METHOD OF PRODUCING L-PHENYLALANINE BY FERMENTATION, AND BACTERIA THEREFOR

Abstract: L-Tryptophan and L-phenylalanine auxotrophic mutant strains of the genus Bacillus which are capable of vigorous growth on culture medium containing enough of m-fluorophe­ nylalanine and/or cinnamic acid to suppress growth of the par­ ent strain produce more L-phenylalanine by aerobic fermenta­ tion of generally conventional aqueous media than the best L-phenylalanine producing related microorganisms available heretofore.

Description: METHOD OF PRODUCING L-PHENYLALANINE BY FERMENTATION, AND BACTERIA THEREFOR The present invention relates to a method of producing L-phenylalanine (hereinafter simply referred to as phenylalanine) by a fermentation process. Heretofore, there has been known, as a methdd of producing phenylalanine, a method involving the use of tyrosine auxotrophy of bacteria belonging to the genus Brevibacterium or the genus Micrococcus (Japanese Published Examined Patent Application 6345/62), a method involving the use of a mutant requiring tyrosine for the growth thereof and having resistance to S-methyltryptophane, a method involving the use of mutants having resistance to phenylalanine analogues (Japanese Published Examined Patent Application 28712/76), a method involving the use of a decoininesensitive mutant (Japanese Published Examined Patent Application 64793/71), etc. On the other hand, with respect to the genus Bacillus, a method involving the use of an L-tyrosine auxotrophic mutant (Japanese Published Examined Patent Application 6345/62), a method involving the use of a mutant having tryptophane auxotrophy and resistance to p-fluorophenylalanine and to '3-2-thienylalanine (Japanese Published Unexamined Patent Application 67488/73), etc. are known. However, amounts of phenylalanine accumulated are merely about 0.2 - 0.4 g/dl in these methods and much inferior to the phenylalanine-producing bacteria belonging to the genus Brevibacterium or the genus Corynebacterium described above. For this reason, growth of strains has been scarecely investigated for the purpose of industrial production of phenylalanine. In fact, no bacteria having high productivity of phenylalanine is known. The present inventors have conducted the growth of phenylalanine-producing bacteria for the purpose of developing a method of industrially producing phenylalanine by microorganisms belonging to the genus Bacillus and, as have have r discovered that by imparting auxotrophy for both tryptophane and tyrosine as well as resistance to m-fluoro phenylalanine (mFP) and/or cinnamic acid, a strain which produces and accumulates phenylalanine in substantial amounts can be obtained. These mutants also show resistance to compounds chemically analogous to phenylalanine. Specific examples of such phenylalanine analogues include, 13-amino-13-phenyl- propionic acid, o-fluorophenylalanine, p-fluorophenylalanine, 13-2-thienylalanine, ss-3-thienylalanine, ss-2-furylalanine, - ss-3-furylalanine, o-aminophenylalanine, p-aminophenylalanine, m-aminophenylalanine, a-amino-a-phenylethanesulfonate, ss-2- pyrrolalanine, l-cyclopentene-l-alanine, l-cyclohexene-lalanine, 13-4-pyridylalanine, 13-4-pyrazolylalanine, p-nitrophenylalanine, 13-4 -thiazolealanine, cyc lohexylalanine, 2amino-4-methyl-4-hexenoic acid, S-(1,2-dichlorovinyl)- cysteine, o-chlorophenylalanine, m-chlorophenylalanine, p- chlorophenylalanine, o-bromophenylalanine, m-bromophenylalanine, p-bromophenylalanine, m-fluorotyrosine, 3-nitrotyrosine, ss-phenylserine and 3-iodotyrosine. The present invention has been accomplished based on this discovery. Microorganisms which may be used in the present invention include the following mutants: Bacillus subtilis AJ 12095 FERM P-7286 FERM BP- 607 (Trp, Tyr, mFP ) Bacillus subtilis AJ 12096 RERM P- 7287 FERM BP-608 (Trp, Tyr, cin Bacillus subtilis AJ 12097 FERM:P-7288 FERM BP- 609 (Trp, Tyr, mFPr, cinr) Trp : tryptophane auxotrophy Tyr : tyrosine auxotrophy mFPr: resistance to m-fluorophenylalanine cinr : resistance to cinnamic acid The mutants identified above by FERM P number were originally deposited on October 1, 1983 at the Fermentation Research Institute, Agency of Industrial Sciences and Technology, Ministry of International Trade and Industry (FRI), 1-3, Migashi 1-chome, Yatabe-machi, Tsukuba-gun, Ibaragi 305, Japan; and have been accorded the FERMP number indicated above. The mutant deposits were then converted into deposits under the Budapest Treaty on September 17, 1984, and have been accorded the corresponding FERM BP numbers. The mutants employed in the present invention may be obtained by using a wild strain belonging to the genus Bacillus or known phenylalanine-producing bacteria as a parent strain, and subjecting it to conventional operations to induce mutation, for example, by irradiation with ultraviolet rays or x-rays, or treatment with a chemical such as N-methyl-N'-nitro-N-nitrosoguanidine (referred to as NG), nitrous acid, etc. Experiment 1 Phenylalanine-producing bacterium AJ 12094 (FERM P-7285) having auxotrophy for both tryptophane and tyrosine, which had been induced from Bacillus subtilis AJ 11708, was cultured in yeast-buillon agar slant medium. The grown bacterium was collected and suspended in 1/50M phosphate buffer (pH 7.0; containing 169/ml of cells). To the suspension NG (NG concentration, 200 ijg/ml) was added followed by maintaining room temperature for 30 minutes. After thoroughly washing the NG-treated cells with the same phosphate buffer, the cells were inoculated on minimum agar plate medium containing 1000 ug/ml of mFP shown in Table 1 and cultured at 31.50C for 7 days. Table 1. Composition of Minimum Medium (pH 7.0) Component Concentration Glucose 20 g/l Ammonium sulfate 5 g/l Urea 2 g/l KH2PO4 1 g/l MgSO4.7H2O 1 g/l Fe , Mn ions 2 ppm each Biotin 50 ug/l Thiamine hydrochloride 200 ug/l L-Tryptophane 150 mg/l L-Tyrosine 150 mg/l Among colonies grown on the agar plate, big colonies were harvested as mFP-resistant strains. Many of the thus obtained resistant strains were found to have superior phenylalanine productivity to the parent strain, from which strain AJ 12095 (FERM BP-607) having the highest productivity was chosen. By similar mutating operations, AJ 12096 (FERM BP-608) was induced by imparting cinnamic acid resistance to AJ 12094 and AJ 12097 (FERM BP- 609) by imparting cinnamic acid resistance to AJ 12095 (FERM BP-607). Experiment 2 In test tubes, 4.0 ml each of the minimum medium (Table 1) containing mFP or cin in such concentrations as shown in Table 2 was separately charged followed by sterilization by heating. A determined amount of the above-mentioned mutant strains was inoculated on the medium and subjected to shake culture at 31.50C for 24 hours. Each of the culture solutions was diluted with water by 26 times and the absorbancy at 562 nm was measured to determine the degree of growth. The results are shown in Table 2. In Table 2, a relative growth value is shown when the degree of growth without adding any chemical is made 100. Table 2. Resistance to Chemical Chemical (ug/ml) Strain mFP cin 0 500 1000 2000 0 200 500 1000 AJ 12094 100 40 0 0 100 25 0 0 AJ 12095 100 100 100 90 100 30 0 0 (FERM BP-607j AJ 12096 100 45 0 0 100 100 55 10 (FERM BP-608) AJ 12097 100 100 100 95 100 100 95 50 (FERM BP-609) The culture medium employed in the present invention is a conventional nutrient medium containing a carbon source, a nitrogen source, inorganic salts, L-tyrosine, L-tryptophane, and, if necessary, organic minor nutrients, such as other amino acids, vitamins, nucleic acids, etc. 'As the carbon source, it may be sufficient as long as the mutant used can utilize it, for example, sugars such as glucose, fructose, sucrose, maltose, hydrolysates of starch, molasses, etc. are employed. Further, alcohols such as ethanol, propanol, etc., organic acids such as acetic acid, citric acid, etc. are employed. As the nitrogen source, ammonium salts such as ammonium sulfate, ammonium chloride, ammonium phosphate, etc., inorganic or organic nitrogen sources such as nitrates, urea, ammonia, meat extract, etc. are employed. As the organic minor nutrients, amino acids, vitamins, fatty acids and nucleic acids, and further, peptone, Casamino acid, yeast extract and protein decomposates, etc. containing amino acids, vitamins, fatty acids and nucleic acids, are employed. With mutants requiring amino acids such as L-tyrosine, L-tryptophane, etc., it is necessary to supplement nutrients, etc. required. It is desired that the incubation be performed under aerobic conditions. By performing shake culture or aerial agitation culture for 1 to 4 days while controlling the pH-of the medium to 5 to 9 and the temperature at 20 to 40oC during the incubation, phenylalanine is accumulated in the culture solution in marked amounts. Harvesting phenylalanine from the culture solution may be in accordance with known methods; after separating the bacteria from the culture solution phenylalanine is harvested by concentration and crystallization, use of ion exchange resins, etc. Hereafter the present invention wll be explained with reference to the example below. Example 1 A medium for producing phenylalanine shown in Table 3 described below was prepared. 500 ml shake flasks we each charged with 20 ml of the medium and sterilized by heating at 1200C for 10 minutes. Then 10 g of calcium carbonate powder, separately sterilized by heating, was added thereto. Table 3. Composition of Phenylalanine-Producing Medium Component Content in 1.0 Liter Glucose 80.0 g Ammonium sulfate 10.0 g KC1 2.0 g KH2PO4 1.0 g MgSO4.7H2O 0.4 g Fe , Mn 2 ppm each L-Tyrosine 0.15 g L-Tryptophane 0.20 g Soybean protein decomposate* 20 ml (* T-N concentration: 4 g/dl) In each sample, a platinum loop amount of one of the phenylalanine-producing bacteria shown in Table 4 was inoculated and subjected to shake culture at 300C for 72 hours. The amount of phenylalanine produced in each culture solution was measured. The results are shown in Table 4. Table 4. Amount of L-Phenylalanine Accumulated Strain Property L-Phenylalanine (mg/ml) AJ 12094 Trp , Tyr 2.1 AJ 12095 Trp , Tyr , mFP 7.6 (FERM BP-607) AJ 12096 Trp , Tyr , cinr 7.5 (FERM BP-608) - - r r AJ 12097 Trp , Tyr , mFP , cin 10.0 (FERM BP-609)

Claims: CLAIMS 1. A method of producing L-phenylalanine which comprises culturing in a liquid medium an L-phenylalanine-producing bacterium belonging to the genus Bacillus, showing auxotrophy for both tryptophane and tyrosine and having resistance to m-fluorophenylalanine and/or cinnamic acid, and recovering L-phenylalanine which has been produced in said liquid medium. 2. A method as set forth in claim 1, wherein said bacterium is a strain of Bacillus subtilis. 3. A method as set forth in claim 2, wherein said bacterium is Bacillus subtilis FERM BP-607. 4. A method as set forth in claim 2, wherein said bacterium is Bacillus subtilis FERM BP-608. 5. A method as set forth in claim 2, wherein said bacterium is Bacillus subtilis FERM BP-609. 6. An L-phenylalanine-producing bacterium belonging to the genus Bacillus, showing auxotrophy for both tryptophane and tyrosine and having resistance to m-fluorophenylalanine and/or cinnamic acid. 7. A bacterium of claim 6 wherein said bacterium is a strain of Bacillus subtilis. 8. A bacterium of claim 7 wherein said bacterium is Bacillus subtilis FERM BP-7, 9. A bacterium of clairn 7 wherein said bacterium is Bacillus subtilis FERM BP-608. 10. A bacterium of claim 7 wherein said bacterium is Bacillus subtilis FERN BP-609.

Inventors: ENEI, HITOSHI, KAWASHIMA, HIROKI, KURAHASHI, OSAMU, TSUCHIDA, TAKAYASU
Applicants: AJINOMOTO CO., INC.
Application year: 1984
Main classification: C12P13
IPC codes: C12P13, C12R1