Process for producing L-arginine by fermentation

Abstract: L-arginine is produced in high yields by culturing an L-arginine-producing microorganism belonging to the genus Brevibacterium or the genus Corynebacterium in a liquid culture medium, producing and accumulating L-arginine in the culture medium and collecting L-arginine from the culture medium, provided that an L-arginine-producing microorganism is used, which has resistance to X-guanidine, wherein X is an aliphatic chain or an aliphatic chain derivative.

Description: L-Arginine is an important component of drugs for stimulating liver functions, amino acid infusion, total amino acid preparations, etc. The present invention relates to an improved process for producing L-arginine by fermentation. In order to impart L-arginine productivity to microorganisms belonging to the genus Brevibacterium or the genus Corynebacterium it is known to provide the microorganisms with resistance to 2-thiazolealanine (hereafter simply referred to as 2-TA), arginine hydroxamate, etc. It is also known that the productivity of L-arginine is improved by imparting resistance to sulfa drugs or argininol resistance, resistance to chemicals such as 8-azaguanine, α-amino-β-hydroxyvaleric acid, etc., in addition to the chemical resistance described above, and by imparting auxotrophy for amino acids such as L-histidine, L-proline, L-threonine, L-tryptophan, L-lysine, etc. In order to reduce the production costs of L-arginine, it is important to improve the fermentation yield. The problem to be solved by the present invention is to provide a fermentation process which allows the production of L-arginine in higher yields. As a result of investigations to improve known microorganisms belonging to the genus Brevibacterium or the genus Corynebacterium and capable of producing L-arginine and to find strains causing a further improved fermentation yield, it has been found that strains capable of producing L-arginine in a higher yield than conventional L-arginine-producing strains are found among strains having resistance to X-guanidine (wherein X is an aliphatic chain or an aliphatic chain derivative) (hereafter simply referred to as X-GN). The present invention relates to a process for producing L-arginine which comprises culturing an L-arginine-producing microorganism belonging to the genus Brevibacterium or the genus Corynebacterium in a liquid culture medium, producing and accumulating L-arginine in the culture medium and collecting L-arginine from the culture medium, wherein an L-arginine-producing microorganism is used, which has resistance to X-guanidine, wherein X is an aliphatic chain or an aliphatic chain derivative. The microorganims used in the present invention are variants belonging to the genus Brevibacterium or the genus Corynebacterium, capable of producing L-arginine and having X-GN resistance. To obtain the variants of the present invention, L-arginine productivity may previously be imparted to wild strains described below and X-GN resistance may then be imparted thereto; alternatively , X-GN resistance may be first imparted and L-arginine productivity may then be imparted. The compounds of the formula X-GN are guanidines having aliphatic chains, such as butenylguanidine, hexylguanidine, octylguanidine, etc. and derivatives of guanidines having aliphatic chains such as 4-methyl-3-butenylguanidine, etc. Wild strains which can be parent strains of the variants of the present invention are known as bacteria belonging to the genus Brevibacterium or the genus Corynebacterium, especially as Coryneform L-glutamic acid producing bacteria and are exemplified by the following bacteria. Brevibacterium divaricatum ATCC 14020 Brevibacterium flavum ATCC 14067 Brevibacterium lactofermentum ATCC 13869 Brevibacterium saccharolyticum ATCC 14066 Corynebacterium acetoacidophilum ATCC 13870 Corynebacterium glutamicum ATCC 13032 For mutation to produce variants of the present invention from these parent strains, a conventional method of mutation which comprises contacting these strains with N-methyl-N′-nitro-N-nitrosoguanidine, etc. can be appropriately used. The isolation of the variant of the present invention can be effected by collecting strains which can grow in a medium containing X-GN. A concrete mutation method to produce the variant of the present invention and the relationship between the concentration of octylguanidine (hereafter simply referred to as O-GN) as one of the compounds X-GN and the growth of the strain are shown below. Method of mutation Bacteria cells of Brevibacterium flavum AJ 11169, FERM P-4161 (2-TA resistant strain derived from ATCC 14067) and Corynebacterium glutamicum AJ 12092, FERM P-7273 (2-TA resistant strain derived from ATCC 13032), which had been grown on bouillon agar slants at 30°C for 24 hours, were suspended in M/30 phosphate buffer solution in a cell density of 10⁸ to 10⁹/ml. To the cell suspension were added 500 µg/ml of N-methyl-N′-nitro-N-nitrosoguanidine. The mixture was maintained at 30°C for 20 minutes. Then the cells were collected by centrifugation. After thoroughly washing with M/30 phosphate buffer solution, the cells were inoculated on a medium having the following composition and cultured at 31.5°C for 4 to 10 days. Composition of Medium (pH 7.0) Component Content Glucose 1.0 g/dl Urea 0.2 g/dl KH₂PO₄ 0.1 g/dl MgSO₄.7H₂O 0.1 g/dl FeSO₄.7H₂O 0.002 g/dl MnSO₄.7H₂O 0.002 g/dl Biotin 100 µg/l Thiamine hydrochloride 100 µg/l O-GN 0.1 g/dl Agar 2.0 g/dl (O-GN = Octylguanidine) From the strains grown in the agar medium, Brevibacterium flavum AJ 12429, FERM BP-2227(2-TA resistant, O-GN resistant) and Corynebacterium glutamicum AJ 12430, FERM BP-2228(2-TA resistant, O-GN resistant) were obtained as having high productivity of L-arginine. The O-GN resistance of the thus obtained variants was compared with that of the parent strains. Onto a medium composed of 0.5 g/dl of glucose, 0.15 g/dl of urea, 0.15 g/dl of ammonium sulfate, 0.3 g/dl of KH₂PO₄ 0.1 g/dl of K₂HPO₄, 0.01 g/dl of MgSO₄.7H₂O, 0.1 mg/dl of CaCl₂.2H₂O, 100 µg/l of biotin, 100 µg/l of thiamine hydrochloride, 0.002 g/dl of FeSO₄.7H₂O, 0.002 g/dl of MnSO₄.7H₂O and O-GN in the amount shown in the table and adjusted to pH of 7.0, there was inoculated a suspension of the cells in sterile water, which were obtained by culturing on a slant of natural medium (1 g/dl of peptone, 1 g/dl of yeast extract and 0.5 g/dl of NaCl, pH 7.0) for 24 hours. After culturing for 24 hours, the growth degree was determined in terms of turbidity. In many cases, the yield increases by further imparting to the aforesaid variants properties already known to improve the productivity of L-arginine, such as sulfaguanidine resistance, argininol resistance or 8-azaguanine resistance. Media used for culturing such variants are conventional media containing carbon sources, nitrogen sources, inorganic ions, substances satisfying the auxotrophy described above and, if necessary, other organic trace nutrients including vitamins, etc. As carbon sources, there are preferably used carbohydrates such as glucose, sucrose, etc., organic acids such as acetic acid, etc. As nitrogen sources, there are preferably used ammonia water, ammonia gas, ammonium salts, etc. As inorganic ions, potassium ions, sodium ions, magnesium ions, phosphate ions, and the like are appropriately added to media, depending upon necessity. The incubation is preferably conducted under aerobic conditions. When the incubation is carried out while adjusting the pH of the medium to a range from 4 to 8 at a temperature of from 25°C to 37°C, more preferable results can be obtained. Thus, during a culture period of 1 to 7 days, remarkable amounts of L-arginine are produced and accumulated in the media. For collecting L-arginine from the culture solution, conventional methods such as a method using an ion exchange resin, etc. can be used. The present invention is further described with reference to the following example. Example A medium containing 10 g/dl of glucose, 7 g/dl of (NH₄)₂SO₄, 0.1 g/dl of KH₂PO₄, 0.04 g/dl of MgSO₄.7H₂O, 1 mg/dl of FeSO₄.7H₂O, 1 mg/dl of MnSO₄.4H₂O, 100 µg/l of thiamine.HCl, 100 µg/l of biotin, 60 mg of soybean protein acid hydrolysate (calculated as total nitrogen) and 5 g/dl of calcium carbonate (separately sterilized) was adjusted to pH 7.0 and 20 ml of the medium was charged into a 500 ml flask with a shoulder followed by sterilization by heating. One platinum loop of the strain shown in Table 1 was inoculated on the medium and cultured while shaken for 4 days at 31.5°C. L-Arginine was produced and accumulated in the culture solution of each strain in the amount shown in Table 2. Property Amount of L-Arginine Accumulated (g/dl) Brevibacterium flavum AJ 11169 (FERM P-4161) 2-TA r 1.9 Brevibacterium flavum AJ 12429 (FERM BP-2227) 2-TA r .O-GN r 3.6 Corynebacterium glutamicum AJ 12092 (FERM P-7273) 2-TA r 1.7 Corynebacterium glutamicum AJ 12430 (FERM BP-2228) 2-TA r .O-GN r 3.4 2-TA r : 2-thiazolealanine resistance O-GN r : octylguanidine resistance AJ 12429 was cultured by the method described above to give 1 liter of the culture solution. The culture solution was centrifuged to remove the cells and the like. The supernatant was passed through a weakly acidic ion exchange resin "Amberlite" C-50 (NH₄ type). After washing the resin with water, L-arginine was eluted with 2 N NH₄OH and the eluate was concentrated. From the concentrate, 19.5 g of L-arginine was obtained as crude crystals.

Claims: A process for producing L-arginine which comprises culturing an L-arginine-producing microorganism belonging to the genus Brevibacterium or the genus Corynebacterium in a liquid culture medium, producing and accumulating L-arginine in the culture medium and collecting L-arginine from the culture medium, characterised in that said L-arginine-producing microorganism has resistance to X-guanidine, wherein X is an aliphatic chain or an aliphatic chain derivative.

Inventors: OHTSUKA NOBORU C O KAWASAKI PL, TAKEUCHI HIROSHI C O KAWASAKI, TSUCHIDA TAKAYASU C O KAWASAKI, UCHIBORI HARUO C O KAWASAKI PL, OHTSUKA, NOBORU, TAKEUCHI, HIROSHI, TSUCHIDA, TAKAYASU, UCHIBORI, HARUO, OHTSUKA, NOBORU, C/O KAWASAKI PLANT, AJINOMOTO, TAKEUCHI, HIROSHI, C/O KAWASAKI PLANT, AJINOMOTO, TSUCHIDA, TAKAYASU, C/O KAWASAKI PLANT, AJINOMOTO, UCHIBORI, HARUO, C/O KAWASAKI PLANT, AJINOMOTO
Applicants: AJINOMOTO KK, AJINOMOTO CO., INC.
Application year: 1990
Main classification: C12P13
IPC codes: C12R1, C12P13