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• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
  • C12P41/00—Processes using enzymes or microorganisms to separate optical isomers from a racemic mixture
  • C12P41/006—Processes using enzymes or microorganisms to separate optical isomers from a racemic mixture by reactions involving C-N bonds, e.g. nitriles, amides, hydantoins, carbamates, lactames, transamination reactions, or keto group formation from racemic mixtures
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
  • C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
  • C12N9/14—Hydrolases (3)
  • C12N9/78—Hydrolases (3) acting on carbon to nitrogen bonds other than peptide bonds (3.5)
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
  • C12P13/00—Preparation of nitrogen-containing organic compounds
  • C12P13/02—Amides, e.g. chloramphenicol or polyamides; Imides or polyimides; Urethanes, i.e. compounds comprising N-C=O structural element or polyurethanes
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
  • C12P13/00—Preparation of nitrogen-containing organic compounds
  • C12P13/04—Alpha- or beta- amino acids
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
  • C12P13/00—Preparation of nitrogen-containing organic compounds
  • C12P13/04—Alpha- or beta- amino acids
  • C12P13/06—Alanine; Leucine; Isoleucine; Serine; Homoserine
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
  • C12P13/00—Preparation of nitrogen-containing organic compounds
  • C12P13/04—Alpha- or beta- amino acids
  • C12P13/08—Lysine; Diaminopimelic acid; Threonine; Valine

Definitions

• the present invention relates to a process for pre ⁇ paring optically active amino acids. More specifically, this invention relates to a process for preparing a single enantiomeric form of an optically active amino acid or amino acid amide which comprises treating an aqueous solution of the enantiomeric mixture of the amino nitrile analog of the amino acid with an enantioselective nitrilase and thereafter recovering the resulting optically active amino acid or amino acid amide.
• Optically active amino acids constitute a class of organic compounds of great industrial interest.
• the naturally occurring amino acids are thus applied industrially on a large scale as food and feed additives and, in recent years, several amino acids not found in nature and in the following referred to as unnatural amino acids have also found extensive use, for example, as constituents in various pharmacological compositions or as intermediates for organic synthesis of optically active compounds.
• amino acids Due to their molecular structure, most amino acids can occur in two distinct forms differing in respect to the so-called chirality of the amino acid molecule. These two forms of an amino acid which, on the molecular level, are mirror images of one another are usually denoted as the D- and the -form of the amino acid. Most amino acids found in nature are of the L-configuration and it is essential, there ⁇ fore, that amino acids used as food and feed additives are also of the L-configuration since the corresponding D-forms or isomers cannot be metabolized by living cells and will interfere with normal cell metabolism and cell function.
• D-amino acids can, however, also be utilized to advantage, for example, by incorporating such unnatural isomers of amino acids into pharmacologically active com- pounds, the activity of which may be due to or enhanced by a moiety of unnatural chirality in its molecular structure.
• Ph represents, for example, phenyl
• an enzyme i.e., an amino acid amidase, a so-called amino peptidase, is utilized for con ⁇ verting amino acid amides into the corresponding amino acids.
• amino acid amides used in the process illustrated are made available by chemical synthesis from achirale starting materials via racemates of amino acid nitriles, the consequence being that the amino acid amides used in the process described are racemic mixtures.
• the enzyme used in the process is, however, chirale and, therefore, capable of distinguishing between the two isomeric forms of the amino acid amide.
• the amino acids generated in the course of the amino peptidase catalyzed reaction are of the L-configuration while the amino acid amides remaining in the reaction mixture after completion of the enzymatic conversion are of the D-con- figuration.
• These two, chemically distinct species can be separated by conventional methods and the enantiomeric pure amino acid amides thus obtained can subsequently be hydrolyzed by chemical means to provide optically pure D- amino acids.
• the method disclosed in the above U.S. patent specifications serves, therefore, as a means for the preparation of optically pure L-. as well as D-amino acids.
• the process of the present invention is characterized in that the conversion of amino nitriles into the corresponding amino acids or amino acid amides is effected with a nitrilase which preferentially converts one of the two enantiomeric forms of the amino nitrile into the corresponding amino acid or amino acid amide.
• the process of the invention is based on the surprising observation that enantioselective nitrilases can be found and used under conditions which serves to generate, from racemic amino nitriles, amino acids and amino acid amides containing an excess of one enantiomer. Even though it is preferred only to obtain the desired compound, normally a mixture containing an excess of the desired compound is obtained. -The essential features of this invention are illustrated in the following Scheme 2:
• the amino nitrile used as starting material is present in the form of a mixture of the D- and L-form of the amino nitrile, for example, in equal amounts.
• the nitrilase applied according to the process of this invention converts, however, preferentially one of these two enantiomers into either the corresponding amino acid amide or, directly, into the corresponding amino acid.
• the reaction mixture obtained by the enzymatic conversion contains an excess of one of the two enantiomers, i.e., the amino acid or the amino acid amide.
• the entire racemic mixture of amino nitriles can, according to this invention, be converted into a reaction mixture containing an excess of one enantiomer of an amino acid or an amino acid amide.
• the compounds which can be prepared by the process of this invention can be represented by the general formula I
• R represents indolyl; benzyl; benzyloxy; lower alkyl; all optionally substituted by hydroxy, mercapto, amino, halogen, phenyl, phenoxy, benzyl or lower alkylthio; or phenyl optionally substituted by one or more of the following substituents: hydroxy, amino, halogen, carboxy or lower alkoxy; and X represents hydroxy or amino; or salts thereof.
• the starting material is an amino nitrile of the general formula II
• R is as defined above, or a salt thereof.
• R examples of the substituent designated R are as follows: methyl, isopropyl, propely butyl, phenyl, p- hydroxyphenyl, benzyl, 1-hydroxyethyl, mercaptomethyl, methylthiomethyl, benzyloxy and phenoxymethyl.
• R is indolyl or benzyl optionally substituted by one or more of the following groups: hydroxy, amino and/or lower alkoxy.
• lower alkyl designates alkyl con- taining less than 8, preferably less than 5, carbon atoms.
• lower alkoxy contains less than 8, preferably less than 5, carbon atoms.
• the enzymatic process may, according to this invention, be carried out, for example, in a batch-wise fashion by stirring a mixture of the nitrilase and the amino nitrile in an aqueous solution under control of the pH value and temperature of the reaction mixture.
• the reaction temperature may be between the freezing point of the reaction medium and about 65°C, preferably between 20 and 45°C, most preferred about 37°C.
• organic solvents can be utilized, to increase the solubility of the reactants, such solvents being, for example, alcohols such as ethanol, methanol, isopropanol or tertiary butanol or organic solvents such as dioxane, N,N-dimethylformamide, dimethylsulfoxide or hexamethylphosphorous triamide.
• the reaction may also be carried out in a two-phase system using a suspension of reactants or two immicible solvents like, for example, water and a hydrocarbon such as hexane or .cyclohexane.
• the nitrilase applied in the process of this invention may be a purified enzyme, a crude enzyme solution, microbial cells exhibiting the desired activity or a homogenate of cells. If required, the enzyme may be used in an immobilized state or in a chemically modified form to ensure a good stability and reactivity of the applied enzyme under the reaction conditions utilized.
• the process of this invention can be carried out at neutral ' or at an alcaline pH value to ensure rapid intercon- version of one of the two enantiomeric forms into the other of the two enantiomeric forms of the amino nitriles used as starting material in the enzymatic process. This intercon- version can also take place at a pH value below 7 or it can be ensured by applying an amino nitrile racemase. Hence, pre ⁇ ferentially, the pH value is from about 6 to about 13.
• the nitrilases used by the process of this invention are enzymes exhibiting a different activity towards the two enantiomeric forms of amino nitriles.
• nitrilases exhibiting a strong selectivity towards one of these enantiomers are used since it is usually desired that the amino acids or amino acid amides prepared by the process of this invention contain a large excess of one of the two enantiomers.
• the excess of one of the two enantiomeric forms of the amino acid or amino acid amide is greater than 25%. Accordingly, it is preferable to test nitrilases prior to use for conversion of a given amino nitrile.
• This test can be carried out, for example, by exposing the amino nitrile in question to the enzyme preparation and by, subsequently, " isolating, after conversion of a small amount of the amino nitrile, the amino acid amide and/or amino acid formed, for example, by high pressure liquid chromatography, and by analyzing the optical purity of the isolated compounds.
• this test is carried out at various degrees of conversion of the applied amino nitrile.
• the enzymes for use in the process of this invention may be isolated from microorganisms, plants or animals.
• enzymes of microbial origin are utilized, such microorganisms being bacteria, fungi or other microorganisms.
• microbial species producing nitrilases are as follows: Species of Pseudomonas, Gluconobacter, Acetobacter, Achromobacter, Acinetobacter, Citrobacter, Enterobacter, Erwinia, Escherichia, Klebsiella, Proteus, Serratia, Yersinia, Aeromonas, Vibrio, Staphylococcus, Streptococcus, Clostridium, Leuconostoc, Cellulomonas, Microbacterium, Propionibacterium, Mycobacterium, Streptomyces, Chaetomella, Septoria, Diplodia, Phoma, Conothyrium, Myrothecium, Pestalotia, Melancon
• LMD Laboratory of Microbiology
• FRI Fermentation Research Institute
• CBS Centraalbureau voor Schimmelcultures
• the desired amino acid amide or amino acid is isolated from the reaction mixture in a manner known per se, for example, by precipitation, optionally after adjustment of the acidity, or evaporation.
• a preparation of an enantioselective aminonitrile hydratase was prepared by cultivating nitrilase producing strain No. 311 (deposited in May 1986 at the National
• NCIB Collection of Industrial Bacteria (NCIB) under the number NCIB 12256) in a modified M9 medium (c.f. Maniatis et. al. , Molecular Cloning, A Laboratory Manual, CSH, 1982) containing 1% glucose, 0.05% yeast extract and 0.5% acetonitrile as substitute for ammonium chloride.
• the biomass generated was harvested after three days of growth at 37°C, washed thoroughly with phosphate buffer (0.1 M, pH 7) and finally stored as a suspension in said buffer. This suspension was used as the enzyme solution in the following examples.
• a solution of racemic leucine aminonitrile was prepared in the following manner:
• Enzymatic hydrolysis of the aminonitrile was subsequently performed by adding 0.1 ml of enzyme solution per 0.3 ml of the solution of the aminonitrile, stirring of the resulting mixture for 1 hour, removing the enzyme by centrifugation, and finally adsorbing the product and eluating it from an ion-exhange resin.
• the amide isolated in this fashion was found to contain an enantiomeric excess of the L-amide of 40%.
• a solution of leucine amino nitrile was made and treated with the enzyme solution described above in a manner analogous to that described in Example 1.
• the enzyme was removed by centrifugation after which pH of the reaction mixture was adjusted to 11 by addition of a 2 M sodium hydroxide solution.
• the pH of the reaction mixture was adjusted to its initial value and mixed with the biocatalyst. This procedure was carried out 5 times during a total reaction period of 6 hours after which conversion of the aminonitrile into the amino acid was complete as determined by thin layer chromatography.
• the amino acid was then isolated by ion-exchange chromatography and found to contain an enantiomeric excess of 35%. '
• L-valine amide was prepared from isobutyraldehyde in a manner analogous to that described in Example 1. The enantiomeric excess of the L-amide in the reaction mixture was found to "toe 35%.
• Example 4
• L-valine was prepared from isobutyraldehyde in a manner analogous to that described in Example 2. The enantiomeric excess of the L-amino acid was found to be 30 ⁇ %.

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Citations (4)

• 1985
  • 1985-06-11 DK DK261685A patent/DK261685A/da not_active Application Discontinuation
• 1986
  • 1986-06-10 JP JP61503306A patent/JPS63500004A/ja active Pending
  • 1986-06-10 WO PCT/DK1986/000061 patent/WO1986007386A1/en not_active Application Discontinuation
  • 1986-06-10 EP EP86903274A patent/EP0228392A1/en not_active Withdrawn
  • 1986-06-10 AU AU59652/86A patent/AU5965286A/en not_active Abandoned

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