A23J3/32

NUTRIENT MEDIA FOR CELL CULTURE CONTAINING PLANT PROTEIN HYDROLYSATES
20240043795 · 2024-02-08 · ·

The present invention relates to nutritional components suitable for cell culture of eukaryotic cells. These nutritional components can be prepared from plant-based protein hydrolysates. The invention further relates to nutrient media comprising these nutritional components. The nutrient media of the invention can be prepared by replacing serum components, which are common in such media, at least partiallyby the nutritional components of the invention. The nutritional components and the nutrient media of the invention are particularly suitable for use in the food industry, such as in the production of cultured meat.

NUTRIENT MEDIA FOR CELL CULTURE CONTAINING PLANT PROTEIN HYDROLYSATES
20240043795 · 2024-02-08 · ·

The present invention relates to nutritional components suitable for cell culture of eukaryotic cells. These nutritional components can be prepared from plant-based protein hydrolysates. The invention further relates to nutrient media comprising these nutritional components. The nutrient media of the invention can be prepared by replacing serum components, which are common in such media, at least partiallyby the nutritional components of the invention. The nutritional components and the nutrient media of the invention are particularly suitable for use in the food industry, such as in the production of cultured meat.

PROTEIN-CONTAINING OIL AND FAT EMULSIFIED COMPOSITION FOR PRODUCING EMULSIFIED FOODS
20240156143 · 2024-05-16 · ·

A protein-containing oil-and-fat emulsion composition for producing an emulsified food is provided. The composition includes 1 to 70 mass % of a protein, 30 to 99 mass % of an oil and fat, and 0 to 40 mass % of a carbohydrate, based on the total amount of the protein, the oil and fat, and the carbohydrate being 100 mass %. 50 mass % or greater of the protein is derived from a denatured protein material satisfying both a) and b): a) an area ratio of 2000 Da or greater and less than 20000 Da is 45 to 90% in a measurement result of molecular weight distribution; and b) an aqueous solution containing the denatured protein material and having a crude protein concentration of 0.1% remains unturbid when 250 mM guanidinium hydrochloride is added to the aqueous solution, but the aqueous solution becomes turbid when 2M ammonium sulphate is added to the aqueous solution.

Hydrolysis method for obtaining a hydrolysed dry food product in powder form

A hydrolysis method for obtaining a hydrolysed dry food product in powder form by adding an acid solution to a material having a vegetable or animal origin for obtaining an acidified paste having a pH of less than 2.0; leaving the acidified paste to rest for the hydrolysis to take place; adding to the acidified paste obtained in the previous step a ground flour having a vegetable or animal origin having a granulometry such that, at least, 50% thereof has a size of less than 1 mm; adding an adsorbent excipient to the mix of acidified paste and ground vegetable/animal flour obtained in the previous step; and leaving the mix of acidified paste, ground vegetal/animal flour and adsorbent excipient to rest until the hydrolyzed dry food product in powder form is obtained.

TREATMENT OF KERATIN-CONTAINING BIOLOGICAL MATERIALS

The present invention provides methods for extraction of amino acid-rich fractions from keratin-containing biological materials, and to amino acid-rich protein fractions generated by the methods described herein. The methods involve forming a reaction mixture with keratin containing material at a pH of 1.1 to 6.9. The reaction mixture is exposed to an energy source, such as microwaves, sufficient to degrade the keratin. The amino acid mixture which is subsequently extracted is substantially insoluble.

PRODUCTION PROCESS OF SOYBEAN MEAL WITH HIGH CONTENT OF SOLUBLE PROTEINS AND PRODUCT SO OBTAINED

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.

METHOD FOR PRODUCING HYDROLYSED KERATINACEOUS MATERIAL
20190075817 · 2019-03-14 · ·

The invention relates to a method for producing digestible keratinaceous material comprising the steps of hydrolysing keratinaceous material in the presence of water in a hydrolyser at elevated temperature and at a pressure between about 2 bar and about 15 bar, and drying the resultant hydrolysed keratinaceous material comprising at least partly insoluble material in a dryer at a temperature/time/pressure combination which limits the drop in pepsin and/or ileal digestibility by less than 10%, and/or such that the pepsin and/or ileal digestibility remains higher than 85%, or such that the pepsin and ileal digestibility remains higher than respectively 75% and 85%. Preferably, the drying of the resultant hydrolysed partly soluble keratinaceous material is performed in a dryer at a temperature such that the keratinaceous material remains at a temperature below 90? C., preferably below 80? C.

METHOD FOR PRODUCING HYDROLYSED KERATINACEOUS MATERIAL
20190075817 · 2019-03-14 · ·

The invention relates to a method for producing digestible keratinaceous material comprising the steps of hydrolysing keratinaceous material in the presence of water in a hydrolyser at elevated temperature and at a pressure between about 2 bar and about 15 bar, and drying the resultant hydrolysed keratinaceous material comprising at least partly insoluble material in a dryer at a temperature/time/pressure combination which limits the drop in pepsin and/or ileal digestibility by less than 10%, and/or such that the pepsin and/or ileal digestibility remains higher than 85%, or such that the pepsin and ileal digestibility remains higher than respectively 75% and 85%. Preferably, the drying of the resultant hydrolysed partly soluble keratinaceous material is performed in a dryer at a temperature such that the keratinaceous material remains at a temperature below 90? C., preferably below 80? C.

Method for producing hydrolysed keratinaceous material

The invention relates to a method for producing digestible keratinaceous material comprising the steps of hydrolysing keratinaceous material in the presence of water in a hydrolyser at elevated temperature and at a pressure between about 2 bar and about 15 bar, and drying the resultant hydrolysed keratinaceous material comprising at least partly insoluble material in a dryer at a temperature/time/pressure combination which limits the drop in pepsin and/or ileal digestibility by less than 10%, and/or such that the pepsin and/or ileal digestibility remains higher than 85%, or such that the pepsin and ileal digestibility remains higher than respectively 75% and 85%. Preferably, the drying of the resultant hydrolysed partly soluble keratinaceous material is performed in a dryer at a temperature such that the keratinaceous material remains at a temperature below 90? C., preferably below 80? C.

Method for producing hydrolysed keratinaceous material

The invention relates to a method for producing digestible keratinaceous material comprising the steps of hydrolysing keratinaceous material in the presence of water in a hydrolyser at elevated temperature and at a pressure between about 2 bar and about 15 bar, and drying the resultant hydrolysed keratinaceous material comprising at least partly insoluble material in a dryer at a temperature/time/pressure combination which limits the drop in pepsin and/or ileal digestibility by less than 10%, and/or such that the pepsin and/or ileal digestibility remains higher than 85%, or such that the pepsin and ileal digestibility remains higher than respectively 75% and 85%. Preferably, the drying of the resultant hydrolysed partly soluble keratinaceous material is performed in a dryer at a temperature such that the keratinaceous material remains at a temperature below 90? C., preferably below 80? C.