PROCESS FOR PRODUCING L-GLUTAMIC ACID BY FERMENTATION AND MUTANT MICROORGANISMS FOR USE THEREIN

Abstract: A fermentation process is disclosed for producing L-­ glutamic acid in high yield using microorganisms belonging to the genus Corynebacterium or Brevibacterium having the abili­ ty to produce L-glutamic acid and which have or have been en­ dowed with a resistance to α-naphthoquinone, a resistance to antibiotics of the type which inhibit energy metabolism, or a re­ sistance to precursors in the biosynthesis of ubiquinone.

Description: The present invention relates to a process for producing L-glutamic acid by fermentation and microorganisms for use therein. L-glutamic acid is an important amino acid which is commercially useful as a food additive. Processes for producing L-glutamic acid by fermentation are known using strains of various microorganisms of the genera Corynebacterium and Brevibacterium in particular strains having a nutritional requirement for various compounds, or a sensitivity or resistance to various chemicals. The yields of these known processes are comparatively low and a need exists for processes for producing L-glutamic acid in higher yields at low cost. As a result of various studies for obtaining strains having an increased L-glutamic acid productivity, it has been found that L-glutamic acid-producing microorganism strains of the genus Corynebacterium or Brevibacterium and endowed with a resistance to ∝-naphthoquinoline, have a remarkably improved ability to produce L-glutamic acid. Accordingly, the present invention provides a process for the production of L-glutamic acid which comprises culturing an L-glutamic acid producing microorganism belonging to the genus Corynebacterium or Brevibacterium in a nutrient medium until L-glutamic acid is accumulated in the resulting culture liquor, and recovering L-glutamic acid therefrom wherein the microorganism used has a resistance to ∝-naphthoquinoline. In a second aspect the invention also extends to biologically pure cultures of the microorganisms per se . Suitable mutants for use in this invention may be obtained by using a mutant inherently having an ability to produce L-glutamic acid or an improved mutant thereof as a parent strain and imparting thereto the specified resistance. Alternatively, a suitable mutant may be prepared by a reverse process, i.e. by imparting the above-mentioned ability to produce L-glutamic acid to a mutant already possessing the specified resistance. The mutant microorganisms useful in carrying out the present invention can be obtained by conventional mutation techniques using for example mutagens such as ultraviolet ray irradiation, x-ray irradiation, radioactive ray irradiation and a treatment with chemical mutagens. Treatment with N-nitro-N'-methyl-N-nitrosoguanidine (hereinafter referred to as NTG) is the preferred technique. In addition, the mutants used in this invention may well have or be endowed with other specific properties such as specific nutritional requirements, drug resistance, drug sensitivity and drug dependence, in addition to the resistance already specified. Preferably, the microorganism used in carrying out this invention may, in addition to a resistance to ∝-naphthoquinoline, have a resistance to one or more antibiotics of the type which inhibit energy metabolism, and/or a resistance to one or more compounds being compounds which are precursors in the biosynthesis of ubiquinone. As used herein the term "antibiotics which inhibit energy metabolism" means that the antibiotics have influences on the electron transport of respiratory chain or oxidative phosphorylation. Examples of such antibiotics include inhibitors of the electron transport system such as antimycin A, uncoupling agents which allow electron transport to continue but prevent the phosphorylation of ADP to ATP, such as gramicidin S, valinomycin, etc., and inhibitors of oxidative phosphorylation which prevent the ATP-forming mechanism from utilizing the high-energy intermediate or state generated by electron transport, e.g. antibiotics such as oligomycin, rutamycin, etc. Furthermore, as used herein the term "precursors for ubiquinone biosynthesis" means that the precursors are biosynthetic intermediates of ubiquinone which plays an important role in the electron transport of respiratory chain for acquiring the energy. Exemplary of such precursors are o-hydroxycinnamate (o-coumarate) and its fluoride, m-hydroxycinnamate (m-coumarate) and its fluoride, p-hydroxycinnamate (p-coumarate) and its fluoride, phenyl pyruvate, p-hydroxyphenyl pyruvate and its fluoride, phenyl acetate, p-hydroxyphenyl lactate and its fluoride, cinnamate, benzoate, p-hydroxybenzoate and its fluoride, and p-hydroxybenzaldehyde and its fluoride. Strains mutated as above mentioned are screened by culturing in a nutrient medium and a strain having the ability to produce L-glutamic acid in greater yiedls than its parent strain is selected and used in this invention. A specific example of the procedure for obtaining a suitable strain is given in the following description. Procedure Corynebacterium glutamicum ATCC 13032 is treated with NTG in a conventional manner. A suspension of the treated cells is cultured at 30°C in an agar medium containing 0.5 g/dl enzyme extract, 0.7 g/dl meat extract, 1 g/dl peptone, 0.3 g/dl NaCl, 2 g/dl agar and 100 µg/ml ∝-naphthoquinoline. Among the formed colonies, a culture test of L-glutamic acid is performed to choose a mutant having excellent productivity. Thus, L-glutamic acid-producing Corynebacterium glutamicum CQ-306 (hereinafter referred to as CQ-306) having a resistance to ∝-naphthoquinoline is obtained. In a similar manner, Brevibacterium lactofermentum BQ-13 (hereinafter referred to as BQ-13) is obtained from Brevibacterium lactofermentum ATCC-13869. These CQ-306 and BQ-13 strains were deposited with ARS Culture Collection Research Fermentation Laboratory under the Budapest Treaty on July 21, 1983 and assigned the international accession Nos. NRRL B-15331 and NRRL B-15530, respectively. Either a synthetic or natural medium may be used as the medium for the present invention, so long as it properly contains a carbon source, nitrogen source, inorganic materials and other necessary nutrients which are assimilable by the strain utilized. As the carbon source, various carbohydrates such as glucose, fructose, maltose, monnose, glycerol, sucrose, starch, starch hydrolyzate and molasses, sugar alcohols, such as glycerol and sorbitol, organic acids, such as acetic acid, fumaric acid, lactic acid, pyruvic acid, gluconic acid, formic acid, butyric acid and malic acid, lower alcohols such as ethanol and methanol, and hydrocarbons, etc. may be used. As the nitrogen source, ammonia, inorganic and organic ammonium salts, such as ammonium chloride, ammonium sulfate, ammonium acetate, ammonium phosphate, ammonium carbonate and ammonium nitrate, urea, amines, other nitrogen-containing compounds such as peptone, meat extract, yeast extract, corn steep liquor, casein hydrolyzate, acid hydrolyzate of soybean meal, various microbial cells, digest of microbial cells, etc., may be used. As the inorganic materials, potassium dihydrogen phosphate, dipotassium hydrogen phosphate, magnesium phosphate, magnesium sulfate, sodium chloride, ferrous sulfate, manganese sulfate, copper sulfate, calcium carbonate, etc. are used. When a microorganism to be used in the present invention requires specific nutrients for growth, an appropriate amount of the nutrients is added to the medium. In some cases, these nutrients are added as components of the natural substances exemplified as the nitrogen source. Further, the productivity of L-glutamic acid by the present microorganism can be, in some cases, enhanced by adding other various additives, for example, various antibiotics such as streptomycin, penicillin G and rifampicin, antioxidant, such as ∝-tocopherol, surfactants such as polyoxyethylene sorbitan-mono-palmitate, amino acids such as methionine, lysine, cysteine and aspartic acid, biotin, acetic acid, oleic acid, adenine, etc., to the medium. Culturing is carried out under aerobic conditions, for example, by shaking culture, agitation submerged culture, etc. The temperature for culturing is generally 20-40°C, and the pH of the medium is in a range of 3 to 9, and is preferably maintained at around neutrality, but culturing can be carried out under conditions which are out of this range so long as the microorganism used can grow. The pH of the medium is adjusted with calcium carbonate, acid or alkali solution, ammonia, pH buffering agent, etc. Usually, after culturing for 1 to 4 days, L-glutamic acid is formed and accumulated in the resulting culture liquor. After the completion of culturing, precipitates such as cells, are removed from the culture liquor and L-glutamic acid can be recovered from the culture liquor by use of the conventional methods, such as ion-exchange resin treatment, concentration, adsorption and salting-out in combination. Practice of specific embodiments of the invention is illustrated by the following representative examples. Example 1 As seed strains, four strains of Corynebacterium glutamicum ATCC-13032, CQ-306 strain, Brevibacterium lactofermentum ATCC-13869 and BQ-13 strain are used. Each of these strains is inoculated into a seed medium (pH 7.2) comprising 4 g/dl glucose, 2 g/dl polypeptone, 0.5 g/dl yeast extract, 0.15 g/dl KH₂PO₄, 0.05 g/dl K₂HPO₄ , 0.05 g/dl MgSO₄.7H₂O, 100 µg/ml biotin and 0.3 g/dl urea. Culturing is carried out at 30°C with shaking for 24 hours. Then, 1 ml of the culture liquor is put into a 300 ml-Erlenmeyer flask containing 20 ml of a fermentation medium having the composition described below. Culturing is carried out at 30°C with shaking for 3 days. The results are shown in Table 1. Composition of Fermentation Medium: 10 g/dl glucose, 0.5 g/dl meat extract, 3 g/dl ammonium sulfate, 0.15 g/dl KH₂PO₄, 0.05 g/dl K₂HPO₄, 0.05 g/dl MgSO₄.7H₂O, 500 µg/l thiamine hydrochloride, 10 mg/l FeSO₄.7H₂O, 10 mg/l MnSO₄.4H₂O, l mg/l CuSO₄.5H₂O, 0.5 g/dl urea, 3 g/dl CaCO₃ (pH 7.2), sterilized at 120°C for 10 minutes. Example 2 The same procedures as described in Example 1 are repeated except that 10 g/dl (calculated as glucose) molasses is used in place of glucose of the fermentation medium and 5 U/ml of penicillin G is added at the initiation of the culturing. The results are shown in Table 2.

Claims: A process for producing L-glutamic acid, which comprises culturing an L-glutamic acid producing microorganism belonging to the genus Coryne bacterium or Brevibacterium in a nutrient medium until L-glutamic acid is accumulated in the resulting culture liquor, and recovering the L-glutamic acid therefrom, characterised in that the microorganism used has or is endowed with a resistance to ∝-naphthoquinoline. A process according to claim 1, wherein the microorganism used also has a resistance to one or more antibiotics of the type which inhibit energy metabolism being selected from oligomycin, antimycin A, rutamycin, and valinomycin, and/or said microorganism has a resistance to one or more compounds being compounds which are precursors in the biosynthesis of ubiquinone. A process according to claim 1 or 2, characterised in that the microorganism used is a strain of the species Corynebacterium glutamicum or Brevibacterium lactofermentum. A process according to claim 3, characterised in that the microorganism is Corynebacterium glutamicum CQ-306, NRRL B-15531 or Brevibacterium lactofermentum BQ-13, NRRL B-15530. A process according to any one of the preceding claims, characterised in that the culture is conducted at 20 to 40°C for 1 to 4 days. A biologically pure culture of a microorganism having the identifying characteristics of: Corynebacterium glutamicum NRRL B-15531, or Brevibacterium lactofermentum NRRL B-15530.

Inventors: HATTORI, KIYOJI, KINO, KUNIKI, KOTANI, YUKINOBU
Applicants: KYOWA HAKKO KOGYO CO., LTD.
Application year: 1984
Main classification: C12P13
IPC codes: C12P13