washing the corn material to remove non-protein components with an ethanol-water solvent comprising at least 85 wt % ethanol to obtain a corn protein isolate, wherein the loss of corn protein content during extraction is less than 10% of total corn protein.

Abstract: Described herein is a corn protein concentrate comprising 55%-80% corn protein on a dry basis, an a* color value between about 0 and 4, and a b* color value between about 15 and 3, and less than about 2% oil on a dry basis; and a method of manufacturing the same.

Abstract: Described herein is a corn protein product comprising greater than about 20% corn protein on a dry weight basis and a free sulfite concentration of less than 150 ppm on an as-is basis. Also disclosed herein is a method to obtain this corn protein product including the steps of providing a protein-rich stream derived from a wet corn milling operation, wherein the protein-rich stream comprises greater than 20% corn protein on a dry weight basis, and treating the protein-rich stream with an oxidant, preferably hydrogen peroxide.

Abstract: Aspects of the present invention provide a corn protein isolate, comprising at least about 85 wt % corn protein on a dry basis; an “a*” color value ranging from about ?0.5 and 1.5, and a “b” color value ranging from about 10 and 25; and less than about 1.5% oil on a dry basis. Further aspects include methods of making the same.

Abstract: A method for preparation of an acidic stabilized syrup concentrate containing rebaudioside B and a stabilizer additive. Acidic stabilized syrup concentrate compositions are also provided.

Abstract: The present disclosure relates to protein-starch compositions. The disclosure also relates to processes for preparing the protein-starch compositions. Further, the disclosure relates to uses of the protein-starch compositions in the preparation of adhesives or binders. Further, the disclosure relates to adhesive formulations that include protein-starch containing compositions and to paper products resulting from the processes herein.

Abstract: Methods and systems for increasing the production of monatin in a multi-step equilibrium pathway are described. Tryptophan and pyruvate are added to a bioreactor to form a mixture comprising monatin and a plurality of intermediates via a multi-step equilibrium pathway. The methods and systems include operating the bioreactor such that a temperature of the mixture in the bioreactor is less than 25 degrees Celsius, resulting in an increased production of monatin. In some embodiments, the temperature of the mixture in the bioreactor is between about 5 degrees Celsius and about 23 degrees Celsius; in other embodiments, the temperature is between about 10 degrees Celsius and about 18 degrees Celsius.