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.

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.

The present invention uses natural materials, namely corn protein concentrates, as bead materials, providing a greener solution to synthetic beads. The present invention further eliminates the need for solvents and other potentially environmentally dangerous chemicals by producing the beads directly from a corn protein concentrate cake.

The present invention uses natural materials, namely corn protein concentrates, as bead materials, providing a greener solution to synthetic beads. The present invention further eliminates the need for solvents and other potentially environmentally dangerous chemicals by producing the beads directly from a corn protein concentrate cake.

Described herein is a method of maintaining corn protein yield during extraction, comprising obtaining a corn gluten material, washing the corn gluten material to remove non-protein components with an ethanol-water solvent comprising at least 85 wt % ethanol to obtain a corn protein concentrate product, wherein the loss of corn protein content during extraction is less than 25% of total corn protein.

Described herein is a method of maintaining corn protein yield during extraction, comprising obtaining a corn gluten material, washing the corn gluten material to remove non-protein components with an ethanol-water solvent comprising at least 85 wt % ethanol to obtain a corn protein concentrate product, wherein the loss of corn protein content during extraction is less than 25% of total corn protein.

The present invention discloses novel phytases that have improved phytase activity, compositions comprising them, recombinant host cells suitable for their production, and their use in feed applications.

An enzyme system for the extraction of proteins from distillers grains and roots. The enzyme system is a three component system containing a first component of protease enzyme and a buffer, a second component comprised of a deactivating agent, and a third component comprised of neutralizing agent.

Systems and methods are provided for separating high value by-products, such as oil and/or germ, from grains used for alcohol production. In one embodiment, a method for separating by-products from grains used for alcohol production includes, subjecting milled grains to liquefaction to provide a liquefied starch solution including fiber, protein, and germ. The germ is separated from the liquefied starch solution. The separated germ is ground, e.g., to a particle size less than 50 microns, to release oil to provide a germ/oil mixture. Then, prior to fermentation, the oil is separated from the germ/oil mixture to yield an oil by-product. The pH of the germ/oil mixture can be adjusted to about 8 to about 10.5 and/or cell wall breaking enzymes or chemicals may be added to help release oil from the germ. In one example, the oil yield is greater than 1.0 lb/Bu.

Systems and methods are provided for separating high value by-products, such as oil and/or germ, from grains used for alcohol production. In one embodiment, a method for separating by-products from grains used for alcohol production includes, subjecting milled grains to liquefaction to provide a liquefied starch solution including fiber, protein, and germ. The germ is separated from the liquefied starch solution. The separated germ is ground, e.g., to a particle size less than 50 microns, to release oil to provide a germ/oil mixture. Then, prior to fermentation, the oil is separated from the germ/oil mixture to yield an oil by-product. The pH of the germ/oil mixture can be adjusted to about 8 to about 10.5 and/or cell wall breaking enzymes or chemicals may be added to help release oil from the germ. In one example, the oil yield is greater than 1.0 lb/Bu.