The present invention relates to the co-production and isolation of mycoprotein and ethanol from carbohydrate feedstock material (e.g cereals). The present invention also provides a fermentation system for the co-production of mycoprotein from a carbohydrate feedstock material.

A process for obtaining high ethanol yield from the fermentation of an energy crop and for producing a nutritionally enhanced feed co-product is provided. In particular, the process includes converting non-fermentable polysaccharides in an energy crop into fermentable sugar. The fermentable sugars may be fermented into ethanol thereby enhancing the ethanol yield. In addition, separation of ethanol from the fermentation product yields a whole stillage product having enhanced protein content and reduced fiber content. The process requires little or no modification to the configuration of existing commercial ethanol facilities.

A process for obtaining high ethanol yield from the fermentation of an energy crop and for producing a nutritionally enhanced feed co-product is provided. In particular, the process includes converting non-fermentable polysaccharides in an energy crop into fermentable sugar. The fermentable sugars may be fermented into ethanol thereby enhancing the ethanol yield. In addition, separation of ethanol from the fermentation product yields a whole stillage product having enhanced protein content and reduced fiber content. The process requires little or no modification to the configuration of existing commercial ethanol facilities.

A method for obtaining a food product from a wet mass of waste materials arising from production processes for producing products like beer, whisky, vodka, gin, tequila, liqueurs or citrus-fruit based distillates, cider, sake, soy sauce is provided. An enzyme is added to the waste materials that is suitable for breaking down possible gluten residues in the materials and making the enzyme act for a period between 15 and 30 minutes. The waste materials are boiled for at least 20 minutes. The waste materials are cooled and centrifuged to eliminate most of the water present in the waste materials. The materials are dried at a temperature between 70° C. and 100° C. for a time between 60 and 120 minutes, by a radio frequency dryer so as to obtain, at the end of drying, a product with relative humidity between 14 and 2%. A food product is provided that includes a percentage by weight between 1% and 60% of at least one flour obtainable from waste materials arising from the production processes for producing products like beer, whisky, vodka, gin, tequila, liqueurs or citrus-fruit based distillates, cider, sake, soy sauce, and at least one cereal flour, or vegetable flour, or animal flour, in a percentage by weight between 40% and 99%.

The present technology relates to processes of fermenting a starch-containing material into a fermentation product comprising a fermentation step in the presence of a xylanase in combination with a pectinase on oil partitioning during post-fermentation processing. In particular, the enzyme(s) were added during simultaneous saccharification and fermentation. The finished beer was subjected to beer well incubation, distillation, and then decanting to separate thin stillage from the solids.

The present invention relates to dissolvable containers for animal feed micro-ingredients, and methods for using such dissolvable containers to prepare an animal feed mixture. Ingredients required in very small amounts with respect to the rest of the components in an animal feed, i.e., micro-ingredients, can be pre-measured and sealed within the dissolvable containers, which can be made from a water-soluble polymer film, then added to the other feed components when the complete animal feed is being prepared.

The present invention relates to dissolvable containers for animal feed micro-ingredients, and methods for using such dissolvable containers to prepare an animal feed mixture. Ingredients required in very small amounts with respect to the rest of the components in an animal feed, i.e., micro-ingredients, can be pre-measured and sealed within the dissolvable containers, which can be made from a water-soluble polymer film, then added to the other feed components when the complete animal feed is being prepared.

Insect feeds comprising a derivative of corn steep liquid are disclosed. Methods of feeding such insect feeds to insects such as bees, are further disclosed. In each of its various embodiments, the present invention fulfills these needs and discloses improved feeds to be fed to bees and other insects. In one embodiment, the insect feed comprises a derivative of corn steep liquid. The derivative of the corn steep liquid may be selected from the group consisting of a product derived from fermentation using media comprising a corn steep liquid, solids derived from a com steeping process, gluten water, corn steep liquor, grain distillers dried yeast, a microbial biomass, and combinations of any thereof.

Insect feeds comprising a derivative of corn steep liquid are disclosed. Methods of feeding such insect feeds to insects such as bees, are further disclosed. In each of its various embodiments, the present invention fulfills these needs and discloses improved feeds to be fed to bees and other insects. In one embodiment, the insect feed comprises a derivative of corn steep liquid. The derivative of the corn steep liquid may be selected from the group consisting of a product derived from fermentation using media comprising a corn steep liquid, solids derived from a com steeping process, gluten water, corn steep liquor, grain distillers dried yeast, a microbial biomass, and combinations of any thereof.

The present technology generally relates to food-processing industry, namely to a method of processing brewer's grains. The invention enables to increase the level of extracted food fractions of brewer's grains up to 90-95% and to increase protein content in barley protein concentrate up to 50-65% wt (dry solid). The method implies that brewer's grains are subject to loosening by means of a vibrating screen, grinding in a colloid mill with addition of water or centrate in the ratio from 0.5:1 to 1:1 to brewer's grains in order to produce a pasty homogeneous mass from brewer's grains; and then this mass is subject to processing by means of a screw extractor for its further grinding and division into 2 factions: suspension with the humidity level of 90-95%, and ground husk of brewer's grains with the humidity level of 60-75% suitable for its further industrial use. Then the suspension is supplied to mechanical filtration in order to remove the ground husk, pumped into the container and dried in order to obtain the humidity level of max. 7%.