A high-protein milk raw material having a good flavor is provided. The liquid high-protein milk raw material of the present invention can be produced by preparing a milk fluid from the milk raw material and subjecting the milk fluid to concentration processing using a nanofiltration membrane.

A high-protein milk raw material having a good flavor is provided. The liquid high-protein milk raw material of the present invention can be produced by preparing a milk fluid from the milk raw material and subjecting the milk fluid to treatment in contact with activated carbon.

A high-protein milk raw material having a good flavor is provided. The liquid high-protein milk raw material of the present invention can be produced by preparing a milk fluid from the milk raw material and subjecting the milk fluid to treatment in contact with activated carbon.

A method for producing a milk or whey powder, involves providing milk or whey, thickening the milk or whey using a first evaporation process or second evaporation process, and drying the thickened milk or whey to provide a milk or whey powder. After the first or second evaporation process, the milk or whey is sterilized using a centrifugal bacteria-removing separator.

A low-bacteria milk powder with a high WPNI is suggested, which is obtainable by (a) providing a raw milk; (b) heating the raw milk in at least one tubular heat exchanger to a temperature of at least 20° C.; (c) separating the cream, obtaining a skimmed milk; (d) pasteurising the skimmed milk in a tubular heat exchanger for a period from 10 to 60 seconds at a temperature from 72 to 75° C.; (e) evaporating the pasteurised skimmed milk to a dry matter content from 35 to 55% by weight; and (f) drying the pasteurised skimmed milk concentrate in a spray tower.

A low-bacteria milk powder with a high WPNI is suggested, which is obtainable by (a) providing a raw milk; (b) heating the raw milk in at least one tubular heat exchanger to a temperature of at least 20° C.; (c) separating the cream, obtaining a skimmed milk; (d) pasteurising the skimmed milk in a tubular heat exchanger for a period from 10 to 60 seconds at a temperature from 72 to 75° C.; (e) evaporating the pasteurised skimmed milk to a dry matter content from 35 to 55% by weight; and (f) drying the pasteurised skimmed milk concentrate in a spray tower.

The present disclosure relates to methods and systems for concentrating a solids stream recovered from one or more process streams derived from a beer in a biorefinery by exposing the recovered solids stream to an evaporator system to remove moisture therefrom and form a concentrated, recovered solids stream.

The present disclosure relates to methods and systems for concentrating a solids stream recovered from one or more process streams derived from a beer in a biorefinery by exposing the recovered solids stream to an evaporator system to remove moisture therefrom and form a concentrated, recovered solids stream.

A removable insert and a spray nozzle which includes the removable insert and a nozzle cap. The removable insert has a base member and a protruding member. The nozzle cap has an annular flange which delimits an interior locating surface for the insert. The flange extends radially and ends with an internal extremity which defines a planar spray opening. When in use, the base member is housed within the nozzle cap whilst the protruding member projects outwardly and stands proud of the planar spray opening.

A removable insert and a spray nozzle which includes the removable insert and a nozzle cap. The removable insert has a base member and a protruding member. The nozzle cap has an annular flange which delimits an interior locating surface for the insert. The flange extends radially and ends with an internal extremity which defines a planar spray opening. When in use, the base member is housed within the nozzle cap whilst the protruding member projects outwardly and stands proud of the planar spray opening.