Method of producing L-glutamic acid by fermentation

Abstract

The present invention provides a method of producing L-glutamic acid by fermentation, comprising the steps ofculturing a mutant of an L-glutamic acid-producing microorganism of the genus Brevibacterium or Corynebacterium which has lower .alpha.-ketoglutaric acid dehydrogenase activity compared with the wild strains from which said mutant is derived, in a liquid nutrient culture medium containing biotin at a concentration of 10 to 1000 .mu.g/l without adding a biotin activity-suppressing substance thereto;producing and accumulating L-glutamic acid in the culture solution; andrecovering L-glutamic acid from said culture solution.According to the method of the present invention, it is possible to industrially produce L-glutamic acid by fermentation in a more economical and efficient manner.

Description

FIELD OF THE INVENTION

The present invention relates to a method of producing L-glutamic acid by fermentation. L-Glutamic acid is an important amino acid in foods, medicines, chemicals, etc.

DESCRIPTION OF THE PRIOR ART

Microorganisms belonging to the genus Brevibacterium or Corynebacterium are known to produce L-glutamic acid. A mutant strain of a L-glutamic acid-producing microorganism of the genus Brevibacterium has also been reported. The .alpha.-ketoglutaric acid dehydrogenase activity of the mutant was shown to be lower than that of its parent strain; however, the productivity of L-glutamic acid by the mutant was demonstrated to be similar to the productivity of the parent strain (Agric. Biol. Chem. (1980) 44: 1897-1904; Agric. Biol. Chem. (1982) 46: 493-500).

L-glutamic acid is industrially produced by fermentation using microorganisms belonging to the genus Brevibacterium or Corynebacterium. Various methods of culturing these microorganisms have been employed in order to maximize the productivity of L-glutamic acid. For example, it is known that biotin is an essential factor for the growth of these microorganisms and that the concentration of biotin or a biotin-active substance in the culture medium greatly influences the excretion of L-glutamic acid by these microorganisms. When these microorganisms are cultivated in media containing restricted amounts of biotin or a biotin-active substance required for the growth of the microorganisms, the production of L-glutamic acid increases. However, the common carbon source used in culture media is inexpensive material such as cane molasses or beet molasses which contains too much biotin to give high yields of L-glutamic acid. Accordingly, a penicillin such as penicillin G, F, K, O, V, X, etc., or a surfactant composed of a higher fatty acid or a derivative thereof such as sucrose monopalmitate, polyoxyethylene sorbitan monopalmitate, etc., must be added to the medium to suppress the biotin activity at the early logarithmic growth phase of the microbial cells. It is highly desirable to find a method for the industrial production of L-glutamic acid which is not influenced by the amount of biotin in the culture media.

SUMMARY OF THE INVENTION

Accordingly, one object of the present invention is to provide an improved method for the industrial production of L-glutamic acid by fermentation which is more economical and more efficient than previously known methods.

DETAIL DESCRIPTION OF THE PREFERRED EMBODIMENTS

The present inventors have now discovered that, when a mutant of a L-glutamic acid-producing microorganism of the genus Brevibacterium or Corynebacterium, which has lower .alpha.-ketoglutaric acid dehydrogenase activity compared with the wild strain from which said mutant is derived, is cultured in a liquid nutrient medium containing an excess amount of biotin, L-glutamic acid is produced at a high accumulation and at a high yield without the necessity of adding to the medium a biotin activity-suppressing substance.

Thus, the present invention provides a method of producing L-glutamic acid by fermentation, comprising culturing a mutant of a L-glutamic acid-producing microorganism of the genus Brevibacterium or Corynebacterium, wherein said mutant has a lower .alpha.-ketoglutaric acid dehydrogenase activity compared with the wild strain from which said mutant is derived, in a liquid nutrient medium containing biotin at a concentration of from 10 to 1000 .mu.g/l without adding a biotin activity-suppressing substance thereto; producing and accumulating L-glutamic acid in the culture solution; and recovering L-glutamic acid from said culture solution.

Suitable mutants useful in accordance with the present invention may be any mutant which is induced from a L-glutamic acid producing microorganism of the genus Brevibacterium or Corynebacterium and which has a lower .alpha.-ketoglutaric acid dehydrogenase activity compared with the wild strain from which it is derived. The mutant may also have other characteristics which enhance the productivity of L-glutamic acid including resistance to compounds having vitamin-P activity, resistance to Decoyinine or Tubercidin, increased superoxide dismutase activity, as well as other such characteristics as described in U.S. Pat. Nos. 4,334,020, 4,389,483 and 4,529,697, incorporated herein by reference.

The following mutant strains may be used:

Brevibacterium lactofermentum (Corynebacterium glutamicum) AJ 12821 (FERM BP-4172); Brevibacterium flavum (Corynebacterium glutamicum) AJ 12822 (FERM BP-4173) and Corynebacterium glutamicum AJ 12823 (FERM BP-4174).

These mutants can be obtained by artificially mutating L-glutamic acid-producing strains belonging to the genus Brevibacterium or Corynebacterium. The parent strain is not particularly limited so long as it belongs to the genus Brevibacterium or Corynebacterium and is capable of producing L-glutamic acid. The following wild strains may be used:

Brevibacterium lactofermentum (Corynebacterium glutamicum) ATCC 13869; Brevibacterium flavum (Corynebacterium glutamicum) ATCC 14067; Brevibacterium divaricatum (Corynebacterium glutamicum) ATCC 14020; Brevibacterium roseum ATCC 13825; Brevibacterium saccharolyticum ATCC 14066; Corynebacterium glutamicum ATCC 13032; Corynebacterium acetoacidophilum ATCC 13870; Corynebacterium acetoglutamicum ATCC 15806; Corynebacterium lilium (Corynebacterium glutamicum) ATCC 15990 and Corynebacterium melassecola ATCC 17965.

The mutants according to the present invention may be obtained by mutating wild type strains according to conventional techniques such as ultraviolet irradiation, X-ray irradiation, radioactive irradiation or treatment with a mutagenic agent. Typically, the mutants are obtained by mutating wild type strains with 250 .mu.g/ml of N-methyl-N'-nitro-N-nitrosoguanidine at 30.degree. C. for 20 minutes. Mutants may alternatively be obtained by recombinant DNA technique.

Suitable methods for isolating the mutants according to the present invention from the wild type cells after mutagenesis are not particularly limited and include, for example, a method of isolating strains which cannot grow on a medium containing L-glutamic acid as the only carbon and nitrogen source, but are capable of growing on a medium in which the L-glutamic acid in the above-stated medium has been substituted with succinic acid and ammonia (see Agric. Biol. Chem.(1982) 46: 493-500, incorporated herein by reference).

Mutants useful in accordance with the present invention have .alpha.-ketoglutaric acid dehydrogenase activities which are lower than the wild strains from which they are derived. The degree to which their activities are lowered is not necessarily limited, but it is preferable to use a mutant whose activity is between 1/5 and 1/500 of that of the parent strain, and more preferably between 1/10 and 1/100 thereof.

In order to produce and accumulate L-glutamic acid using the obtained mutant, the cultivation is effected in a liquid nutrient medium wherein a material containing an excess amount of biotin, such as cane molasses or beet molasses, is used as the carbon source. Alternatively, a liquid medium in which biotin is added in an excess amount to a carbon source, such as a saccharified solution or acetic acid may be used.

Conventionally, when the cultivation is effected in a liquid medium containing an excess amount of biotin, it has been necessary to add a substance thereto to suppress the biotin activity such as a penicillin such as penicillin G, F, K, O, V or X or a surfactant composed of a higher fatty acid or a derivative thereof such as sucrose monopalmitate or polyoxyethylene sorbitan monopalmitate in order to produce L-glutamic acid at a high yield. However, if a mutant according to the present invention is used which has a lower .alpha.-ketoglutaric acid dehydrogenase activity than the wild strain from which it is derived, then L-glutamic acid may be produced and accumulated at a high yield without adding the biotin activity-suppressing substance as mentioned above, even in a liquid nutrient medium which contains biotin at a high concentration of 10 to 1000 .mu./l.

The liquid nutrient media used to cultivate the mutants according to the present invention may also contain, in addition to a carbon source, appropriate nutrients such as a nitrogen source or an inorganic ion. Useful nitrogen sources include ammonium salt, ammonia water, ammonia gas, urea, or any other compounds which are normally used as nitrogen sources for L-glutamic acid fermentation. Useful inorganic ions include phosphate, magnesium or any other alkaline or alkaline earth metal salt. In addition, trace nutrients such as thiamine may be added appropriately as necessary.

The cultivation is suitably effected under aerobic conditions. The temperature is suitably maintained at from 24.degree. C. to 42.degree. C. The pH is suitably maintained at from 5 to 9. The pH may be adjusted with an inorganic or organic compound or an acidic or alkaline substance such as urea, calcium carbonate or ammonia gas.

The method of recovering L-glutamic acid from the culture solution may involve an appropriate combination of known methods such as ion-exchange resin treatment or crystallization.

Having generally described this invention, a further understanding can be obtained by reference to certain specific examples which are provided herein for purposes of illustration only and are not intended to be limiting unless otherwise specified.

EXAMPLES

Obtaining Mutants

Cells of Brevibacterium lactofermentum ATCC 13869 were subjected to conventional mutagenetic treatment using N-methyl-N'-nitro-N-nitrosoguanidine (250 .mu.g/ml, 30.degree. C., 20 minutes), after which the cultivation was effected on an agar medium of the composition shown in Table 1 to form colonies.

TABLE 1______________________________________ Ingredients Concentration______________________________________ Polypeptone 10 g/l Yeast extract 10 g/l NaCl 5 g/l Acetic acid 1 g/l Agar 20 g/l pH 7.0______________________________________ The replica method was then used to isolate therefrom mutants incapable of growing on a medium containing L-glutamic acid as the only carbon and nitrogen source. That is, colonies were picked up which was unable to grow on a medium of the composition shown in Table 2 even after culturing at 30.degree. C. for days, but which grew under the same conditions on the medium where sodium L-glutamate in Table 2 was substituted with 10 g/l of succinic acid and 1 ml/l of ammonia. TABLE 2______________________________________Ingredients Concentration______________________________________Sodium L-glutamate 10 g/lKH.sub.2 PO.sub.4 10 g/lMgSO.sub.4.7H.sub.2 O 0.4 g/lFeSO.sub.4.7H.sub.2 O 0.5 g/lMnSO.sub.4.4H.sub.2 O 8.1 mg/lThiamine hydrochloride 100 .mu.g/lBiotin 300 .mu.g/lAgar 20 g/lpH 7.0______________________________________ Many mutants were thus obtained which have lower .alpha.-ketoglutaric acid dehydrogenase activity compared with the parent wild strain, Brevibacterium lactofermentum ATCC 13869. Brevibacterium lactofermentum AJ 12821 (FERM BP-4172) was selected as the representative strain. By the similar method, Brevibacterium flavum AJ 12822 (FERM BP-4173) and Corynebacterium glutamicum AJ 12823 (FERM BP-4174) were obtained using the wild strains, Brevibacterium flavum ATCC 14067 and Corynebacterium glutamicum ATCC 13032, as the parent strains, respectively. Cultures of Brevibacterium lactofermentum AJ 12821, Brevibacterium flavum AJ 12822, and Corynebacterium glutamicum AJ 12823 were deposited with the National Institute of Bioscience and Human-technology, Agency of Industrial Science and Technology, Ministry of International Trade and Industry, 1-3, Higashi 1-Chome, Tsukuba-shi, Ibaraki-ken 305, Japan under the provisions of the Budapest Treaty on Feb. 4, 1993, and may be accessed under the identification numbers FERM BP-4172, FERM BP-4173, and FERM BP-4174, respectively.

The .alpha.-ketoglutaric acid dehydrogenase activity of each of the above-stated three mutants and their parent strains was measured in the following manner. Twenty milliliters of a medium of the composition shown in Table 3 was poured into a 500 ml shaking flask, and subjected to sterilization at 115.degree. C. for 10 minutes.

TABLE 3______________________________________Ingredients Concentration______________________________________Glucose 50 g/l(NH.sub.4).sub.2 SO.sub.4 45 g/lKH.sub.2 PO.sub.4 1 g/lMgSO.sub.4.7H.sub.2 O 1 g/lFeSO.sub.4.7H.sub.2 O 10 mg/lMnSO.sub.4.4H.sub.2 O 10 mg/lSoy protein acid-hydrolyzate 400 mg/l(as total nitrogen content)Thiamine hydrochloride 200 .mu.g/lBiotin 300 .mu.g/lCaCO.sub.3 50 g/lpH 7.0______________________________________ The cells of the strain being tested were inoculated into the medium and cultured at 31.5.degree. C. for 36 hours. The cells were harvested from the resulting culture by centrifugation and washed, after which they were suspended in 20 ml of a 0.1M TES (N-Tris (hydroxymethyl) methyl-2-aminoethane sulfonic acid)-NaOH buffer solution containing 30% glycerol. Then the cells were treated by ultrasonication, and the supernatant obtained by centrifugation thereof was subjected to gel filtration using a Sephadex G-25 column to produce a crude enzyme solution. Next, the .alpha.-ketoglutaric acid dehydrogenase activity of the crude enzyme solution was determined using the reaction solution of the composition shown in Table 4. TABLE 4______________________________________Ingredients Concentration______________________________________TES-NaOH 100 mMCoenzyme A 0.2 mMThiamine pyrophosphate 0.3 mM.alpha.-ketoglutaric acid 1 mML-cysteine 3 mMMnSO.sub.4.7H.sub.2 O 1 mMMgCl.sub.2 5 mM3-acetylpyridine adenine dinucleotide 1 mMpH 7.7______________________________________ The reaction was initiated by adding 0.1 ml of the crude enzyme solution to 1.5 ml of the reaction solution, and the change in absorbance at 365 nm was traced at room temperature. A reaction solution lacking .alpha.-ketoglutaric acid was used as the control. The results are shown in Table 5. TABLE 5______________________________________ .alpha.-ketoglutaric acid dehydrogenase activityStrains tested (unit/mg protein)______________________________________Brevibacterium lactofermentumATCC 13869 4.5AJ 12821 0.06Brevibacterium flavumATCC 14067 4.8AJ 12822 0.32Corynebacterium glutamicumATCC 13032 3.9AJ 12823 0.24______________________________________ (One unit is defined as the amount of enzyme required to consume 1 .mu.mol of 3-acetylpyridine adenine dinucleotide per minute in the reaction mixture).

As clearly shown here, all of the three mutants obtained by the methods described above had considerably lower .alpha.-glutaric acid dehydrogenase activities than the respective parent wild strains.

Example 1

A seed culture medium was prepared with the composition shown in Table 6, and 20 ml portions thereof were placed in 500 ml shaking flasks, and then subjected to sterilization. Each of the three mutants and their parent strains were inoculated into this medium, and the cultivation was effected using a reciprocal shaker for 15 hours while keeping the temperature at 31.5.degree. C. This shall hereunder be referred to as the seed culture.

TABLE 6______________________________________Ingredients Concentration______________________________________Glucose 50 g/lUrea 4 g/lKH.sub.2 PO.sub.4 1 g/lMgSO.sub.4.7H.sub.2 O 0.4 g/lFeSO.sub.4.7H.sub.2 O 10 mg/lMnSO.sub.4.4H.sub.2 O 10 mg/lThiamine hydrochloride 200 .mu.g/lBiotin 30 .mu.g/lSoy protein acid-hydrolysate 0.9 g/l(as total nitrogen content)pH 7.0______________________________________

Next, a culture medium was separately prepared with the composition shown in Table 7, and 20 ml portions thereof were poured into 500 ml shaking flasks and then subjected to sterilization at 115.degree. C. for 10 minutes. The concentration of biotin in this medium was 60 .mu.g/l.

TABLE 7______________________________________Ingredients Concentration______________________________________Cane molasses 60 g/l(as glucose)KH.sub.2 PO.sub.4 1 g/lMgSO.sub.4.7H.sub.2 O 1 g/lThiamine hydrochloride 100 .mu.g/lpH 7.0______________________________________

The above mentioned seed culture was inoculated into the respective medium at a proportion of about 10 volume %, and the cultivation was effected at 31.5.degree. C. using a reciprocal shaker. A solution of urea at a concentration of 450 mg/ml was added in small amounts during the cultivation to maintain the pH of the culture solution at between 6.0 and 8.5. The fermentation was terminated at 36 hours and the amounts of L-glutamic acid accumulated in the culture solutions were measured.

As shown in Table 8, the accumulation of L-glutamic acid was very low with the wild strains due to the presence of excess biotin in the medium, while the mutants having low .alpha.-ketoglutaric acid dehydrogenase activity all produced and accumulated large amounts of L-glutamic acid. PG,14

TABLE 8______________________________________ Amounts of L-glutamic acidStrains tested accumulated (g/l)______________________________________Brevibacterium lactofermentumATCC 13869 7.5AJ 12821 34.0Brevibacterium flavumATCC 14067 6.1AJ 12822 32.1Corynebacterium glutamicumATCC 13032 6.8AJ 12823 30.8______________________________________

Example 2

A culture medium was prepared with the composition shown in Table 9, and 300 ml portions thereof were poured into 1 liter jar fermenters and then subjected to sterilization at .degree. C. for 10 minutes. The concentration of biotin in this medium was 150 .mu.g/l.

TABLE 9______________________________________Ingredients Concentration______________________________________Cane molasses 150 g/l(as glucose)KH.sub.2 PO.sub.4 1 g/lMgSO.sub.4.7H.sub.2 O 1 g/lThiamine hydrochloride 100 .mu.g/lAnti-foaming agent 20 .mu.g/lpH 7.0______________________________________

The seed culture of each of the strains according to Example 1 were inoculated into the medium at a proportion of volume %, and the cultivation was effected at 31.5.degree. C. with aeration and agitation. The pH of the culture solution was adjusted to 7.8 using ammonia gas. The fermentation was terminated at 32 hours and the amounts of L-glutamic acid accumulated in the culture solutions were measured.

As shown in Table 10, the accumulation of L-glutamic acid was very low with the wild strains due to the presence of excess biotin, while the mutants having low .alpha.-ketoglutaric acid dehydrogenase activity all produced and accumulated large amounts of L-glutamic acid.

TABLE 10______________________________________ Amounts of L-glutamic acidStrains tested accumulated (g/l)______________________________________Brevibacterium lactofermentumATCC 13869 18.3AJ 12821 78.3Brevibacterium flavumATCC 14067 16.2AJ 12822 77.1Corynebacterium glutamicumATCC 13032 14.8AJ 12823 77.2______________________________________

Example 3

Culture media were prepared with the composition shown in Table 11 with biotin added at concentrations of 3, 10, 50, 300 and 1000 .mu.g/l, and 300 ml portions thereof were poured into 1 liter jar fermenters and then subjected to sterilization at 120.degree. C. for 10 minutes.

TABLE 11______________________________________Ingredient Concentration______________________________________Glucose 100 g/lKH.sub.2 PO.sub.4 1 g/lMgSO.sub.4.7H.sub.2 O 1 g/lFeSO.sub.4.7H.sub.2 O 10 mg/lMnSO.sub.4.4H.sub.2 O 10 mg/lSoy protein acid-hydrolyzate 0.4 g/l(as total nitrogen content)Thiamine hydrochloride 100 .mu.g/lAnti-foaming agent 20 .mu.l/lpH 7.0______________________________________

The seed culture of each of the strains according to Example 1 were inoculated into the respective media at a proportion of 10 volume %, and the cultivation was effected at 31.5.degree. C. with aeration and agitation. The pH of the culture solutions was adjusted to 7.8 using ammonia gas. The fermentation was terminated at 30 hours and the amounts of L-glutamic acid produced and accumulated in the culture solutions were measured.

As shown in Table 12, in the L-glutamic acid-producing culture media in which biotin was limited to a concentration of 3 .mu.g/l, the amounts of accumulation of L-glutamic acid were about the same for both the parent wild strains and the mutants. On the other hand, in the media which contained biotin at concentrations of 10 to 1000 .mu.g/l, the production of L-glutamic acid by the wild strains was subjected to inhibition, while the mutants having lower .alpha.-ketoglutaric acid dehydrogenase activity all produced and accumulated large amounts of L-glutamic acid.

TABLE 12______________________________________ Amounts of Amounts of L- biotin added glutamic acidStrains tested (.mu.g/l) accumulated (g/l)______________________________________Brevibacterium lactofermentum 3 49.2ATCC 13869 10 25.6 50 15.3 300 5.2 1000 3.1Brevibacterium lactofermentum 3 51.3AJ 12821 10 51.5 50 52.4 300 53.3 1000 53.6Brevibacterium flavum 3 46.8ATCC 14067 10 23.1 50 13.1 300 4.2 1000 3.8Brevibacterium flavum 3 47.5AJ 12822 10 48.1 50 49.4 300 50.2 1000 50.6Corynebacterium glutamicum 3 49.8ATCC 13032 10 25.7 50 12.5 300 5.1 1000 4.6Corynebacterium glutamicum 3 48.5AJ 12823 10 48.6 50 49.5 300 50.8 1000 51.0______________________________________

Having now fully described the invention, it will be apparent to one of ordinary skill in the art that many changes and modifications can be made thereto without departing from the spirit or scope of the invention as set forth herein.

Claims

1. A method of producing L-glutamic acid by fermentation, comprising the steps of

culturing a mutant of an L-glutamic acid-producing microorganism of the species Corynebacterium glutamicum which has an .alpha.-ketoglutaric acid dehydrogenase activity which is between 1/5 and 1/500 of that of the wild strain from which said mutant is derived, in a liquid culture medium comprising biotin at a concentration of at least 10 .mu.g/l in the absence of a biotin activity-suppressing substance selected from the group consisting of penicillin G, penicillin F, penicillin K, penicillin O, penicillin V, penicillin X, sucrose monopalmitate, and polyoxyethylene sorbitan monopalmitate;

producing and accumulating L-glutamic acid in said culture medium in an amount greater than that produced by said wild strain; and

recovering said L-glutamic acid from said culture medium;

whereby the accumulation of L-glutamic acid is not inhibited by any concentration of biotin in the culture medium within he range of 10 to 1,000 .mu.g/l.

2. The method according to claim 1, where said concentration of biotin is of from 10 to 1000 .mu.g/l.

3. The method according to claim 1, wherein said mutant is selected from the group consisting of

Brevibacterium lactofermentum (Corynebacterium glutamicum) AJ 12821 (FERM BP-4172);

Brevibacterium flavum (Corynebacterium glutamicum) AJ 12822 (FERM BP-4173) and

Corynebacterium glutamicum AJ 12823 (FERM BP-4174).

4. The method according to claim 1, wherein said .alpha.-ketoglutaric acid dehydrogenase activity of said mutant is between 1/10 and 1/100 of that of said wild strain.

5. The method according to claim 1, wherein said mutant is derived from a wild strain of Corynebacterium glutamicum selected from the group consisting of Corynebacterium glutamicum ATCC 13869; Corynebacterium glutamicum ATCC 14067; Corynebacterium glutamicum ATCC 14020; and Corynebacterium glutamicum ATCC 15990 and Corynebacterium glutamicum ATCC 13032.

6. A method of producing L-glutamic acid by fermentation, comprising the steps of

culturing a mutant of an L-glutamic acid-producing microorganism of the species Corynebacterium glutamicum, wherein said mutant is selected from the group consisting of Corynebacterium glutamicum AJ 12821 (FERM BP-4172), Corynebacterium glutamicum AJ 12822 (FERM BP-4173) and Corynebacterium glutamicum AJ 12823 (FERM BP-4174), in a liquid culture medium comprising biotin at a concentration of 10 to 1000 .mu.g/l;

producing and accumulating L-glutamic acid in the culture medium; and

recovering said L-glutamic acid from said culture medium; whereby the accumulation of L-glutamic acid is not inhibited by any concentration of biotin in the culture medium within the range of 10 to 10,000 .mu.g/l.

7. The method of claim 6, wherein said biotin activity-suppressing substance is selected from the group consisting of penicillin G, penicillin F, penicillin K, penicillin O, penicillin V, penicillin X, sucrose monopalmitate, and polyoxyethylene sorbitan monopalmitate.