A23C9/16

Low-bacteria milk powders with a high WPNI (III)

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.

Low-bacteria milk powders with a high WPNI (III)

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.

FREEZE-DRYING, STORING, REHYDRATING AND FEEDING USING BREAST MILK
20230255222 · 2023-08-17 ·

The present invention is a system and method for performing freeze drying of small quantities of a liquid for personal use, wherein a liquid material is disposed within a single-use container, the container is then coupled to a small-scale freeze-drying unit which extracts liquid from the material in the container using a freeze-drying process, and the freeze-dried material is then left in the container and the container is stored until rehydration. The container may be a specialized single-use container that may be used to rehydrate the liquid and then fitted with a delivery device to feed an infant or child.

FREEZE-DRYING, STORING, REHYDRATING AND FEEDING USING BREAST MILK
20230255222 · 2023-08-17 ·

The present invention is a system and method for performing freeze drying of small quantities of a liquid for personal use, wherein a liquid material is disposed within a single-use container, the container is then coupled to a small-scale freeze-drying unit which extracts liquid from the material in the container using a freeze-drying process, and the freeze-dried material is then left in the container and the container is stored until rehydration. The container may be a specialized single-use container that may be used to rehydrate the liquid and then fitted with a delivery device to feed an infant or child.

Food products for infants and babies and method of making same
11324247 · 2022-05-10 · ·

A milk food product is provided that when mixed with baby food and given regularly to a baby will reduce the likelihood of the baby developing a food allergy. The milk food product is produced by taking milk and mixing or whipping the milk with other ingredients such as rice, tapioca, wheat, corn, nut flours, soy flour, or bean flour. The resulting batter is then baked in order to produce a cake-like product. The resulting cake is then dried in order to remove substantially all moisture. The dried cake is then ground or milled into a powder.

HUMAN MILK FORTIFIER
20230248011 · 2023-08-10 ·

The present disclosure provides a human milk fortifier product composition with, a protein component in the milk fortifier in an amount ranging from 6 wt/wt % to 35 wt/wt % on solids basis; a fat component in the in the milk fortifier in an amount ranging from 0.1 wt/wt % to 36 wt/wt % on solids basis; a carbohydrate in the milk fortifier selected from the group of Lactose and Oligosaccharides present in the in an amount from 25 wt/wt % to 75 wt/wt % on solids basis; small molecules consisting of Oligosaccharides in the human milk fortified by the said fortifier is at least 25% more than the human milk alone. The majority of small molecules consisting of Vitamin A, Vitamin D, Vitamin E, LCPUFA, Epidermal growth factor and many others are retained in the fortifier product.

HUMAN MILK FORTIFIER
20230248011 · 2023-08-10 ·

The present disclosure provides a human milk fortifier product composition with, a protein component in the milk fortifier in an amount ranging from 6 wt/wt % to 35 wt/wt % on solids basis; a fat component in the in the milk fortifier in an amount ranging from 0.1 wt/wt % to 36 wt/wt % on solids basis; a carbohydrate in the milk fortifier selected from the group of Lactose and Oligosaccharides present in the in an amount from 25 wt/wt % to 75 wt/wt % on solids basis; small molecules consisting of Oligosaccharides in the human milk fortified by the said fortifier is at least 25% more than the human milk alone. The majority of small molecules consisting of Vitamin A, Vitamin D, Vitamin E, LCPUFA, Epidermal growth factor and many others are retained in the fortifier product.

PROCESS FOR MAKING LACTOSE-FREE MILK POWDERS

The invention relates to a process for producing a lactose-free milk powder with a fat-standardized content, such as whole milk, skim milk, lowfat milk, organic milk, non-organic milk and the like.

PROCESS FOR MAKING LACTOSE-FREE MILK POWDERS

The invention relates to a process for producing a lactose-free milk powder with a fat-standardized content, such as whole milk, skim milk, lowfat milk, organic milk, non-organic milk and the like.

PROCESS FOR THE PREPARATION OF A POWDERY COMPOSITION COMPRISING BIOACTIVE MOLECULES

Process for the preparation of a powder comprising bio active molecules, said process comprising the steps of (i) providing a liquid composition comprising bio active molecules, (ii) optionally pre-heating said liquid composition, provided that the temperature of the liquid composition does not exceed 65° C., (iii) transporting the optionally pre-heated liquid composition to the top of a spray drying tower via a tower feeding line, (iv) raising the temperature of the optionally pre-heated liquid composition using a direct electric volumetric heater located within the tower feeding line, the final temperature of the liquid composition being in the range 60-90° C., followed by (v) transporting the resulting liquid composition via the tower feeding line to the atomizer of a spray-dryer.