A spray drying process and apparatus for drying a spray dryable liquid composition to a spray dried powder is described, in which the spray dryable liquid composition contains no carrier. The spray dryable liquid composition is processed at a solids concentration not exceeding 80% by weight, based on total weight of the spray dryable liquid composition, being atomized to generate an atomized spray of liquid particles of the spray dryable liquid composition into a spray drying chamber, in which the atomized spray is contacted with a stream of drying fluid flowed at temperature not exceeding 100 C. into the spray drying chamber, to form the spray dried powder.

The invention relates to a process for the treatment of animal skim milk and for the production of an infant formula base product from animal skim milk, which process is highly efficient and cost effective, as only membrane filtration techniques, such as microfiltration and ultrafiltration, are required. By carefully controlling the process parameters, a product is obtained in which most of the major components are within the desired range for an infant formula base product. The invention also relates to products obtainable by the process according to the invention.

The invention relates to a process for the treatment of animal skim milk and for the production of an infant formula base product from animal skim milk, which process is highly efficient and cost effective, as only membrane filtration techniques, such as microfiltration and ultrafiltration, are required. By carefully controlling the process parameters, a product is obtained in which most of the major components are within the desired range for an infant formula base product. The invention also relates to products obtainable by the process according to the invention.

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.

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.

Creamers for whitening food products are provided. The creamers can havelong-term stability, high whitening capacity and a pleasant mouthfeel. In a general embodiment, the present disclosure provides aspray-dried creamer composition comprising added sugar comprising sucrose and/or lactose ranging from 5-30% by weight; milk ranging from 30-60% by weight; fat ranging from 15-40% by weight; wherein said composition is devoid of added emulsifiers and/or buffer-and stabilizing salts. The invention also provides a coffee creamer mix comprising the above creamer composition and coated or compacted coffee, wherein coffee dissolves after the creamer dissolution.

Creamers for whitening food products are provided. The creamers can havelong-term stability, high whitening capacity and a pleasant mouthfeel. In a general embodiment, the present disclosure provides aspray-dried creamer composition comprising added sugar comprising sucrose and/or lactose ranging from 5-30% by weight; milk ranging from 30-60% by weight; fat ranging from 15-40% by weight; wherein said composition is devoid of added emulsifiers and/or buffer-and stabilizing salts. The invention also provides a coffee creamer mix comprising the above creamer composition and coated or compacted coffee, wherein coffee dissolves after the creamer dissolution.

A spray drying process and apparatus for drying a spray dryable liquid composition to a spray dried powder is described, in which the spray dryable liquid composition contains no carrier. The spray dryable liquid composition is processed at a solids concentration not exceeding 80% by weight, based on total weight of the spray dryable liquid composition, being atomized to generate an atomized spray of liquid particles of the spray dryable liquid composition into a spray drying chamber, in which the atomized spray is contacted with a stream of drying fluid flowed at temperature not exceeding 100 C. into the spray drying chamber, to form the spray dried powder.

A system and method is provided for processing milk for spray drying. The system may have a pre-evaporator configured to receive and concentrate the milk stream producing an intermediate concentration milk. The system may also have a first buffer tank configured to receive the intermediate concentration milk and store the intermediate concentrate milk at a reduced temperature. The system may further have a first finisher evaporator configured to draw the intermediate concentration milk from the first buffer tank and concentrate the intermediate concentration milk producing a final concentration milk. The final concentration milk may be suitable for spray drying.

A system and method is provided for processing milk for spray drying. The system may have a pre-evaporator configured to receive and concentrate the milk stream producing an intermediate concentration milk. The system may also have a first buffer tank configured to receive the intermediate concentration milk and store the intermediate concentrate milk at a reduced temperature. The system may further have a first finisher evaporator configured to draw the intermediate concentration milk from the first buffer tank and concentrate the intermediate concentration milk producing a final concentration milk. The final concentration milk may be suitable for spray drying.