A process for preparing a galacto-oligosaccharide product comprises exposing a permeate composition to one or more enzymes that convert one or more compounds in the permeate composition to one or more galacto-oligosaccharide compounds to provide a galacto-oligosaccharide solution, wherein at least about 10% of total sugar, by weight, in the galacto-oligosaccharide solution is in the form of the one or more galacto-oligosaccharide compounds, and concentrating at least a portion of the galacto-oligosaccharide solution to provide a galacto-oligosaccharide syrup. In an example, a galacto-oligosaccharide product, for example made by the process, comprises a dry or substantially dry powder including one or more dried compounds from a permeate composition and at least 20% by weight of one or more galacto-oligosaccharides, wherein the powder is free or substantially free from a drying agent.

A product in powder form having a dry matter content of at least 90% by weight on its total weight and containing lactose in a quantity of at least 85% by weight on its total weight, as well as having a high bulk density; moreover a process for the production of this product in powder form is disclosed, comprising the steps of vacuum-concentrating a lactose-containing liquid, mixing the so-concentrated liquid with a lactose-containing powder and with a high dry matter content and, finally, drying the so-obtained powdered mixture.

A product in powder form having a dry matter content of at least 90% by weight on its total weight and containing lactose in a quantity of at least 85% by weight on its total weight, as well as having a high bulk density; moreover a process for the production of this product in powder form is disclosed, comprising the steps of vacuum-concentrating a lactose-containing liquid, mixing the so-concentrated liquid with a lactose-containing powder and with a high dry matter content and, finally, drying the so-obtained powdered mixture.

A system and method for the continuous production of brown butter involves concentrating butter while retaining solids non-fat in the butter, and continuously transferring and heating the concentrated butter to cause the solids non-fat in the butter to react in a maillard reaction to form a brown butter product. The system may use one or more of a heating vessel, an evaporator and a reaction vessel to form the brown butter in the continuous process. A brown butter product derived from butter includes reacted solids non-fat particulates from a maillard reaction suspended by nascent fat crystals nucleated about the reacted solids non-fat particulates and by large fat crystal structures joined to the nascent fat crystals.

A system and method for the continuous production of brown butter involves concentrating butter while retaining solids non-fat in the butter, and continuously transferring and heating the concentrated butter to cause the solids non-fat in the butter to react in a maillard reaction to form a brown butter product. The system may use one or more of a heating vessel, an evaporator and a reaction vessel to form the brown butter in the continuous process. A brown butter product derived from butter includes reacted solids non-fat particulates from a maillard reaction suspended by nascent fat crystals nucleated about the reacted solids non-fat particulates and by large fat crystal structures joined to the nascent fat crystals.

A system and method for the continuous production of brown butter involves concentrating butter while retaining solids non-fat in the butter, and continuously transferring and heating the concentrated butter to cause the solids non-fat in the butter to react in a Maillard reaction to form a brown butter product. The system may use one or more of a heating vessel, an evaporator and a reaction vessel to form the brown butter in the continuous process. A brown butter product derived from butter includes reacted solids non-fat particulates from a Maillard reaction suspended by nascent fat crystals nucleated about the reacted solids non-fat particulates and by large fat crystal structures joined to the nascent fat crystals.

A system and method for the continuous production of brown butter involves concentrating butter while retaining solids non-fat in the butter, and continuously transferring and heating the concentrated butter to cause the solids non-fat in the butter to react in a Maillard reaction to form a brown butter product. The system may use one or more of a heating vessel, an evaporator and a reaction vessel to form the brown butter in the continuous process. A brown butter product derived from butter includes reacted solids non-fat particulates from a Maillard reaction suspended by nascent fat crystals nucleated about the reacted solids non-fat particulates and by large fat crystal structures joined to the nascent fat crystals.

Concentrated creams are produced from starting cream compositions characterized as homogenous, oil-in-water emulsions containing fat globules, phospholipid membrane components and non-fat solids, and which have an initial fat content between about 35 to about 55 percent by weight. To produce the concentrated creams, moisture is removed from the starting cream compositions through evaporative processing, and as a result, the concentrated cream remains in a homogenous state, retains the fat globules, phospholipid membrane components and non-fat solids, and includes a concentrated fat content of at least about 70 percent by weight. In addition, the concentrated cream may be in an oil-in-water or a bi-continuous emulsion. Evaporative processing may be through a wiped film evaporator or a scraped surface heat exchanger.

Concentrated creams are produced from starting cream compositions characterized as homogenous, oil-in-water emulsions containing fat globules, phospholipid membrane components and non-fat solids, and which have an initial fat content between about 35 to about 55 percent by weight. To produce the concentrated creams, moisture is removed from the starting cream compositions through evaporative processing, and as a result, the concentrated cream remains in a homogenous state, retains the fat globules, phospholipid membrane components and non-fat solids, and includes a concentrated fat content of at least about 70 percent by weight. In addition, the concentrated cream may be in an oil-in-water or a bi-continuous emulsion. Evaporative processing may be through a wiped film evaporator or a scraped surface heat exchanger.

The present invention relates to a milk powder comprising caseins and whey proteins wherein the powder upon reconstitution in an aqueous medium comprises casein-whey protein/fat aggregates having a mean diameter value Dv50 of at least 1 mycrom as measured by laser diffraction. The invention also relates to a process for preparing a milk powder including the steps of providing a liquid milk concentrate at T<25° C., adjusting pH to 5.7-6.4, heating at 80-150° C. for 3-300 s, cooling to below 70° C. and optionally readjusting the pH to between 6.5-6.8, drying the composition, and the milk powder obtained by this process for producing growing up milks, culinary sauces, coffee mixes, tea and coffee creamer or cocoa-malt beverages.