A human milk powderization system can include a spray drying machine, a receptacle, and a container. The spray drying machine can be configured to receive liquid human milk through an inlet at a rate of about 2 milliliters per millisecond and to spray dry the human milk at a temperature of about 163 to 167 degrees C. to transform the liquid human milk into a powderized human milk product. The receptacle can be coupled to and configured to receive the powderized human milk product from the spray drying machine. The receptacle can be formed from one or more nonreactive materials, such as crystal. The container can be removably coupled to and configured to receive the powderized human milk product from the receptacle. The container can be configured to transport the powderized human milk product away from the system, and can be formed from one or more nonreactive materials, such as aluminum.

Provided is a method for producing skim milk powder in which the amount of free fatty acids has been increased without bringing about deterioration of flavor. The method for producing skim milk powder comprises a step of carrying out homogenization treatment under temperature conditions of 30 to 55° C. in a process of producing the skim milk powder from skim milk.

Provided is a method for producing skim milk powder in which the amount of free fatty acids has been increased without bringing about deterioration of flavor. The method for producing skim milk powder comprises a step of carrying out homogenization treatment under temperature conditions of 30 to 55° C. in a process of producing the skim milk powder from skim milk.

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.

Methods of making a powdered milk product are described. The methods may include providing an aqueous milk-sourced mixture, and evaporating water from the aqueous milk-sourced mixture to produce an evaporated milk-sourced mixture having a total solids concentration of 35 wt. % or more. The evaporated milk-sourced mixture may be dried to form the powdered milk product, which may have less than 6 wt. % water. Systems for making the milk powdered product are also described. The systems may include an evaporator to evaporate water from a supply of a milk-sourced mixture to form an evaporated milk-sourced mixture. They may also include a dryer to dry the evaporated milk-sourced mixture and atomize it into the powdered milk product.

Methods of making a powdered milk product are described. The methods may include providing an aqueous milk-sourced mixture, and evaporating water from the aqueous milk-sourced mixture to produce an evaporated milk-sourced mixture having a total solids concentration of 35 wt. % or more. The evaporated milk-sourced mixture may be dried to form the powdered milk product, which may have less than 6 wt. % water. Systems for making the milk powdered product are also described. The systems may include an evaporator to evaporate water from a supply of a milk-sourced mixture to form an evaporated milk-sourced mixture. They may also include a dryer to dry the evaporated milk-sourced mixture and atomize it into the powdered milk product.

A method of production of a homogeneous powdered product from a starting product in a liquid state, the starting product having sugars as at least 60% of its total solids, the method comprising: in the absence of air: pressurizing the starting product to a pressure greater than 1 bar; injecting a gas into the starting product to form a mixture in which the starting product is substantially saturated by the gas; and degassing the mixture into a continuous stream of transport gas such that, on contact with the transport gas, water from the mixture evaporates to leave the homogeneous powdered product.

This application is directed to systems and methods of creating sterilized powdered food product. Specific examples regarding breast milk are described whereby the milk is powderized and placed into a vat before it is passed along to a sterilization chamber in which it is fluidized and sterilized by UV-C light. Once powdered food product has been sufficiently sterilized, it can be loaded into syringes for distribution. Embodiments of the inventive subject matter are designed to maintain nutritional value of the powdered food at levels that were not previously possible, opening new opportunities for storing and distribution of, e.g., donor breast milk.

This application is directed to systems and methods of creating sterilized powdered food product. Specific examples regarding breast milk are described whereby the milk is powderized and placed into a vat before it is passed along to a sterilization chamber in which it is fluidized and sterilized by UV-C light. Once powdered food product has been sufficiently sterilized, it can be loaded into syringes for distribution. Embodiments of the inventive subject matter are designed to maintain nutritional value of the powdered food at levels that were not previously possible, opening new opportunities for storing and distribution of, e.g., donor breast milk.

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.