A23J1/205

WHEY PROTEIN EXTRACTS AND THEIR USE AS SPHINGOMYELIN SOURCE

Use of an -lactalbumin enriched whey protein extract as a source of sphingomyelin in a synthetic nutritional composition for an infant or child wherein, the -lactalbumin enriched WPE is obtained by a process comprising: a. acidifying a whey protein product to pH 4 or below b. forming a low calcium whey protein product by concentrating the proteins in the acidified whey protein until the calcium to protein ratio is less than about 0.001 and, c. Precipitating -lactalbumin from the low-calcium whey protein product, wherein said precipitating step includes the sub-steps of: I. diluting the low-calcium whey protein product, II. adjusting the pH of the diluted low-calcium whey protein product to between 4 and 5 to form a precipitate and soluble proteins, and III. Separating the precipitate proteins from the soluble proteins.

Methods of purifying exosomes

Exosome purification methods involve use of a whey composition as an exosome source. Exosomes are isolated by subjecting the whey composition to a first ultrafiltration, which yields a first permeate and a first retentate. The first retentate may then be subjected to a second ultrafiltration, yielding a second permeate and a second retentate. During the second ultrafiltration, the first retentate may be treated with carbon dioxide. The second retentate may then be subjected to a third ultrafiltration, yielding a third permeate and a third retentate. The third permeate may then be optionally dried to yield an exosome powder.

Capsular polysaccharide solubilisation and combination vaccines
10716841 · 2020-07-21 · ·

Precipitated bacterial capsular polysaccharides can be efficiently re-solubilised using alcohols as solvents. The invention provides a process for purifying a bacterial capsular polysaccharide, comprising the steps of (a) precipitation of said polysaccharide, followed by (b) solubilisation of the precipitated polysaccharide using ethanol. CTAB can be used for step (a). The material obtained, preferably following hydrolysis and sizing, can be conjugated to a carrier protein and formulated as a vaccine. Also, in vaccines comprising saccharides from both serogroups A and C, the invention provides that the ratio (w/w) of Men A saccharide:MenC saccharide is >1.

CMP-containing, high protein denatured whey protein compositions, products containing them, and uses thereof

The present invention pertains to a new type of CMP-containing, high protein denatured whey protein compositions and to a method of producing them. The invention furthermore pertains to products containing the high protein denatured whey protein compositions, particularly high protein, acidified dairy products, and additional uses of the denatured whey protein compositions.

A METHOD OF PRODUCING A FOOD OR BEVERAGE PRODUCT WITH FREE DIVALENT CATIONS DAIRY AND PLANT PROTEIN AGGREGATION

The invention relates to a method of producing a food or beverage product, comprising the steps of: providing an ingredient composition comprising micellar caseins, whey protein and plant protein having a pH of 5.9-7.1, preferably 6.2-6.8, and having a concentration of 1 to 15 wt. % of total proteins, and wherein the composition has a micellar casein to whey protein ratio of, 90/10 to 60/40 and a micellar caseins and whey protein to plant protein ratio of 80/20 to 20/80, adding divalent cations to provide a concentration of 2.0-10 mM free divalent cations in the ingredient composition and subsequently heat treating the ingredient composition to form agglomerated proteins comprising micellar casein, whey protein and plant proteins, the agglomerates having a size of 5 to 50 microns as measured by D(4,3) mean diameter as measured by laser diffraction. The invention also relates to a product obtained by this method.

Methods and compositions involving whey protein isolates

The present invention concerns methods of isolating milk proteins. Methods of the invention include charged ultrafiltration processes that use variations in pH to further separate protein species.

Demineralized whey powders

A demineralised whey powder is suggested which is obtainable by: (a) Separating raw milk, removing the cream; (b) Subjecting the skimmed milk such obtained to microfiltration or microdiafiltration, obtaining a whey protein-rich permeate P1 and a retentate R1 containing casein and GMP in the process; (c) Subjecting the permeate P1 to column chromatography separation, in which the lactoferrin contained therein remains on the column; (d) Subjecting the permeate, from which lactoferrin had been removed, to dialysis; and (e) Dehydrating the diluate such obtained.

Process for the coupled production of sweet whey and lactic acid from acid whey

A process for the coupled production of sweet whey and lactic acid from acid whey is suggested, comprising the following steps: (a) providing acid whey having a lactic acid content of about 0.1 to about 1% by weight; (b) nanofiltration of the acid whey, obtaining a first permeate P1 and a first retentate R1; (c) optionally, redilution of the first retentate R1 with water to reconstitute the initial dry matter content, and preparation of the second nanofiltration step; (d) nanofiltration or nano-diafiltration of the retentate R1, obtaining a second permeate P2 and sweet whey as a second retentate R2; (e) combining the two permeates P1 and P2 and subjecting the mixture to reverse osmosis, obtaining a third permeate P3 which, substantially, only contains water, and a concentrate of lactic acid as a third retentate R3.

Process for treating a sweet whey material containing cGMP and related method for producing a protein material having a targeted tryptophan/threonine ratio

Process for the treatment of a sweet whey material (SWM) containing cGMP (caseinoGlycoMacroPeptide), comprising the following steps: Decationising the SWM material so as to obtain a sweet whey SW having a pH value of 1 to 4.5; Treating said SW in a fluidized bed reactor comprising a volume of an anionic resin, at 10 to 18 C., wherein said SW contacts said resin so that the resin absorbs between 0% and 100% of the cGMP present in the SW; and Recovering a protein material; Wherein the treating is such that the resin absorbs 30 to 45 g/L of the cGMP present in the sweet whey. Method for producing a protein material from a SWM cGMP, said protein material having a targeted tryptophan/threonine (Trp/Thr) ratio, comprising the following steps: Implementing the treating process twice, wherein the resins absorbs P1 of the cGMP, obtaining a first protein material having Trp/Thr1 and wherein the resins absorbs a percentage P2 of the cGMP, obtaining a second protein material having Trp/Thr2; Drafting the linear calibration curve in a graph (cGMP %; Trp/Thr) by positioning (Trp/Thr1; P1) and (Trp/Thr2; P2) and drawing a line through these two plots; Determining the specific ratio of cGMP present in the SW that the resin should absorb with respect to the targeted Trp/Thr by the calibration curve; and Implementing the process of the invention on the SWM wherein the resins absorbs the specific ratio of cGMP, so that to obtain the protein material having the targeted Tp/Thr.

Process for the preparation of whey protein aggregate particles and use thereof

The present invention relates to whey protein aggregate particles that can be used to stabilize foams, and more particularly edible foams, such as foamed dairy products. The invention provides a process for preparation of such whey protein aggregates, for the use of such particles for stabilizing foam, as well as edible foams or foamed product comprising such whey protein aggregate particles.