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JPS6224072B2 - - Google Patents

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Publication number
JPS6224072B2
JPS6224072B2 JP54015341A JP1534179A JPS6224072B2 JP S6224072 B2 JPS6224072 B2 JP S6224072B2 JP 54015341 A JP54015341 A JP 54015341A JP 1534179 A JP1534179 A JP 1534179A JP S6224072 B2 JPS6224072 B2 JP S6224072B2
Authority
JP
Japan
Prior art keywords
lysine
ethanol
culture
acinetobacter
medium
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
Application number
JP54015341A
Other languages
Japanese (ja)
Other versions
JPS55108291A (en
Inventor
Hideaki Yugawa
Kazuoki Ookuma
Shoichi Nara
Yoshihiro Takayama
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Petrochemical Co Ltd
Original Assignee
Mitsubishi Petrochemical Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Petrochemical Co Ltd filed Critical Mitsubishi Petrochemical Co Ltd
Priority to JP1534179A priority Critical patent/JPS55108291A/en
Priority to DE19803005409 priority patent/DE3005409A1/en
Priority to US06/120,963 priority patent/US4276380A/en
Publication of JPS55108291A publication Critical patent/JPS55108291A/en
Publication of JPS6224072B2 publication Critical patent/JPS6224072B2/ja
Granted legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Description

【発明の詳細な説明】 本発明は、醗酵法によるL―リジン製造法に関
するものである。L―リジンは、必須アミノ酸と
して有用であり、その安価なる工業的製法が期待
されている。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing L-lysine by fermentation. L-lysine is useful as an essential amino acid, and an inexpensive industrial method for producing it is expected.

醗酵法によるアミノ酸の製造は、糖質(炭水化
物)系物質を主原料として実施されているが、原
料が農産物系のため、価格及び供給の安定性に問
題があることや、含有する多量の不純物に由来
し、生成される著量の副産物の問題、また醗酵廃
液の着色等の種々の問題を有し、根本的改善が望
まれていた。これらへの対応策として、炭化水素
等を醗酵原料とする製造法が研究されているが、
炭化水素はガス状であつたり、水に不溶性であつ
たりして工業的に使用するに難点があり、その為
に生成物の収量にも限界がある。そこで、本発明
者らは、安価で安定した供給が可能と考えられ、
かつ上記の欠点のないエタノールに着目して鋭意
研究の結果、アシネトバクター属に属し、エタノ
ール資化性を有する、微生物の中よりエタノール
を主炭素源とする培地にて培養すると、著量のL
―リジンを生成蓄積する能力を有する微生物を発
見し、ここに発明を完成した。すなわちアシネト
バクター属に属し、エタノール資化性を有し、か
つL―リジンを生成する能力を有する微生物をエ
タノールを主炭素源とする培地に培養して、L―
リジンを生成蓄積せしめ、培養物からこれを採取
することにより効率的にL―リジンを製造でき
る。
Amino acids are produced by fermentation using sugar (carbohydrate) substances as the main raw materials, but since the raw materials are agricultural products, there are problems with price and supply stability, and the large amount of impurities they contain. There are various problems such as the large amount of by-products produced and the coloring of the fermentation waste liquid, and fundamental improvements have been desired. As a countermeasure to these problems, production methods using fermentation raw materials such as hydrocarbons are being researched.
Hydrocarbons are difficult to use industrially because they are gaseous or insoluble in water, which limits the yield of products. Therefore, the present inventors believe that cheap and stable supply is possible,
As a result of intensive research focusing on ethanol, which does not have the above drawbacks, we found that among microorganisms that belong to the genus Acinetobacter and have the ability to assimilate ethanol, when cultured in a medium containing ethanol as the main carbon source, a significant amount of L.
- Discovered a microorganism that has the ability to produce and accumulate lysine, and completed the invention. That is, a microorganism belonging to the genus Acinetobacter, capable of assimilating ethanol, and capable of producing L-lysine is cultured in a medium containing ethanol as the main carbon source.
L-lysine can be efficiently produced by producing and accumulating lysine and collecting it from the culture.

本発明に使用する微生物は、アシネトバクター
属に属し、エタノールを資化し、L―リジンを生
成蓄積する能力を有する微生物であれば、自然界
からの分離株もしくは、公知の菌株あるいは、こ
れからの人為的遺伝変異株であつてもよい。
The microorganisms used in the present invention belong to the genus Acinetobacter and have the ability to assimilate ethanol and produce and accumulate L-lysine, and may be isolated from nature, known strains, or artificially inherited from the future. It may be a mutant strain.

エタノールからのL―リジンを生成蓄積する微
生物の例としてアシネトバクター・カルコアセチ
カムYK―1011を示す。
Acinetobacter calcoaceticum YK-1011 is shown as an example of a microorganism that produces and accumulates L-lysine from ethanol.

アシネトバクター・カルコアセチカムYK―
1011は工業技術院微生物研究所に受理番号第4818
号(昭和54年2月9日、微工研菌寄第4818号)と
して受理されている。
Acinetobacter Calcoaceticum YK-
1011 is the receipt number 4818 of the Institute of Microbiology, Agency of Industrial Science and Technology.
(February 9, 1978, Microtechnical Research Institute No. 4818).

この微生物は、アシネトバクター・カルコアセ
チカムATCC19606より5―メチル―DL―トリプ
トフアン耐性株として誘導分離されたものであ
り、5―メチル―DL―トリプトフアン耐性であ
る点を除いたその他の性質はアシネトバクター・
カルコアセチカムATCC19606と同一である。
This microorganism was isolated from Acinetobacter calcoaceticum ATCC19606 as a 5-methyl-DL-tryptophan-resistant strain, and other than its resistance to 5-methyl-DL-tryptophan, other characteristics are similar to that of Acinetobacter.
Identical to Calcoaceticum ATCC19606.

本発明の具体的実施方法は以下の通りである。 A concrete implementation method of the present invention is as follows.

培地組成の炭素源としては、エタノールを使用
するが、初期濃度については、使用する菌株によ
り1〜5%v/v内外より適当な条件を選定する。
なおエタノールは、消費にともない菌株の生育も
しくは、L―リジン生成に阻害を与えない適当な
る濃度条件に注意しながら逐次添加を行なう。
Ethanol is used as the carbon source in the medium composition, and the initial concentration is selected from 1 to 5% v/v or less depending on the strain used.
Note that ethanol is added sequentially while paying attention to appropriate concentration conditions that do not inhibit the growth of the bacterial strain or the production of L-lysine as it is consumed.

窒素源としては、硫安、硝安、リン安、尿素等
より菌株の利用能により選定する。この他必要量
に応じて、アミノ酸類、コーンステイープリカ
ー、味液、酵母エキス等の有機栄養源や、無機塩
類、ビタミン類などを添加し培地とする。
The nitrogen source is selected from among ammonium sulfate, ammonium nitrate, ammonium phosphorus, urea, etc., depending on the utilization capacity of the bacterial strain. In addition, organic nutritional sources such as amino acids, cornstarch liquor, flavor liquid, yeast extract, inorganic salts, vitamins, etc. are added to the medium according to the required amount.

培養条件については、温度20〜37℃、PH4〜
10、好ましくは、25〜35℃、PH6〜8として培養
すればよいが、これらの条件についても、使用菌
株により最適のものを選択する。培養は大体2〜
7日間を必要とする。
Regarding culture conditions, temperature: 20-37℃, pH: 4~
10. Preferably, the culture may be carried out at 25 to 35° C. and at a pH of 6 to 8, but these conditions are also selected as appropriate depending on the strain used. Culture is about 2~
It takes 7 days.

培養終了後、液中よりイオン交換樹脂法、活性
炭法、濃縮晶析法等の公知の方法により生成した
L―リジンを回収することが出来る。以下に実施
例を示す。
After completion of the culture, L-lysine produced can be recovered from the liquid by a known method such as an ion exchange resin method, an activated carbon method, or a concentration crystallization method. Examples are shown below.

なお、生成されたL―リジンの定量は、ロイコ
ノストツク メセンテロイデスATCC8042を用い
る微生物定量法により培地中に含有するL―リジ
ンを差引いた値を示した。
The amount of L-lysine produced was determined by subtracting the amount of L-lysine contained in the culture medium using a microbial quantitative method using Leuconostoc mesenteroides ATCC8042.

実施例 1 前培養培地(尿素20g、硫安7.0g、
KH2PO40.5g、K2HPO40.5g、MgSO4
7H2O0.5g、酵母エキス0.5g、カザミノ酸0.5g、
FeSO4・7H2O2mg、MnSO4・4〜6H2O2mg、
ZnSO4・7H2O2mg、NaCl2mg、CaCl2・2H2O2
mg、ビオチン200μg、チアミン塩酸塩100μg、
水道水1)10mlを口径24mmの大型試験管に分注
し、120℃、10分間滅菌し、無菌条件下にてエタ
ノールを0.2ml添加しアシネトバクター・カルコ
アセチカムYK―1011を植菌し、30℃で2日間振
盪培養を行なう。次に前培養地と同一の培地10ml
を口径24mmの大型試験管に分注し、120℃、10分
間滅菌し、あらかじめ乾熱滅菌した炭酸カルシウ
ム0.2gを添加し、次にエタノール0.2mlを添加し
た後、前培養液0.2mlを植菌し、30℃にて、7日
間振盪培養を行なう。エタノールは消費にともな
い添加する。(この際エタノールは3v/v%を越
えないようにする。)培養7日目に6g/蓄積さ
れたL―リジンを採取した。
Example 1 Preculture medium (20 g of urea, 7.0 g of ammonium sulfate,
KH 2 PO 4 0.5g, K 2 HPO 4 0.5g, MgSO 4
7H 2 O 0.5g, yeast extract 0.5g, casamino acid 0.5g,
FeSO 4・7H 2 O2mg, MnSO 4・4~6H 2 O2mg,
ZnSO 4・7H 2 O2mg, NaCl2mg, CaCl 2・2H 2 O2
mg, biotin 200μg, thiamine hydrochloride 100μg,
1) Dispense 10ml of tap water into a large test tube with a diameter of 24mm, sterilize it at 120℃ for 10 minutes, add 0.2ml of ethanol under aseptic conditions, inoculate it with Acinetobacter calcoaceticum YK-1011, and inoculate it at 30℃. Perform shaking culture for 2 days. Next, 10 ml of the same medium as the pre-culture medium.
Dispense the solution into a large test tube with a diameter of 24 mm, sterilize it at 120℃ for 10 minutes, add 0.2 g of calcium carbonate that has been dry heat sterilized in advance, add 0.2 ml of ethanol, and inoculate 0.2 ml of the preculture solution. Incubate the cells and culture with shaking at 30°C for 7 days. Ethanol is added as it is consumed. (At this time, ethanol should not exceed 3 v/v%.) On the 7th day of culture, 6 g/accumulated L-lysine was collected.

実施例 2 実施例1に用いたと同じ前培養培地10mlを口径
24mmの大型試験管に分注し、120℃、10分間滅菌
した。これに無菌条件下にてエタノールを0.2ml
添加し、更にアシネトバクター・カルコアセチカ
ムYK―1011(微工研菌寄第4818号)を植菌し
て、30℃で2日間振盪培養を行つた。
Example 2 10 ml of the same preculture medium used in Example 1 was
The mixture was dispensed into large 24 mm test tubes and sterilized at 120°C for 10 minutes. Add 0.2ml of ethanol to this under sterile conditions.
In addition, Acinetobacter calcoaceticum YK-1011 (Feikoken Bibori No. 4818) was inoculated and cultured with shaking at 30°C for 2 days.

次に前培養培地と同一の培地100mlを500ml容三
角フラスコに分注し、120℃、10分間滅菌した。
これに予め乾燥滅菌した炭酸カルシウム2gを添
加し、次にエタノール2mlを添加した後、上記前
培養液2mlを植菌し、30℃にて、7日間振盪培養
を行つた。この際エタノールは消費に伴い3v/v
%を越えないように添加した。培養7日目L―リ
ジンが6.5g蓄積された培養液を得た。この培養液
100mlを遠心分離して得られた上清液を強酸性イ
オン交換樹脂〔ローム・アンド・ハース社製「ア
ンバーライトIR―120」、H型〕カラムに通しL
―リジンを吸着させた。次いで3%アンモニア水
で溶出し、溶出液を減圧下濃縮し、これに塩酸を
加え、冷却・晶析後乾燥して560mlのL―リジン
塩酸塩を得た。
Next, 100 ml of the same medium as the preculture medium was dispensed into a 500 ml Erlenmeyer flask and sterilized at 120°C for 10 minutes.
To this was added 2 g of calcium carbonate that had been previously dried and sterilized, and then 2 ml of ethanol, followed by inoculation with 2 ml of the above preculture solution, and cultured with shaking at 30° C. for 7 days. At this time, ethanol is 3v/v as it is consumed.
It was added so as not to exceed %. On the 7th day of culture, a culture solution was obtained in which 6.5 g of L-lysine had been accumulated. This culture solution
The supernatant liquid obtained by centrifuging 100 ml was passed through a column of strongly acidic ion exchange resin [Amberlite IR-120, H type, manufactured by Rohm and Haas].
- Adsorbed lysine. The eluate was then eluted with 3% aqueous ammonia, the eluate was concentrated under reduced pressure, hydrochloric acid was added thereto, and the mixture was cooled, crystallized, and dried to obtain 560 ml of L-lysine hydrochloride.

Claims (1)

【特許請求の範囲】[Claims] 1 アシネトバクター属に属し、エタノール資化
性を有し、かつL―リジンを生成する能力を有す
る微生物をエタノールを主炭素源とする培地に培
養してL―リジンを生成蓄積せしめ、培養物から
これを採取することを特徴とする醗酵法によるL
―リジンの製造法。
1. A microorganism that belongs to the genus Acinetobacter and has the ability to assimilate ethanol and produce L-lysine is cultured in a medium containing ethanol as the main carbon source to produce and accumulate L-lysine, and this is extracted from the culture. L by a fermentation method characterized by collecting
-Production method of lysine.
JP1534179A 1979-02-13 1979-02-13 Production of l-lysine through fermentation process Granted JPS55108291A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP1534179A JPS55108291A (en) 1979-02-13 1979-02-13 Production of l-lysine through fermentation process
DE19803005409 DE3005409A1 (en) 1979-02-13 1980-02-13 METHOD FOR PRODUCING L-VALINE OR L-LYSINE
US06/120,963 US4276380A (en) 1979-02-13 1980-02-13 Production of L-amino acids

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1534179A JPS55108291A (en) 1979-02-13 1979-02-13 Production of l-lysine through fermentation process

Publications (2)

Publication Number Publication Date
JPS55108291A JPS55108291A (en) 1980-08-20
JPS6224072B2 true JPS6224072B2 (en) 1987-05-26

Family

ID=11886080

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1534179A Granted JPS55108291A (en) 1979-02-13 1979-02-13 Production of l-lysine through fermentation process

Country Status (1)

Country Link
JP (1) JPS55108291A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108796026A (en) * 2018-06-29 2018-11-13 齐齐哈尔龙江阜丰生物科技有限公司 Production, extraction and the purifying process of lysine

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5036691A (en) * 1973-08-07 1975-04-05

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5036691A (en) * 1973-08-07 1975-04-05

Also Published As

Publication number Publication date
JPS55108291A (en) 1980-08-20

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