JPS6236676B2 - - Google Patents
Info
- Publication number
- JPS6236676B2 JPS6236676B2 JP4321880A JP4321880A JPS6236676B2 JP S6236676 B2 JPS6236676 B2 JP S6236676B2 JP 4321880 A JP4321880 A JP 4321880A JP 4321880 A JP4321880 A JP 4321880A JP S6236676 B2 JPS6236676 B2 JP S6236676B2
- Authority
- JP
- Japan
- Prior art keywords
- glutamic acid
- fermentation
- brevibacterium
- strains
- producing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- WHUUTDBJXJRKMK-VKHMYHEASA-N L-glutamic acid Chemical compound OC(=O)[C@@H](N)CCC(O)=O WHUUTDBJXJRKMK-VKHMYHEASA-N 0.000 claims description 26
- 229960002989 glutamic acid Drugs 0.000 claims description 14
- 238000000855 fermentation Methods 0.000 claims description 10
- 230000004151 fermentation Effects 0.000 claims description 10
- NZPACTGCRWDXCJ-UHFFFAOYSA-N 2-heptyl-4-hydroxyquinoline N-oxide Chemical compound C1=CC=CC2=[N+]([O-])C(CCCCCCC)=CC(O)=C21 NZPACTGCRWDXCJ-UHFFFAOYSA-N 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 241000186146 Brevibacterium Species 0.000 claims description 4
- 241000186216 Corynebacterium Species 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 4
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 claims description 2
- 235000013922 glutamic acid Nutrition 0.000 claims description 2
- 239000004220 glutamic acid Substances 0.000 claims description 2
- YBJHBAHKTGYVGT-ZKWXMUAHSA-N (+)-Biotin Chemical compound N1C(=O)N[C@@H]2[C@H](CCCCC(=O)O)SC[C@@H]21 YBJHBAHKTGYVGT-ZKWXMUAHSA-N 0.000 description 10
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 8
- 229960002685 biotin Drugs 0.000 description 5
- 235000020958 biotin Nutrition 0.000 description 5
- 239000011616 biotin Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 241000186226 Corynebacterium glutamicum Species 0.000 description 4
- 239000004202 carbamide Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 230000001580 bacterial effect Effects 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 235000013379 molasses Nutrition 0.000 description 3
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 2
- 229910001410 inorganic ion Inorganic materials 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 235000010483 polyoxyethylene sorbitan monopalmitate Nutrition 0.000 description 2
- 239000000249 polyoxyethylene sorbitan monopalmitate Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 241000219310 Beta vulgaris subsp. vulgaris Species 0.000 description 1
- 241001485655 Corynebacterium glutamicum ATCC 13032 Species 0.000 description 1
- 241000807905 Corynebacterium glutamicum ATCC 14067 Species 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- 235000021314 Palmitic acid Nutrition 0.000 description 1
- 229930182555 Penicillin Natural products 0.000 description 1
- 108010009736 Protein Hydrolysates Proteins 0.000 description 1
- 240000000111 Saccharum officinarum Species 0.000 description 1
- 235000007201 Saccharum officinarum Nutrition 0.000 description 1
- 108010073771 Soybean Proteins Proteins 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- XZAGBDSOKNXTDT-UHFFFAOYSA-N Sucrose monopalmitate Chemical compound CCCCCCCCCCCCCCCC(O)=O.OC1C(O)C(CO)OC1(CO)OC1C(O)C(O)C(O)C(CO)O1 XZAGBDSOKNXTDT-UHFFFAOYSA-N 0.000 description 1
- 235000021536 Sugar beet Nutrition 0.000 description 1
- 241000319304 [Brevibacterium] flavum Species 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 231100000350 mutagenesis Toxicity 0.000 description 1
- 239000003471 mutagenic agent Substances 0.000 description 1
- 231100000707 mutagenic chemical Toxicity 0.000 description 1
- 230000035772 mutation Effects 0.000 description 1
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 150000002960 penicillins Chemical class 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 229940001941 soy protein Drugs 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 229960000344 thiamine hydrochloride Drugs 0.000 description 1
- 235000019190 thiamine hydrochloride Nutrition 0.000 description 1
- 239000011747 thiamine hydrochloride Substances 0.000 description 1
- DPJRMOMPQZCRJU-UHFFFAOYSA-M thiamine hydrochloride Chemical compound Cl.[Cl-].CC1=C(CCO)SC=[N+]1CC1=CN=C(C)N=C1N DPJRMOMPQZCRJU-UHFFFAOYSA-M 0.000 description 1
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Description
本発明は発酵法によるL−グルタミン酸の製造
方法に関する。本発明者等は発酵法によるL−グ
ルタミン酸の製造法を改良すべく鋭意研究した結
果、ブレビバクテリウム(Brevibacterium)属
またはコリネバクテリウム(Corynebacterium)
属のL−グルタミン酸生産菌より誘導した2−ヘ
プチル−4−ヒドロキシキノリン−N−オキシド
(以下「HOQNO」と記す)に耐性を有する変異
株の中から、L−グルタミン酸の生産能が優れた
菌株を分離育成することに成功し、本発明を完成
するにいたつた。
すなわち、本発明の要旨はブレビバクテリウム
属またはコリネバクテリウム属に属し、HOQNO
に耐性を有し、かつL−グルタミン酸生成能を有
する変異株を培養して、培養液中にL−グルタミ
ン酸を生成蓄積させて、これを採取することを特
徴とする発酵法によるL−グルタミン酸の製造方
法である。以下本発明をさらに詳細に説明する。
本発明に使用するHOQNOに耐性を有する菌株
は、例えば以下の菌株がある。
ブレビバクテリウム・ラクトフエルメンタム
AJ11563(FERM−P 5471)
ブレビバクテリウム・フラバム
AJ11564(FERM−P 5472)
コリネバクテリウム・グルタミクム
AJ11565(FERM−P 5473)
これ等の菌株は、それぞれブレビバクテリウ
ム・ラクトフエルメンタムATCC13859、ブレビ
バクテリウム・フラバムATCC14067、コリネバ
クテリウムグルタミクムATCC13032を親株とし
て変異誘導したものである。
その他例えばブレビバクテリウム・デイバリカ
タム(Brevibacterium divaricatum)
ATCC14020、ブレビバクテリウム・サツカロリ
テイカム(Brevibacterium saccharoliticum)
ATCC14066、及びコリネバクテリウム・アセト
アシドフイラム(Corynebacterium
acetoacidophilum)ATCC13870等を親株として
用いても同様に変異株をつくることができる。
上記変異株の変異誘導法としては、紫外線照
射、X線照射、放射線照射、変異誘起剤処理等の
通常の方法が用いられ、例えば250μg/mlのN
−ニトロ−N′−メチル−N−ニトロソグアニジ
により30℃で20分間処理する方法等がある。
上記例示の菌株のHOQNO耐性に関する実験結
果を第1表に示す。
The present invention relates to a method for producing L-glutamic acid using a fermentation method. As a result of intensive research aimed at improving the production method of L-glutamic acid by fermentation, the present inventors discovered that Brevibacterium genus or Corynebacterium spp.
A strain with excellent L-glutamic acid production ability among mutant strains resistant to 2-heptyl-4-hydroxyquinoline-N-oxide (hereinafter referred to as "HOQNO") derived from L-glutamic acid producing bacteria of the genus We succeeded in isolating and cultivating this, leading to the completion of the present invention. That is, the gist of the present invention belongs to the genus Brevibacterium or Corynebacterium, and
A method of producing L-glutamic acid by a fermentation method characterized by culturing a mutant strain that is resistant to This is the manufacturing method. The present invention will be explained in more detail below. Bacterial strains resistant to HOQNO used in the present invention include, for example, the following strains. Brevibacterium lactofermentum AJ11563 (FERM-P 5471) Brevibacterium flavum AJ11564 (FERM-P 5472) Corynebacterium glutamicum AJ11565 (FERM-P 5473) These strains are Brevibacterium lactofermentum, respectively. fermentum ATCC13859, Brevibacterium flavum ATCC14067, and Corynebacterium glutamicum ATCC13032 as parent strains. Others such as Brevibacterium divaricatum
ATCC14020, Brevibacterium saccharoliticum
ATCC14066, and Corynebacterium acetophyllum
acetoacidophilum) ATCC 13870 or the like as a parent strain, mutant strains can be similarly created. Conventional methods such as ultraviolet irradiation, X-ray irradiation, radiation irradiation, and treatment with mutagens are used to induce mutations in the above mutant strains.
-Nitro-N'-methyl-N-nitrosoguanidi at 30°C for 20 minutes. Table 1 shows the experimental results regarding the HOQNO resistance of the above-mentioned exemplary strains.
【表】
上記の本発明のHOQNOに耐性を有する菌株を
用いてL−グルタミン酸を生成蓄積させるにはL
−グルタミン酸発酵に用いられる常法を用いて行
なえばよい。
すなわち、使用する培地としては、通常の炭素
源、窒素源、無機イオンその他の栄養素の含有す
る通常の培地が用いられる。炭素源としては例え
ばサトウキビ、甜菜からの糖汁あるいは廃糖蜜、
澱粉、加水分解物等の糖質原料等または酢酸等の
有機酸等を用いる。
窒素源としては通常のL−グルタミン酸発酵に
用いられる例えばアンモニウム塩、アンモニア
水、尿素等が用いられ、その他リン酸イオン、マ
グネシウムイオン等の無機イオンが必要に応じて
適宜使用される。又ビオチンに関しても、ビオチ
ン又はビオチン活性物質が生育の適量以下の制限
量含有する培地が用いられ、廃糖蜜等のビオチン
過剰原料を炭素源として使用するときはペニシリ
ンG、F、K、O、V、X等のペニシリン類ある
いはシユークロースモノパルミテート、ポリオキ
シエチレンソルビタン−モノパルミテート、パル
ミチン酸等の高級脂肪酸又はその誘導体よりなる
界面活性剤をビオチン抑制物質として添加する等
の常法で行なう。培養条件についても、温度30〜
40℃、pH6〜8の範囲内で好気的条件で実施する
等、常法によって実施する。
以下本発明のHOQNOに耐性を有する変異株を
用いた実施例を次に示す。
実施例 1
グルコース36mg/ml、尿素2mg/ml、
KH2PO41mg/ml、MgSO4・7aq0.4mg/ml、
FeSO4・7H2O10μg/ml、MnSO4・4H2O8μ
g/ml、大豆蛋白酸加水分解物(「味液」)5μ
l/ml、サイアミン塩酸塩100μg/、ビオチ
ン2.5μg/を含有する培地を調製しその20ml
ずつを500ml容の振盪フラスコに入れ115℃で10分
間加熱殺菌した。この培地に次に示す菌株を接種
し往復振盪により31.5℃で培養を行つた。培養
中、培養液をpH6.5ないし8.0に保つように450
mg/mlの濃度の尿素溶液を少量ずつ添加した。30
時間で発酵を終了し発酵液中に蓄積したL−グル
タミン酸の対糖収率を測定した。その結果を第2
表に示す。[Table] To produce and accumulate L-glutamic acid using the strain resistant to HOQNO of the present invention, L
- It may be carried out using a conventional method used for glutamic acid fermentation. That is, as a medium to be used, a conventional medium containing a conventional carbon source, nitrogen source, inorganic ions, and other nutrients is used. As a carbon source, for example, sugar cane, sugar juice from sugar beet or blackstrap molasses,
Carbohydrate raw materials such as starch and hydrolysates, or organic acids such as acetic acid are used. As the nitrogen source, for example, ammonium salts, ammonia water, urea, etc., which are used in ordinary L-glutamic acid fermentation, are used, and other inorganic ions such as phosphate ions and magnesium ions are used as appropriate. Regarding biotin, a medium containing biotin or a biotin active substance in a limiting amount below the appropriate amount for growth is used, and when using biotin-excess raw materials such as blackstrap molasses as a carbon source, penicillins G, F, K, O, and V are used. , X, etc., or a surfactant consisting of a higher fatty acid such as sucrose monopalmitate, polyoxyethylene sorbitan monopalmitate, palmitic acid, or a derivative thereof, as a biotin inhibitor. . As for the culture conditions, the temperature is 30~
It is carried out by a conventional method such as carried out under aerobic conditions at 40°C and pH within the range of 6 to 8. Examples using the mutant strain of the present invention having resistance to HOQNO are shown below. Example 1 Glucose 36 mg/ml, urea 2 mg/ml,
KH 2 PO 4 1mg/ml, MgSO 4・7aq0.4mg/ml,
FeSO 4・7H 2 O 10 μg/ml, MnSO 4・4H 2 O 8 μ
g/ml, soy protein acid hydrolyzate (“flavor liquid”) 5μ
Prepare a medium containing 100 μg/ml of thiamine hydrochloride and 2.5 μg/ml of biotin and add 20 ml of it.
Each sample was placed in a 500 ml shaking flask and sterilized by heating at 115°C for 10 minutes. The following bacterial strains were inoculated into this medium and cultured at 31.5°C with reciprocal shaking. During cultivation, keep the culture solution at pH 6.5 to 8.0.
A urea solution with a concentration of mg/ml was added in small portions. 30
Fermentation was completed in time, and the yield of L-glutamic acid accumulated in the fermentation liquid relative to sugar was measured. The second result is
Shown in the table.
【表】
実施例 2
甘蔗廃糖蜜を、糖として100mg/ml、KH2PO41
mg/ml、MgSO4・7H2O1mg/ml、サイアミン塩
酸塩100μg/の組成を有する培地を調製し
(pH7.0)、その30mlずつを500ml振盪フラスコに分
注し、加熱殺菌した。この培地に下記の菌株を接
種し、往復振盪機により31.5℃で培養を行つた。
培養中、培養液をpH6.5〜8.0に保つように400
mg/mlの濃度の尿素溶液を少量ずつ添加した。培
地の26培希釈液の562mμの吸光度が0.30に到達
した時にポリオキシエチレンソルビタンモノパル
ミテートを添加した。36時間で発酵を終了し、発
酵液中に蓄積したL−グルタミン酸の対糖収率を
測定した。その結果を第3表に示す。[Table] Example 2 Cane molasses, 100mg/ml as sugar, KH 2 PO 4 1
Prepare a medium with the composition of
(pH 7.0), 30 ml of each was dispensed into 500 ml shaking flasks and heat sterilized. The following bacterial strains were inoculated into this medium and cultured at 31.5°C using a reciprocating shaker. 400 to keep the culture solution at pH 6.5-8.0 during cultivation.
A urea solution with a concentration of mg/ml was added in small portions. Polyoxyethylene sorbitan monopalmitate was added when the absorbance at 562 mμ of the 26-diluted medium reached 0.30. Fermentation was completed in 36 hours, and the yield of L-glutamic acid accumulated in the fermentation liquid relative to sugar was measured. The results are shown in Table 3.
Claims (1)
ウム属に属し、2−ヘプチル−4−ヒドロキシキ
ノリン−N−オキシドに耐性を有し、かつL−グ
ルタミン酸生成能を有する変異株を培養して、培
養液中にL−グルタミン酸を生成蓄積させて、こ
れを採取することを特徴とする発酵法によるL−
グルタミン酸の製造方法。1. A mutant strain belonging to the genus Brevibacterium or Corynebacterium that is resistant to 2-heptyl-4-hydroxyquinoline-N-oxide and has the ability to produce L-glutamic acid is cultured, and the mutant strain is added to the culture solution. L-glutamic acid is produced by a fermentation method characterized by producing and accumulating L-glutamic acid and collecting it.
Method for producing glutamic acid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4321880A JPS56140895A (en) | 1980-04-02 | 1980-04-02 | Preparation of l-glutamic acid by fermentation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4321880A JPS56140895A (en) | 1980-04-02 | 1980-04-02 | Preparation of l-glutamic acid by fermentation |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56140895A JPS56140895A (en) | 1981-11-04 |
JPS6236676B2 true JPS6236676B2 (en) | 1987-08-07 |
Family
ID=12657769
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4321880A Granted JPS56140895A (en) | 1980-04-02 | 1980-04-02 | Preparation of l-glutamic acid by fermentation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS56140895A (en) |
Families Citing this family (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57115190A (en) * | 1980-12-29 | 1982-07-17 | Ajinomoto Co Inc | Preparation of l-glutamic acid by fermentation |
CA1215338A (en) * | 1983-02-25 | 1986-12-16 | Kiyoji Hattori | Process for producing l-glutamic acid by fermentation |
KR101233739B1 (en) | 2004-12-28 | 2013-02-18 | 아지노모토 가부시키가이샤 | L-glutamic acid-producing microorganism and a method for producing L-glutamic acid |
JP2010017082A (en) | 2006-10-10 | 2010-01-28 | Ajinomoto Co Inc | Method for producing l-amino acid |
JP2010041920A (en) | 2006-12-19 | 2010-02-25 | Ajinomoto Co Inc | Method for producing l-amino acid |
JP2010110216A (en) | 2007-02-20 | 2010-05-20 | Ajinomoto Co Inc | Method for producing l-amino acid or nucleic acid |
JP2010130899A (en) | 2007-03-14 | 2010-06-17 | Ajinomoto Co Inc | Microorganism producing l-glutamic acid-based amino acid, and method for producing amino acid |
JP2011067095A (en) | 2008-01-10 | 2011-04-07 | Ajinomoto Co Inc | Method for producing target substance by fermentation process |
WO2009093703A1 (en) | 2008-01-23 | 2009-07-30 | Ajinomoto Co., Inc. | Method of producing l-amino acid |
WO2011013707A1 (en) | 2009-07-29 | 2011-02-03 | 味の素株式会社 | Method for producing l-amino acid |
JP2012223091A (en) | 2009-08-25 | 2012-11-15 | Ajinomoto Co Inc | Method for producing l-amino acid |
RU2496867C2 (en) | 2011-04-25 | 2013-10-27 | Закрытое акционерное общество "Научно-исследовательский институт Аджиномото-Генетика" (ЗАО "АГРИ") | Method to produce l-amino acid of glutamate family using coryneformic bacterium |
WO2012157699A1 (en) | 2011-05-18 | 2012-11-22 | 味の素株式会社 | Immunostimulant for animals, feed containing same, and method for manufacturing same |
HUE032394T2 (en) | 2011-07-29 | 2017-09-28 | Mitsui Chemicals Inc | Microorganism having carbon dioxide fixation cycle introduced thereinto |
JPWO2013069634A1 (en) | 2011-11-11 | 2015-04-02 | 味の素株式会社 | Production method of target substance by fermentation method |
US9828618B2 (en) | 2013-01-24 | 2017-11-28 | Mitsui Chemicals, Inc. | Microorganism having carbon dioxide fixation cycle introduced thereinto |
JP5831669B2 (en) | 2013-05-13 | 2015-12-09 | 味の素株式会社 | Method for producing L-amino acid |
JP2016165225A (en) | 2013-07-09 | 2016-09-15 | 味の素株式会社 | Method for producing useful substance |
JP2016192903A (en) | 2013-09-17 | 2016-11-17 | 味の素株式会社 | Method for manufacturing l-amino acid from biomass derived from seaweed |
EP3053999B1 (en) | 2013-10-02 | 2019-11-20 | Ajinomoto Co., Inc. | Ammonia control apparatus and ammonia control method |
BR112016008830B1 (en) | 2013-10-23 | 2023-02-23 | Ajinomoto Co., Inc | METHOD FOR PRODUCING A TARGET SUBSTANCE |
JP6623690B2 (en) | 2015-10-30 | 2019-12-25 | 味の素株式会社 | Method for producing glutamic acid-based L-amino acid |
JP7066977B2 (en) | 2017-04-03 | 2022-05-16 | 味の素株式会社 | Manufacturing method of L-amino acid |
CN116583605A (en) | 2020-10-28 | 2023-08-11 | 味之素株式会社 | Process for producing L-amino acid |
-
1980
- 1980-04-02 JP JP4321880A patent/JPS56140895A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS56140895A (en) | 1981-11-04 |
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