Abstract: Disclosed is a method for purifying sialylated oligosaccharides from a fermentation broth, cell-lysate or biocatalytic reaction mixture for obtaining high amounts of desired sialylated oligosaccharides in high purity. The method is particular suitable for the large-scale economic purification of sialylated human milk oligosaccharides (such as 3?-sialyllactose, 6?-sialyllactose or sialylated lacto-N-tetraose derivatives) from microbial fermentation, using recombinant bacterial cells or yeast cells. The obtained material is of high purity and can be used for food or medical application such like medical nutrition products, infant formula, dietary supplements, general nutrition products (e.g. dairy drinks).

Abstract: The present invention concerns an efficient way to isolate L-fucose from a fermentation broth. The L-fucose contained in the fermentation broth is produced by microbial fermentation (bacterial or yeasts). The inventive process comprises a step of removing biomass from the fermentation broth, a step of subjecting the resulting solution to at least one of a cationic ion exchanger treatment and an anionic ion exchanger treatment and a step of removing salts after the ion exchanger treatment. The process can provide L-fucose in powder form, in granulated form as well as in form of L-fucose crystals.

Abstract: The present invention describes an efficient way to isolate a sialic acid from a fermentation broth. The sialic acid contained in the fermentation broth is produced by bacterial fermentation. The inventive process comprises a step of removing biomass from the fermentation broth, a step of subjecting the resulting solution to at least one of a cationic ion exchanger treatment and an anionic ion exchanger treatment and a step of removing salts after the ion exchanger treatment. The process can provide the sialic acid in spray-dried form as well as in form of sialic acid crystals.

Abstract: Provided is a method for the purification of lacto-N-neotetraose from other carbohydrates, characterized in that the method comprises the steps of subjecting an aqueous solution containing lacto-N-neotetraose to two membrane filtration steps using different membranes or of subjecting an aqueous solution containing lacto-N-neotetraose to a membrane filtration step and a continuous chromatography.

Abstract: The present invention concerns an efficient way to isolate L-fucose from a fermentation broth. The L-fucose contained in the fermentation broth is produced by microbial fermentation (bacterial or yeasts). The inventive process comprises a step of removing biomass from the fermentation broth, a step of subjecting the resulting solution to at least one of a cationic ion exchanger treatment and an anionic ion exchanger treatment and a step of removing salts after the ion exchanger treatment. The process can provide L-fucose in powder form, in granulated form as well as in form of L-fucose crystals.

Abstract: Provided is a method for the purification of lacto-N-neotetraose from other carbohydrates, characterized in that the method comprises the steps of subjecting an aqueous solution containing lacto-N-neotetraose to two membrane filtration steps using different membranes or of subjecting an aqueous solution containing lacto-N-neotetraose to a membrane filtration step and a continuous chromatography.

Abstract: The present invention relates to a method for drying human milk oligosaccharides (HMOs). More specifically, the present invention is related to a method of roller drying or drum drying of human milk oligosaccharides in a simple and economical way.

Abstract: Disclosed is a process for the purification of LNnT (lacto-N-neotetraose) from a fermentation broth, the process comprises subjecting a fermentation broth to a first step of membrane filtration, thereby providing a filtrated solution, such filtrated solution is subjecting to a second step of simulated moving bed chromatography, obtaining a purified solution thereof, then subjecting this purified solution to a third step of crystallization, obtaining crystals containing the LNnT of interest, and subjecting the crystals to a fourth and final step of drying, thereby providing a highly purified powder of LNnT.

Abstract: Disclosed is method for the purification of an oligosaccharide of interest from a fermentation broth, the method comprises providing a cell-free fermentation broth to a first filtration step using a nanofiltration membrane, thereby providing a filtrate which contains the oligosaccharide of interest; subjecting the filtrate to a second filtration step using a nanofiltration membrane, thereby providing a retentate which contains the oligosaccharide of interest; and removing salts from the retentate thereby providing a purified preparation of the oligosaccharide of interest.

Abstract: The present application discloses a process for the purification of a neutral human milk oligosaccharide (neutral HMO). The process uses simulated moving bed (SMB) chromatography which allows the continuous purification of large quantities of HMOs with high purity. Contrary to chemical synthesis routes of neutral HMOs, and their subsequent purification, the presented process allows the provision of HMOs free of noxious chemicals, such as e.g. trace amounts of heavy metals or organic solvents. The individual neutral HMO product may be obtained in solid form by spray drying or as a concentrated syrup. The provided neutral HMO is very well-suited for use in food applications.

Abstract: Provided is a method for the purification of lacto-N-neotetraose from other carbohydrates, characterized in that the method comprises the steps of subjecting an aqueous solution containing lacto-N-neotetraose to two membrane filtration steps using different membranes or of subjecting an aqueous solution containing lacto-N-neotetraose to a membrane filtration step and a continuous chromatography.

Abstract: Provided is a method for the purification of a sialyllactose from other carbohydrates, characterized in that the method comprises the steps of subjecting an aqueous solution containing the sialyllactose to two membrane filtration steps using different membranes, a membrane having a molecular weight cut-off of between about 300 Dalton to about 500 Dalton and a membrane having a molecular weight cut-off of between about 600 Dalton to about 800 Dalton.

Abstract: The present invention concerns an efficient way to isolate L-fucose from a fermentation broth. The L-fucose contained in the fermentation broth is produced by microbial fermentation (bacterial or yeasts). The inventive process comprises a step of removing biomass from the fermentation broth, a step of subjecting the resulting solution to at least one of a cationic ion exchanger treatment and an anionic ion exchanger treatment and a step of removing salts after the ion exchanger treatment. The process can provide L-fucose in powder form, in granulated form as well as in form of L-fucose crystals.

Abstract: The present invention describes an efficient way to isolate a sialic acid from a fermentation broth. The sialic acid contained in the fermentation broth is produced by bacterial fermentation. The inventive process comprises a step of removing biomass from the fermentation broth, a step of subjecting the resulting solution to at least one of a cationic ion exchanger treatment and an anionic ion exchanger treatment and a step of removing salts after the ion exchanger treatment. The process can provide the sialic acid in spray-dried form as well as in form of sialic acid crystals.

Abstract: Disclosed is a method for purifying sialylated oligosaccharides from a fermentation broth, cell-lysate or biocatalytic reaction mixture for obtaining high amounts of desired sialylated oligosaccharides in high purity. The method is particular suitable for the large-scale economic purification of sialylated human milk oligosaccharides (such as 3?-sialyllactose, 6?-sialyllactose or sialylated lacto-N-tetraose derivatives) from microbial fermentation, using recombinant bacterial cells or yeast cells. The obtained material is of high purity and can be used for food or medical application such like medical nutrition products, infant formula, dietary supplements, general nutrition products (e.g. dairy drinks).

Abstract: The present application discloses a process for the purification of a neutral human milk oligosaccharide (neutral HMO). The process uses simulated moving bed (SMB) chromatography which allows the continuous purification of large quantities of HMOs with high purity. Contrary to chemical synthesis routes of neutral HMOs, and their subsequent purification, the presented process allows the provision of HMOs free of noxious chemicals, such as e.g. trace amounts of heavy metals or organic solvents. The individual neutral HMO product may be obtained in solid form by spray drying or as a concentrated syrup. The provided neutral HMO is very well-suited for use in food applications.

Abstract: The present application discloses a process for the purification of a neutral human milk oligosaccharide (neutral HMO). The process uses simulated moving bed (SMB) chromatography which allows the continuous purification of large quantities of HMOs with high purity. Contrary to chemical synthesis routes of neutral HMOs, and their subsequent purification, the presented process allows the provision of HMOs free of noxious chemicals, such as e.g. trace amounts of heavy metals or organic solvents. The individual neutral HMO product may be obtained in solid form by spray drying or as a concentrated syrup. The provided neutral HMO is very well-suited for use in food applications.

Abstract: The present application discloses a process for the purification of a neutral human milk oligosaccharide (neutral HMO). The process uses simulated moving bed (SMB) chromatography which allows the continuous purification of large quantities of HMOs with high purity. Contrary to chemical synthesis routes of neutral HMOs, and their subsequent purification, the presented process allows the provision of HMOs free of noxious chemicals, such as e.g. trace amounts of heavy metals or organic solvents. The individual neutral HMO product may be obtained in solid form by spray drying or as a concentrated syrup. The provided neutral HMO is very well-suited for use in food applications.