A23J1/16

Protein suspension from brewer's grains, method and apparatus for obtaining same
11576401 · 2023-02-14 · ·

The group of inventions relates to the food industry, and more particularly to a method and device for transforming brewer's spent grain (BSG). The invention makes it possible to increase the level of recovery of edible fractions from BSG to 90-95%, and to increase the amount of protein in an edible suspension to not less than 50 wt % dry solids. The underlying principle of the invention is a technique for preparing BSG for nutrient extraction and extracting said nutrients by mechanical processing on a proposed industrial processing line. The essence of the claimed method lies in loosening BSG on a vibratory sieve, grinding the BSG in a colloid mill with the addition of water or centrate in a ratio of from 0.5:1 to 1:1 relative to BSG to produce a paste-like homogeneous mass of BSG, and then processing said mass in a screw extractor for further grinding and separation into two fractions: an edible suspension having a 90-95% moisture content and containing all of the nutrients of BSG, including protein substances; and ground BSG husks having a 60-75% moisture content, suitable for subsequent industrial use. The edible suspension is then mechanically filtered to remove ground husk residue, and the suspension is pumped into a storage tank.

Fractionated stillage separation

This disclosure describes methods to separate solids from liquids in a production facility. A process separates components in the process stream by using a mechanical device to separate the solids from the liquids based on a density difference. The process produces the liquids and solids, which may be further processed to create valuable animal feed products.

Fractionated stillage separation

This disclosure describes methods to separate solids from liquids in a production facility. A process separates components in the process stream by using a mechanical device to separate the solids from the liquids based on a density difference. The process produces the liquids and solids, which may be further processed to create valuable animal feed products.

METHOD FOR SEPARATION OF POTATO PROTEINS AND INSOLUBLE FIBERS FROM PHENOLIC AND/OR GLYCOALKALOID COMPOUNDS

The present invention concerns a method for separation of (a) potato proteins and insoluble fibers from (b) first salts and phenolic and/or glycoalkaloid compounds in potato fruit juice or a derivative thereof, said method comprising the steps of: (i) providing a potato fruit juice or a derivative thereof, comprising potato proteins; and insoluble fibers; and one or more first salts; and phenolic and/or glycoalkaloid compounds; (ii) subjecting the potato fruit juice or the derivative thereof to a first cross-flow membrane filtration process resulting in a first retentate and a first permeate; and (iii) adding aqueous diafiltration liquid containing one or more salts to the first retentate and performing a second cross-flow membrane filtration as diafiltration, to create a second permeate containing at least a portion of said phenolic and/or glycoalkaloid compounds and salts and a second retentate comprising potato proteins, salts and insoluble fibers.

The present invention further concerns a potato fruit juice product comprising potato protein and insoluble fibers, such as a potato fruit juice product obtainable by the method according to the invention.

METHOD FOR SEPARATION OF POTATO PROTEINS FROM PHENOLIC AND/OR GL Y CO ALKALOID COMPOUNDS

The invention concerns a method for the separation of potato proteins from one or more first salts and phenolic and/or glycoalkaloid compounds in potato fruit juice, said method comprising the steps of: (i) providing a potato fruit juice comprising potato proteins, one or more first salts and phenolic and/or glycoalkaloid compounds; (ii) subjecting said potato fruit juice to a first cross-flow membrane filtration process wherein at least a portion of the first salts and at least a portion of the phenolic and/or glycoalkaloid compounds migrate across the membrane into a first permeate and the potato proteins are retained in a first retentate; (iii) adding one or more second salts and water to the first retentate, while continuing the membrane filtration process, to create a diafiltrate containing at least a portion of said phenolic and/or glycoalkaloid compounds and the added second salts and a retentate; and (iv) subjecting the first permeate and/or said diafiltrate from said first cross-flow membrane filtration process to a second cross-flow membrane filtration process.

METHOD FOR SEPARATION OF POTATO PROTEINS WITH REDUCED ENZYMATIC ACTIVITY FROM POTATO FRUIT JUICE

The present invention concerns a method for separation of (a) potato proteins and optionally insoluble fibers from (b) first salts and phenolic and/or glycoalkaloid compounds in potato fruit juice or a derivative thereof, said method comprising the steps of:

(i) providing a potato fruit juice or a derivative thereof;

(ii) subjecting said potato fruit juice or the derivative thereof to a first cross-flow membrane filtration process resulting in a first permeate and a first retentate;

(iii) adding aqueous diafiltration liquid containing one or more salts to the first retentate and performing a second cross-flow membrane filtration as diafiltration, to create a second permeate being a diafiltrate containing at least a portion of said phenolic and/or glycoalkaloid compounds and salts and a second retentate comprising potato proteins, salts and optionally insoluble fibers;

wherein the pH of the first retentate and the second retentate remains within the range of 4.5 to 8.5 during step (ii) and step (iii), said method further comprising a step of eliminating or reducing enzymatic activity.

SOY PROTEINS FOR PREPARATION OF GELS, FIBERS AND FILMS
20220378713 · 2022-12-01 ·

The present invention provides compositions of soy protein gel fibers, soy protein fiber membranes, and soy protein films. The present invention also provides methods of making the soy protein compositions and also uses of the compositions.

FREEZE CONCENTRATION OF ROOT- OR TUBER JUICE

The invention provides a method for treating root—or tuber juice, comprising a) a pretreatment of the root—or tuber juice to remove root—or tuber lipids to a level below 28 g/kg dry weight; b) cooling the root—or tuber juice to a temperature of −0.3° C. to −16° C. to form ice crystals; and c) separating the ice crystals from the root—or tuber juice to obtain, as a first root—or tuber juice product, a concentrated root—or tuber juice. In addition, the invention provides methods to obtain protein depleted root—or tuber juice products, as well as products comprising root—or tuber free amino acids, and uses thereof.

FREEZE CONCENTRATION OF ROOT- OR TUBER JUICE

The invention provides a method for treating root—or tuber juice, comprising a) a pretreatment of the root—or tuber juice to remove root—or tuber lipids to a level below 28 g/kg dry weight; b) cooling the root—or tuber juice to a temperature of −0.3° C. to −16° C. to form ice crystals; and c) separating the ice crystals from the root—or tuber juice to obtain, as a first root—or tuber juice product, a concentrated root—or tuber juice. In addition, the invention provides methods to obtain protein depleted root—or tuber juice products, as well as products comprising root—or tuber free amino acids, and uses thereof.

Process for obtaining a concentrated protein-rich phase from waste products of bioethanol production

1) A method for obtaining a concentrated protein-rich phase from residues of bioethanol production. 2.1) Previously, the separation of a protein-rich phase from whole stillage from bioethanol production has been achieved either by the addition of chemicals or by process steps that are complex in terms of equipment and/or energy. 2.2) Whole stillage from bioethanol production is fed to a solid-liquid separation, and the liquid phase (thin stillage) resulting from this is partially returned to the mashing process. This recirculation increases the raw protein content in the process. Part of the thin stillage is diluted and fed to a simple separation process without the addition of chemicals and temperature treatment, with a protein-rich phase being obtained. 2.3) A protein-rich phase is obtained from residues of bioethanol production.