The present invention describes a bio-based process to produce high quality protein concentrate (HQPC) by converting plant derived celluloses into bioavailable protein via aerobic incubation, including the use of such HQPC so produced as a nutrient, including use as a fish meal replacement in aquaculture diets.

The present invention describes a bio-based process to produce high quality protein concentrate (HQPC) by converting plant derived celluloses and carbohydrates into bioavailable protein via aerobic incubation, including the use of such HQPC so produced as a nutrient, including use as a fish meal replacement in aquaculture diets.

The present invention is directed to enzyme based methods for removing water insoluble non-starch polysaccharides (NSPs) and/or water soluble or insoluble oligosaccharides from soy products without significantly damaging the proteins contained therein This removal is facilitated by the enzymatic hydrolysis of poly- and oligomeric carbohydrates into monosaccharides and other water soluble sugars. The present invention provides for the production of three streams of useful materials. The first is an enriched protein material comparable to the known SPCs but without significant quantities of undigestible oligosaccharides and polysaccharides. The second is an SPI made from the soluble protein in the hydrolysate which is valuable for high-quality feed, food and industrial uses. The third is the soluble saccharides and hydrolyzed carbohydrates (releasing sugars) that can be converted by fermentation to various valuable bioproducts.

The present invention is directed to a modified rapeseed protein isolate and to a process for making a modified rapeseed protein isolate with the aid of a peptidyl arginine deiminase.

Food-grade pulse protein concentrates prepared from various pulses and flours derived therefrom are provided. Also provided are method of making the concentrates and beverages and foodstuffs that include the concentrates. The pulse protein concentrates are characterized by a high protein content, high digestibility, and complete essential amino acid profile.

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.

The invention relates to a process for preparing a protein containing fermented plant based product yoghurt analogue liquid from a defatted oleaginous plant, characterized in that it comprises the following steps: a) Forming a suspension comprising the defatted oleaginous plant in an aqueous solvent; b) Enzymatically treating the suspension obtained in step a), with the following enzymes: at least one protein glutaminase for the solubilisation in said aqueous solvent of proteins contained in the defatted oleaginous plant, optionally one transglutaminase, at least one glycosidase, said enzymes being used successively or simultaneously; c) Homogenizing at a pressure higher than 30 bar to obtain a protein containing plant based product, d) Optionally recovering the plant protein containing plant based product obtained in step c); e) Heating the plant based product to a temperature from 80 C. to 140 C. for 2 seconds to 10 min; and f) Inoculating the plant based product with at least one starter culture to obtain an inoculated the plant based product and fermenting the plant based product until reaching a pH from 4.5 and 5.5 to obtain a protein containing fermented plant based product. The invention also relates to product obtainable from this process.

A process for producing a protein isolate from an oilseed meal, and the isolate thus obtained, said isolate comprising proteins and an amount of 4 wt. % or less of phytic acid, said amount of phytic acid being by weight of proteins in said isolate. The process may comprise the following steps: a) providing an oilseed meal; b) mixing the oilseed meal with a first aqueous solvent to form a slurry at a pH ranging from 6 to 7.8, said slurry having a solid phase; c) separating said solid phase from said slurry, d) mixing said separated solid phase with a second aqueous solvent at a pH ranging from 1 to 3.5, preferably from 2 to 3, to form a mixture said mixture having a liquid phase; e) separating said liquid phase from said mixture formed in step d); f) f1) mixing the separated liquid phase to a phytase at a temperature and a pH suitable for phytase activity to obtain a mixture having a liquid phase and a solid phase; and/or f2) mixing the separated liquid to a salt, to obtain a resulting liquid composition having a molar concentration of said salt ranging from 0.05M to 0.5M, at a temperature ranging from 40 C. to 70 C., to obtain a mixture having a liquid phase and a solid phase; g) precipitating a solid phase from the liquid of step f) for example by a cooling down step of the mixture to a temperature of 30 C. or less; h) separating said solid precipitate from the liquid of step g) said liquid comprising a water-rich liquid phase and an oil-rich liquid phase; i) separating said water-rich liquid phase from said oil-rich liquid phase, j) subjecting said water-rich liquid phase obtained in step i) to one or several membrane filtration(s) to obtain a protein isolate; and k) optionally, drying said protein isolate to obtain a dry protein isolate.

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.

Provided herein are methods for producing a mung bean protein isolate having high functionality for a broad range of food applications. In some embodiments, the methods for producing the isolate comprise one or more steps selected from: (a) extracting one or more mung bean proteins from a mung bean protein source in an aqueous solution, for example, at a pH between about 6.5-10.0; (b) purifying protein from the extract using at least one of two methods: (i) precipitating protein from the extract at a pH near the isoelectric point of a globulin-rich fraction, for example a pH between about 5.0-6.0; and/or (ii) fractionating and concentrating protein from the extract using filtration such as microfiltration, ultrafiltration or ion-exchange chromatography; and (c) recovering purified protein isolate.