ENZYMATIC L-ASPARTYL-L-PHENYLALANINE ALKYL ESTER PRODUCTION

Abstract: The invention relates to a method of producing L-aspartyl-L-phenylalanine alkyl ester comprising reacting L-aspartic acid alpha ester or amide with L-phenylalanine alkyl ester in the presence of an enzyme which cleaves aspartic acid from the alpha ester or amide to yield L-aspartyl-L-phenylalanine alkyl ester by condensation.

Description: This invention relates to a method of producing L-aspartyl-L-phenylalanine alkyl ester (abbreviated as APM hereafter). APM is a peptide which is noted as a sweetener in recent years. It is well known that the processes for production of APM or L-aspartyl-L-phenylalanine (AP) include a chemical synthesizing process and an enzymatic synthesizing process. The chemical synthesizing process for the production of APM comprises condensing N-protected L-aspartic acid anhydride and L-phenylalanine methylester (PM) to obtain N-protected APM. The protective group is removed afterwards. The enzymatic synthesizing process comprises exerting the effect of a protein-decomposing enzyme on N-protected L-aspartic acid and PM to obtain N- protected APM or the PM adduct of N-protected APM and then removing the protective group to form APM. However, both processes require the complicated steps of introducing the protective groups and removing the same. (See GB2,092,161A). The art also teaches a process for producing APM without using protective groups (JP 83/126,796) which is a microbiological synthetic process using one of Pseudomonas, Torulopsis, Rhodotoryla, and Sporobolomyces, but this is not always suitable for industrial production because of extremely low yields. A more direct unprotected route is employed wherein a microorganism or an enzyme therefrom can bring around a direct formation of APM from L-aspartic acid and PM. (Japanese Patent application No. 75559/1983). However, a difficulty of this process for producing APM using L-aspartic acid without a protective group is that the reaction of L-aspartic acid and PM to form APM is an equilibrium reaction, and the equilibrium prevents the substrates from being converted efficiently to APM thus giving poor yields. While some improvement in yield was achieved in later references using the L-phenylalanine ester residue of an alcohol (EP 154,472) the reaction remains equilibrium driven and hence relatively low yields occur. The present invention improves the yields of production without the equilibrium problems of the unblocked route or routes employing nonderivatized aspartic acid. Accordingly, the invention relates to a method of producing L-aspartyl-L-phenylalanine alkyl esters comprising reacting in a an organic solvent-containing, optionally aqueous medium, non-N-protected L-aspartic acid alpha ester (LAE) or L-aspartic acid alpha amide (LAA) with L-phenylalanine alkyl ester (LPAE) in the presence of an enzyme, microorganism containing the enzyme or enzyme containing fraction of the microorganism or enzyme immobilized to solid supports where the enzyme is capable of forming non-N-protected L-aspartyl-L-phenylalanine alkyl ester by condensation of L-aspartic acid alpha ester or L-aspartic acid alpha amide and L-phenylalanine alkyl ester. The invention relates to the production of APM starting from L-aspartic acid alpha ester or alpha and and L-phenylalanine alkyl ester. Alpha esters of L-aspartic acid are well known in the art and can be made for example by the methods of J. Kovacs et.al., J. Org. Chem. 26, 1084 (1961). Preferred alpha esters include a residue of an alcohol, a substituted or unsubstituted phenol, a thiol or an alkyl ester; also, it is contemplated that other forms of L-aspartic acid alpha ester or alpha amide could be used. A preferred other form would be L-aspartic acid dialkylester. Such compounds are known within the art. Such additional groups could then be removed by means known in the art. Alpha amides are made by reacting the aspartic alpha methyl ester with ammonia in methanol under conditions known in the art. Other methods are known in the art for making amides and can also be utilized. Amide group at the alpha position can be derived from, for example, NH₃ or R-NH₂ or R₂NH or R₃N where R contains an aromatic or aliphatic structure. Preferred amide is aspartic amide. Preferred alkyl ester is the methyl ester. L-pehnylalanine alkyl esters are well known in the art especially the lower (1-6) alkyl esters. A preferred lower alkyl ester of L-phenylalanine is the methyl ester. The process is carried out by reacting L-aspartic acid alpha ester or alpha amide with L-phenylalanine alkyl ester in an aqueous organic media in the presence of an enzyme capable of condensing the alpha ester or alpha amide of L-aspartic acid to form the condensation product APM. Reactions are carried out at suitable temperatures, preferably within the range of 25-45° C for a period of about 1 to 10 days. The reaction is carried out at a pH of roughly 4-9. A preferred pH is about 8. The actual amounts of starting reactants are of course relative with approximately stoichiometric amounts reacting to form APM and preferably for optimum results such amounts at any relative concentration is preferred. However, more or less of one or the other reactant can be used as well as selecting more than one L-aspartic acid ester or amide or more than one L-phenylalanine alkyl ester. Enzymes selected preferably have a preference for the alpha ester or amide bonds of L-aspartic acid and will preferably not hydrolyze the bonds (especially ester) of L-phenylalanine alkyl ester and other L-aspartic acid bonds or the APM product. A preferred enzyme is the extracellular protease (obtained from Sigma Chemical Co.) of Staphylococcus aureus strain V8 and mutant variants and genetically altered forms of that protease which retains the same function. The amino acid sequence of the N-terminal region of the enzyme was previously known (G.R. Drapeau, (1978) Canadian Journal of Biochemistry 56 534-44). However, the complete amino acid and encoding DNA sequence of the mature enzyme is given below (see also Carmona et al, Nucleic Acids Research, 15 , 16, (1987), 6757). It is also known in the art that site specific changes in codons; i.e., other than naturally occurring or random mutations or alterations can be made to enzymes which can alter specific activity, reaction rate, reaction specificity Kcat, Km stability to organic solvents and temperature and the like. Such modifications for site specific changes at specific codons are well known in the art and intended to be a part of this invention when selecting enzymes. Important site specific changes would occur at or near the active site, for example near the catalytic residues of an enzyme, or the face of the enzyme, or at some other amino acid at or near the outer portion of the amino acid. Additionally, disulfide bonds can also be introduced for stabilizing the enzyme. Alternatively, the microorganism containing the enzyme or a fraction of the microorganism containing the enzyme may be used. Immobilized enzymes can also be used. The reaction of the enzyme of LAE or LAA with PAE in the presence of the appropriate selected enzyme yields the condensation product APM. Where enzymes are used from microorganisms or fractions of microorganisms, such microorganisms can be obtained by using ordinary culture media. Further, reactants may be added at the beginning or during the process of cultivation of the cells. The culture media to be used for the microorganisms are ordinary ones containing usual carbon and nitrogen sources and inorganic ions. Moreover, the addition of trace amounts of organic nutritive substances such as vitamins and amino acid often brings about desirable results. The carbon sources suitable for use herein include carbohydrates such as glucose and sucrose, organic acids such as acetic acid, and alcohols. The nitrogen sources suitable for use herein include ammonia gas, aqueous ammonia and ammonium salts. The inorganic ions are suitably selected from e.g. magnesium ion, phosphoric acid ion, potassium ions and iron ion, as necessary. The cultures are suitably conducted under aerobic conditions at pH 4-9, preferably about pH 8, at suitable temperatures controlled within the range of 25-45° C, and for about 1-10 days. The microorganisms which can be used in this invention include the whole culture solutions obtained after completion of cultivation, microorganisms separated from the culture solutions, or washed microorganisms. Also, the microorganisms which can be used may be freeze-dried, acetone-dried, contacted with toluene, surfactants, etc., treated with lysozyme, exposed to ultrasonic waves or mechanically ground, and enzyme protein fractions obtained from these cell-treating materials having enzymic activity. Fixed cells of these microorganisms, insolubilized materials of treated cells, etc. may also be used. As aqueous media, there can be used those containing water, buffers, and organic solvents such as ethanol. Moreover, nutritive elements needed for the growth of microorganisms, anti-oxidants, surfactants, coenzymes, hydroxylamine and metallic ions, organic solvents such as DMSO etc. can be added to the aqueous media if necessary. When the whole culture solutions, culture cells or treated cell materials of the above-mentioned microorganisms are brought directly into contact with the reactants to exert the action thereon, an aqueous medium is prepared by dissolving or suspending reactants and the culture solution, culture cells, or treated cell materials, and is controlled suitably at a temperature of 10-70° C and pH 4-9, and allowed to stand for awhile or stirred. The APM thus produced can be separated and purified by the known separation processes. The APM obtained is determined with an amino-acid analyzer. Example 1 Aqueous solution of L-phenylalanine methyl ester and L-aspartic acid alpha methyl ester were made and adjusted to pH 8.0. These solutions were then mixed with Dimethyl Sulfoxide (DMSO) so that final concentration of L-phenylalanine methyl ester, L-aspartic acid alpha methyl ester and DMSO were 0.1M, 0.5M and 50% respectively. A solution of the V-8 enzyme described earlier was then added to a final concentration of 0.5 mg/ml and the reaction mixture allowed to stand at room temperature for 24 hours. Analysis by HPLC of the product based on PM converted to APM was about 33%.

Claims: A method for producing L-aspartyl-L-phenylalanine alkyl esters comprising: a) reacting in an organic solvent-containing medium non-N-protected L-aspartic acid alpha ester or L-aspartic acid alpha amide with L-phenylalanine alkyl ester in the presence of an enzyme, microorganism containing the enzyme, enzyme containing fraction of a microorganism, or enzyme immobilized on solid support, said enzyme being capable of forming L-aspartyl-L-phenylalanine alkyl ester by condensation of the non-N-protected L-aspartic acid alpha ester or L-aspartic acid alpha amide and L-phenylalanine alkyl ester. A method according to claim 1 wherein the selected enzyme is the extracellular protease of Staphylococcus aureus strain V8, or a mutant variant or genetically altered form thereof which retains the same function. A method according to claim 1 wherein the enzyme selected has an N-terminus corresponding to that of the amino acid sequence: A method according to any one of claims 1, 2 and 3 wherein L-aspartic acid methyl ester is used. A method according to any one of claims 1 to 4 wherein L-phenylalanine methyl ester is used. A method according to any one of the preceding claims wherein the L-aspartic acid alpha ester or alpha amide is also a beta ester or amide, the method further comprising removal of the beta ester or amide to yield L-aspartyl-L-phenylalanine alkyl ester. A method according to any one of the preceding claims wherein the enzyme selected has greater specificity for the L-aspartic acid alpha ester or alpha amide than for the L-phenylalanine alkyl ester. A method according to any one of the preceding claims wherein purified enzyme is used. A method according to any one of the preceding claims wherein the reaction is carried out at about pH 8.

Inventors: BOSTON, MATTHEW G., POULOSE, AYROOKARAN J.
Applicants: GENENCOR INTERNATIONAL, INC.
Application year: 1987
Main classification: C12P21
IPC codes: C07K5