The present invention relates to a method of separating amino acids from an aqueous solution comprising amino acids as well as proteins and/or protein decomposition products by combining phosphoric acid with the aqueous solution to precipitate an amino acid monophosphate. The precipitate so formed may be separated from the aqueous solution and used as such, e.g. in plant fertilizer compositions. The precipitate may be redissolved in a suitable liquid, after which phosphate and amino acid may be separated following conventional methods. In either case, the present invention enables highly selective precipitation of arginine and/or lysine monophosphate as crystals.

The present invention relates to a method of separating amino acids from an aqueous solution comprising amino acids as well as proteins and/or protein decomposition products by combining phosphoric acid with the aqueous solution to precipitate an amino acid monophosphate. The precipitate so formed may be separated from the aqueous solution and used as such, e.g. in plant fertilizer compositions. The precipitate may be redissolved in a suitable liquid, after which phosphate and amino acid may be separated following conventional methods. In either case, the present invention enables highly selective precipitation of arginine and/or lysine monophosphate as crystals.

The present invention relates to a method of separating amino acids from an aqueous solution comprising amino acids as well as proteins and/or protein decomposition products by combining phosphoric acid with the aqueous solution to precipitate an amino acid monophosphate. The precipitate so formed may be separated from the aqueous solution and used as such, e.g. in plant fertilizer compositions. The precipitate may be redissolved in a suitable liquid, after which phosphate and amino acid may be separated following conventional methods. In either case, the present invention enables highly selective precipitation of arginine and/or lysine monophosphate as crystals.

The present invention provides a process for the preparation of vigabatrin of formula (I) comprising of dissolving vigabatrin in water, optionally treating with charcoal, filtering and adding an acid to the reaction mass followed by the addition of an organic solvent and then isolating vigabatrin of formula (I) with high purity.

##STR00001##

The present invention provides a process for the preparation of vigabatrin of formula (I) comprising of dissolving vigabatrin in water, optionally treating with charcoal, filtering and adding an acid to the reaction mass followed by the addition of an organic solvent and then isolating vigabatrin of formula (I) with high purity.

##STR00001##

The invention relates to a method for the production of acetylsalicylic acid lysinate, optionally lysine acetylsalicylate.glycine, comprising the following steps: a) providing a solution of acetylsalicylic acid in ethanol; b) providing an aqueous solution of lysine; c) combining the solutions of step a) and b) to form a mixture; d) optionally stirring the mixture; e) adding acetone to the mixture; f) incubating the mixture, to allow the formation of a acetylsalicylic acid lysinate product; g) isolating the acetylsalicylic acid lysinate product; wherein acetylsalicylic acid is used in excess compared to lysine and wherein no seed crystals are added to the mixture; and optionally the following further steps: h) providing a recrystallized glycine; wherein the glycine has been recrystallized with the following steps: h1) dissolving glycine in water; h2) adding acetone to the glycine solution; h3) stirring the mixture until a precipitate is obtained; i) combining the recrystallized glycine of step h) with the acetylsalicylic acid lysinate product of step g) to obtain lysine acetylsalicylate.glycine (LASAG) particles.

The invention relates to a method for the production of acetylsalicylic acid lysinate, optionally lysine acetylsalicylate.glycine, comprising the following steps: a) providing a solution of acetylsalicylic acid in ethanol; b) providing an aqueous solution of lysine; c) combining the solutions of step a) and b) to form a mixture; d) optionally stirring the mixture; e) adding acetone to the mixture; f) incubating the mixture, to allow the formation of a acetylsalicylic acid lysinate product; g) isolating the acetylsalicylic acid lysinate product; wherein acetylsalicylic acid is used in excess compared to lysine and wherein no seed crystals are added to the mixture; and optionally the following further steps: h) providing a recrystallized glycine; wherein the glycine has been recrystallized with the following steps: h1) dissolving glycine in water; h2) adding acetone to the glycine solution; h3) stirring the mixture until a precipitate is obtained; i) combining the recrystallized glycine of step h) with the acetylsalicylic acid lysinate product of step g) to obtain lysine acetylsalicylate.glycine (LASAG) particles.

A process for the preparation of a solid composition of an amino acid diacetic acid compound wherein the amino acid diacetic acid compound is methyl glycine-N,N-diacetic acid or a salt thereof, or glutamic N,N-diacetic acid or a derivative thereof, as well as the product obtained by such process are disclosed. The process includes feeding a saturated or oversaturated aqueous composition of the amino acid diacetic acid compound in an aqueous solvent to a drum dryer, wherein the aqueous composition is fed to the drum surface with a layer thickness of from about 0.1 to about 10 mm, the drum has a surface temperature of from about 80 to about 180 C., and the drum operates at a tangential speed of from about 0.1 to about 100 m/min. The method further includes removing the mass from the drum before a full revolution of the drum.

A process for the preparation of a solid composition of an amino acid diacetic acid compound wherein the amino acid diacetic acid compound is methyl glycine-N,N-diacetic acid or a salt thereof, or glutamic N,N-diacetic acid or a derivative thereof, as well as the product obtained by such process are disclosed. The process includes feeding a saturated or oversaturated aqueous composition of the amino acid diacetic acid compound in an aqueous solvent to a drum dryer, wherein the aqueous composition is fed to the drum surface with a layer thickness of from about 0.1 to about 10 mm, the drum has a surface temperature of from about 80 to about 180 C., and the drum operates at a tangential speed of from about 0.1 to about 100 m/min. The method further includes removing the mass from the drum before a full revolution of the drum.

A process for the preparation of a solid composition of an amino acid diacetic acid compound wherein the amino acid diacetic acid compound is methyl glycine-N,N-diacetic acid or a salt thereof, or glutamic N,N-diacetic acid or a derivative thereof, as well as the product obtained by such process are disclosed. The process includes feeding a saturated or oversaturated aqueous composition of the amino acid diacetic acid compound in an aqueous solvent to a drum dryer, wherein the aqueous composition is fed to the drum surface with a layer thickness of from about 0.1 to about 10 mm, the drum has a surface temperature of from about 80 to about 180 C., and the drum operates at a tangential speed of from about 0.1 to about 100 m/min. The method further includes removing the mass from the drum before a full revolution of the drum.