The invention describes an apparatus for the desolventisation and toasting or an apparatus for the combined desolventisation, toasting, drying and cooling of a spent material, i.e., a solvent extraction residue obtained from the solvent extraction of oleaginous material. In particular, the invention describes desolventiser toaster or combined desolventiser toaster dryer cooler of improved design equipped with a side vapours outlet and optionally combined with at least one sieve stripping tray to allow nearly the full saturation of the outgoing vapours with hexane.

The present invention relates to a method for the manufacture of a processed, solid soya protein product derived from soya bean meal (SBM) which protein product comprises 65-75% protein by weight of dry matter, has a protein to potassium weight ratio of at least about 50:1 and a dry matter content of at least about 90%, which product is substantially free of sodium, and wherein at least about 65% by weight of the indigestible oligosaccharide content of the SBM wherefrom the protein is derived has been removed; the method comprises the following steps: 1) providing an initial mixture comprising milled or flaked or otherwise disintegrated soya bean meal (SBM) and water; 2) leaching the initial mixture under conditions where the dry matter amount in the initial mixture is between 8 and 20% by weight, for 0.15 to 6 hours at a temperature of 5 to 65 C. and at neutral pH; 3) separating the leaching mixture in a liquid fraction and a first solid fraction; 4) adjusting the pH of the liquid fraction from the initial leaching mixture with acid to a value of 3.5 to 5.5; 5) conveying the acidified liquid fraction through separation means such as a decanter centrifuge or similar means thereby separating the waste liquid and collecting a further solid fraction; 6) combining the solid fraction from the initial leaching mixture with the solid fraction collected from the separation means; 7) drying the combined solid fraction to a dry matter content of at least about 90%; 8) wherein the total amount of spent water in the method calculated from the initial SBM starting material is about 10 times the amount of SBM or less. It also relates to a processed, solid soya protein product derived from soya bean meal (SBM) which protein product comprises 65-75% protein by weight of dry matter, has a protein to potassium weight ratio of at least about 50:1 and a dry matter content of at least about 90%, which product is substantially free of sodium, and wherein at least about 65% by weight of the indigestible oligosaccharide content of the SBM wherefrom the protein is derived has been removed, and the use of such a product.

A method and system provides for for de-oiling and extracting protein from chickpeas prior to generating chickpea protein concentrate. The method and system includes receiving a chickpea flour generated from the chickpeas, including having cortex material removed from the chickpeas and generating an ethanol mixture by mixing the chickpea flour with ethanol to remove at least a portion of the oil content from the chickpea flour. The method and system includes separating the ethanol mixture into a de-oiled chickpea flour and an ethanol recycling stream having organics from the chickpea flour absorbed therein. Therein, the method and system includes extracting a protein concentrate from the de-oiled flour.

A dry fractionation method and system provides for generating a protein concentrate product therefrom. The method and system includes milling a plant-based flour to generate milled flour and generating a first protein concentrate from the milled flour using an air classifier. The method and system includes processing the first protein concentrate to generate a protein rich curd and generating a neutral hydrolyzed protein slurry by mixing the protein curd with a base, water and enzymatic cocktail. The method and system includes generating a homogenized protein slurry from the protein slurry and generating a cooled protein slurry by pasteurizing the homogenized protein slurry. Therein, the method and system provides for extracting the protein concentrate product from the cooled protein slurry.

A process for the production of soybean meal with a high content of soluble proteins in which a soybean meal with a content of soluble proteins in KOH in the range of 60 to 75% is reached, in which the soluble sugars are first removed from the soybean meal for extraction with aqueous ethanol solution and then the oil by extraction with hexane, without intermediate desolventization and in a single integrated industrial unit; an SPC soybean meal having 58-62% of a crude protein content; and 60-70% of soluble proteins in KOH.

An umami taste and/or flavor enhancing composition which is obtained from cooking or blanching water of peas, the composition comprising (5R)-(-D-glucopyranosyloxy)-1,5-dihydro-2H-pyrrol-2-one.

A method of identifying a selected pollination window in a Poaceae crop by monitoring one or more environmental parameters and identifying a selected pollination window based upon the monitored parameters. The correct selection of parameters has been shown to markedly increase seed set, yield, and/or other desirable characteristics, including but not limited to preferred content of oil, starch, protein, and/or other nutritional components. Parameters may include one or more of: temperature, relative humidity, and vapor pressure deficit.

A system and method for anti-nutritional removal includes generating a feed stock from a plant-based protein source, the plant-based protein source having anti-nutritionals disposed therein. The system and method includes generating an ethanol slurry by combining the feed stock with an ethanol wash containing a first volume of ethanol and processing the ethanol slurry through an extractor to generate an ethanol matrix and a feed stock mass. The method and system further includes providing the feed stock mass to a desolventizer and generating a desolventized feed stock mass therefrom. Therein, the method and system includes drying the desolventized feed stock mass to generate a clean feed stock with at least a portion of the anti-nutritionals removed therefrom. In one embodiment, the feed stock may be fava beans with the removal of vicine and covicine as anti-nutritionals.

Pulse proteins of reduced astringency are obtained by fractionating pulse protein products which are completely soluble and heat stable in aqueous media at acid pH value of less than about 4.4 into lower molecular weight, less astringent proteins and higher molecular weight, more astringent proteins.

A method provides for removing oil content from a source material and extracting protein from the source material prior to generating a protein concentrate, including decorticating the source material, the source material having a protein and an oil content therein, the decorticating to remove a cortex from the source material. The method includes creating a flour from the source material having the cortex removed therefrom, removing at least a portion of the oil content from the flour by generating a solvent mixture by mixing the flour with a solvent and extracting a de-oiled flour from the solvent mixture, including oil and sugars extracted from the flour. The solvent may include supercritical CO2, subcritical CO2, ethanol, or a combination thereof. The method includes drying the de-oiled flour using at least one dryer and extracting a protein concentrate from the de-oiled flour.