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.

The invention relates to a method of separating components from milk and utilizing the separated components to form a fermentable composition such as yogurts. The present invention relates to nutritional milk compositions and products which are designed to include per serving size a specified percentage range of one or more components separated from milk. The compositions of the present invention can optionally include non-essential but nutritionally functional components.

Disclosed are processes for preparing dry or powder dairy compositions having low lactose contents and containing polyphenol compounds. The resultant dry or powder dairy compositions can be used to form reconstituted fluid dairy products, which can have improved organoleptic properties, such as less cooked flavor, sulfur odor, and brown color.

The invention relates to a method of separating components from milk and utilizing the separated components to form blended dairy compositions. The present invention relates to nutritional milk compositions and products which are designed to include per serving size a specified percentage range of one or more components separated from milk. The compositions of the present invention can optionally include non-essential but nutritionally functional components.

Systems and methods for filtering dairy may filter milk with a wide-pore filter to produce a wide-pore retentate and a wide-pore permeate, wherein the wide-pore retentate may comprise casein and beta-lactoglobulin. The systems and methods may further ultra-filter the wide-pore permeate to produce an ultra-filtered retentate and an ultra-filtered permeate, wherein the ultra-filtered retentate comprises alpha-lactalbumin. The systems and methods may further nano-filter the ultra-filtered permeate to produce a nano-filtered retentate and a nano-filtered permeate, wherein the nano-filtered retentate comprises lactose. The systems and methods may further perform reverse osmosis (RO) on the nano-filtered permeate to produce a reverse osmosis retentate and a reverse osmosis permeate.

A method for producing a low sugar acidified milk product includes providing a milk base having a protein content of about 2.5% to about 8%, a fat content of about 0% to about 10%, a lactose content of about 0.6% to about 2.5% and an ash content of about 0.6% to about 0.9%; adding a citrate preparation to the milk base; optionally homogenizing the milk base; pasteurizing the base milk; fermenting the milk base with a starter culture to provide a low sugar acidified milk product having a pH of about 4.4 to about 4.7. A low sugar acidified milk product includes added citrate preparation in an amount of about 0.1% to about 0.18%, calculated as a pure citrate. A low sugar acidified milk product, wherein the total citrate concentration of the product in the range of about 0.1% to about 0.25%, calculated as pure citrate.

The present invention relates to a bioactive sweet whey protein concentrate or composition for increasing e.g. cognitive functions particularly in young mammals such as pre-term or term infants, toddlers, children or young adults. The present invention further disclose a new concept for large-scale industrial production method of bioactive whey protein concentrates or compositions by use of mild heat treatment and pressure driven membrane separation.

The invention relates to a method of separating components from milk, and the apparatus used therefor. The invention also relates to compositions prepared from the separated components. The present invention relates to nutritional milk compositions and products which are designed to include per serving size a specified percentage range of one or more components separated from milk. The compositions of the present invention can optionally include non-essential but nutritionally functional components. The complete nutritional milk compositions of the present invention can be provided as unflavored milks, flavored milks, ice creams and yogurts.

Systems and methods for generating a processed fortified human milk product from raw human milk, and processed fortified human milk product compositions obtained thereby, are provided. The processed fortified human milk product composition possesses high nutritional content such as high concentrations of protein and human milk oligosaccharides. The processed fortified human milk product composition exhibits low overall bioburden and is non-allogenic and non-immunogenic. When ingested by an individual, the processed fortified human milk product composition achieves high bioavailability and reduces inflammatory processes.

Process for preparing lactose-free skimmed, partially skimmed and whole milk, comprising the following steps: 1) pasteurization and skimming, 2) enzymatic hydrolysis of the skimmed milk by lactase enzyme, 3) microfiltration of the hydrolysed skimmed milk and obtainment of a microfiltration retentate (RMF) and of a microfiltration permeate (PMF), 4) PMF ultrafiltration and obtainment of an ultrafiltration retentate (RUF) and of an ultrafiltration permeate (PUF), 5) first PUF nanofiltration and obtainment of the first nanofiltration retentate (RNF 1) and of a first nanofiltration permeate (PNF 1), 6) second PNF 1 nanofiltration and obtainment of a second nanofiltration retentate (RNF2) and of a second nanofiltration permeate (PNF2), and 7) final step: obtainment of lactose-free milk by mixing one or more of the fractions deriving from one or more of the previous steps, which is characterized in that: (I) the first nanofiltration of step 5) is carried out with membranes having a molecular weight cut-off ranging from 400 to 600 Da and the second nanofiltration is carried out with membranes having a molecular weight cut-off ranging from 150 to 250 Da, and (II) the final step 7) is carried out by mixing a composition comprising at least RUF, RNF1 and PNF2.