JPS60248195A - Preparation of l-glutamine by fermentation - Google Patents
Preparation of l-glutamine by fermentationInfo
- Publication number
- JPS60248195A JPS60248195A JP10173184A JP10173184A JPS60248195A JP S60248195 A JPS60248195 A JP S60248195A JP 10173184 A JP10173184 A JP 10173184A JP 10173184 A JP10173184 A JP 10173184A JP S60248195 A JPS60248195 A JP S60248195A
- Authority
- JP
- Japan
- Prior art keywords
- exchange resin
- glutamine
- ion exchange
- fermentation
- resin
- 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.)
- Granted
Links
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
L−グルタミンは消化器潰瘍治療薬、アルコール中毒治
療薬、脳機能改善の薬剤等に用いられている。本発明は
とのL−グルタミンを発酵法で製造する方法を改良する
ものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) L-glutamine is used as a drug for treating gastrointestinal ulcers, a drug for treating alcoholism, a drug for improving brain function, and the like. The present invention improves the method for producing L-glutamine by fermentation.
(従来の技術)
L−fルタミンは大量生産されているアミノ酸であシ、
製造方法に種々の改良が行なわれている。(Prior art) L-f rutamine is an amino acid that is mass-produced.
Various improvements have been made to the manufacturing method.
ヒートモラセスを有機溶剤で抽出することMの発酵収率
を向上させる物質が得られることは知られているが(特
公昭56−12111号公報)、ビート糖製造工程の各
液をイオン交換樹脂に接触させることによシム−グルタ
ミンの発酵収率を向上させる物質が吸着されることは知
られていない。It is known that a substance that improves the fermentation yield of M can be obtained by extracting heat molasses with an organic solvent (Japanese Patent Publication No. 56-12111). It is not known that a substance that improves the fermentation yield of shim-glutamine is adsorbed by contacting it.
(発明が解決しようとする問題点)
L−グルタミンの製造コストを低下させるために発酵収
率を向上させることは重要な問題である。(Problems to be Solved by the Invention) Improving the fermentation yield is an important problem in order to reduce the production cost of L-glutamine.
本発明は、このような目的を達成するべくなされたもの
であり、L−グルタミンの発酵培地にビート糖製造工程
の各種シークロース含有液をイオン交換樹脂に接触させ
た溶離液にL−グルタミンの発酵収率を向上させる物質
が含1れていることを見出したことに基いている。The present invention was made in order to achieve such an object, and L-glutamine is added to an eluent obtained by contacting an L-glutamine fermentation medium with an ion exchange resin and various sucrose-containing liquids used in the beet sugar manufacturing process. This is based on the discovery that it contains a substance that improves fermentation yield.
(問題点を解決するための手段)
本発明は、ビート汁又はそれから精製糖を製造する工程
゛におけるシュクロース含有液をイオン交換樹脂に接触
させ、該イオン交換樹脂に吸着した成分を溶離して、こ
れをL−グルタミン発酵に用いる培地に添加することを
特徴とする、発酵法によるL−グルタミンの製造法に関
するものである。(Means for Solving the Problems) The present invention involves bringing the sucrose-containing liquid in the process of producing beet juice or refined sugar from it into contact with an ion exchange resin, and eluting the components adsorbed on the ion exchange resin. , relates to a method for producing L-glutamine by a fermentation method, which is characterized by adding this to a medium used for L-glutamine fermentation.
ビート汁又はそれから精製糖を製造する工程におけるシ
ークロース含有液とは、ビートを搾汁した原糖汁、脱色
等これに種々の精製手段を施した液、それから数段階に
わたってシュクロース結晶を分離した母液、廃糖蜜であ
るビートモラセスなどである。In the process of manufacturing beet juice or refined sugar from it, the sucrose-containing liquid is the raw sugar juice obtained by squeezing beets, the liquid obtained by subjecting it to various purification methods such as decolorization, and the liquid obtained by separating sucrose crystals from it in several stages. These include mother liquor, beet molasses, and blackstrap molasses.
ビート汁又はノークロース含有液を接触させるイオン交
換樹脂は通常のものでよく、強酸性カチオン交換樹脂、
中、弱酸性カチオン交換樹脂、強塩基性アニオン交換樹
脂、中、弱塩基性アニオン交換樹脂など種々あるがその
いずれであってもよい。The ion exchange resin with which the beet juice or nokrose-containing liquid is brought into contact may be any ordinary one, such as a strongly acidic cation exchange resin,
There are various types of resins, such as medium to weakly acidic cation exchange resins, strongly basic anion exchange resins, and medium to weakly basic anion exchange resins, and any of them may be used.
本発明の方法に用いられる活性成分はビート汁又はノー
クロース含有液をイオン交換樹脂に接触させて吸着成分
を溶離することにより得られるのであるが、現在ビート
汁から精製糖を製造する工程においてイオン交換樹脂に
よる脱塩が行なわれているのでこのイオン交換樹脂の脱
塩廃液を使用するのが簡便である。この脱塩は、冷却し
た粗汁をH型の強酸性カチオン交換樹脂の塔に通液して
カチオンを水素イオンと交換し、塔から流出する強酸性
の糖汁をOH型の弱塩基性アニオン交換樹脂の塔に通液
してアニオンをOHイオンと交換することにより行なわ
れる。これらのイオン交換樹脂の再生の際に吸着された
各種成分が溶離され、この溶離液がいわゆるイオン交換
樹脂脱塩廃液として多量に副生される。この脱塩廃液は
主として無機塩類を含んでいるが、そのほか少量の有機
酸類、アミノ酸等の有機窒素を含み、糖はほとんど含ん
でいない。脱塩廃液にはカチオン交換樹脂塔からの廃液
、アニオン交換樹脂塔からの廃液及び両者の混合液があ
るがいずれも本発明の方法に使用できる。これらはその
まま培地に添加してもよいが、適当な濃度に濃縮してか
ら添加するほうが一般に好都合である。培地への添加量
は総窒素量で設定すればよく、通常100 m9/l!
以上添加すれば収率向上の効果が得られる。The active ingredient used in the method of the present invention can be obtained by contacting beet juice or a solution containing noucrose with an ion exchange resin to elute the adsorbed components. Since desalination is carried out using an exchange resin, it is convenient to use desalination waste liquid from this ion exchange resin. This desalting process involves passing the cooled crude juice through a tower made of H-type strongly acidic cation exchange resin to exchange cations with hydrogen ions, and converting the strongly acidic sugar juice flowing out from the tower into OH-type weakly basic anions. This is carried out by passing an exchange resin through a tower to exchange anions with OH ions. During the regeneration of these ion exchange resins, various adsorbed components are eluted, and a large amount of this eluate is produced as a so-called ion exchange resin desalting waste liquid. This desalted waste liquid mainly contains inorganic salts, but also contains small amounts of organic acids, amino acids, and other organic nitrogen, and almost no sugar. The desalination waste liquid includes waste liquid from a cation exchange resin tower, a waste liquid from an anion exchange resin tower, and a mixture of the two, and any of them can be used in the method of the present invention. These may be added to the medium as they are, but it is generally more convenient to concentrate them to an appropriate concentration before adding them. The amount added to the culture medium can be set based on the total amount of nitrogen, usually 100 m9/l!
If the above amount is added, the effect of improving the yield can be obtained.
その他の培地成分はL−グルタミン発酵に用いられる通
常の培地と同様でよく、グルコース、フモニウム塩、ア
ンモニア、尿素等の窒素源、リン酸塩、マグネシウム塩
、鉄塩、マンガン塩等の塩類、ビオチン、サイアミン等
のピクミン類、アミノ酸等の有機微量栄養素等が使用さ
れる。Other medium components may be the same as the usual medium used for L-glutamine fermentation, including glucose, nitrogen sources such as fumonium salts, ammonia, and urea, salts such as phosphates, magnesium salts, iron salts, and manganese salts, and biotin. , pikmin such as thiamine, organic micronutrients such as amino acids, etc. are used.
本発明の方法に使用される微生物は通常のL−グルタミ
ン生産菌でよく、例えばいわゆるコリネフォームの、
ブレビバクテリウム・フラバム FERM−P4272
コリネバクテリウム・アセトアシドフィラムATCC1
3870などが使用される。The microorganisms used in the method of the present invention may be ordinary L-glutamine producing bacteria, such as the so-called coryneform Brevibacterium flavum FERM-P4272.
Corynebacterium acetoacidophyllum ATCC1
3870 etc. are used.
培養方法及び発酵液からのL−グルタミンの採取方法は
常法に従って行なえばよく、特別な方法を必要としない
。The culture method and the method for collecting L-glutamine from the fermentation liquid may be carried out according to conventional methods, and no special method is required.
本発明の方法は、ビート汁又はそれから精製糖を製造す
る工程におけるシークロース含有液のうちイオン交換樹
脂吸着成分を培地に添加するだけでL−グルタミンの発
酵収率を向上させることができる。この吸着成分には、
例精製糖を製造する工程で副生ずる利用価値の少ないイ
オン交換樹脂脱塩廃液を有効利用できるのでその処分の
負担を軽減し、経済的に有利にL−グルタミンを製造す
ることができる。The method of the present invention can improve the fermentation yield of L-glutamine by simply adding an ion-exchange resin-adsorbed component of the sucrose-containing liquid to the culture medium in the process of producing beet juice or refined sugar from it. This adsorbed component includes
Example: Since the ion-exchange resin desalination waste liquid, which is produced as a by-product in the process of producing refined sugar and has little utility value, can be effectively used, the burden of its disposal can be reduced, and L-glutamine can be economically advantageously produced.
北海道のビート糖製糖工場の糖蜜脱塩工程で生ずるイオ
ン交換樹脂脱塩廃液を総窒素濃度20g−/l程間に濃
縮した。An ion exchange resin desalting waste liquid produced in the molasses desalting process at a beet sugar factory in Hokkaido was concentrated to a total nitrogen concentration of about 20 g/l.
グルコース 100P/d
KH2PO42“
MgSO4・7H200,5II
(NH4)2SO415p
Na2SO4151
FeSO44H201m9/13
ビオチン 4μMで
サイアミン塩酸塩 200 〃
大豆蛋白加水分解液 0.2y7/l
(総窒素濃度として)
上記の組成の培地をllづつジャーファーメンタ−に入
れ、苛性ソーダでpH7,0に調整して120℃で10
分間加熱殺菌した。・これに上記の脱塩廃液濃縮液を1
20℃で10分間加熱殺菌してその後述する量を添加し
、さらに予め培養しておいたブレビバクテリウム・フラ
バムFERM−P 4272の種培養液50 mlを接
種した。培養温度を31℃とし、アンモニアガスでPH
5,5に保ちつつ残クルコース。Glucose 100P/d KH2PO42" MgSO4・7H200,5II (NH4)2SO415p Na2SO4151 FeSO44H201m9/13 Biotin thiamine hydrochloride at 4 μM 200 Soybean protein hydrolyzate 0.2y7/l (as total nitrogen concentration) 1 liter of medium with the above composition Place in a jar fermentor, adjust the pH to 7.0 with caustic soda, and incubate at 120℃ for 10 minutes.
Heat sterilized for minutes.・Add 1 part of the desalination waste liquid concentrate to this.
After heat sterilization at 20° C. for 10 minutes, the amount described above was added, and 50 ml of a seed culture of Brevibacterium flavum FERM-P 4272, which had been cultured in advance, was inoculated. The culture temperature was set to 31℃, and the pH was adjusted with ammonia gas.
Remaining course while keeping it at 5.5.
が無くなるまで通気攪拌を続けた。Aeration and stirring were continued until there was no more residue.
得られた培養液のし一グルタミン濃度を常法により測定
して対糖収率をめた。得られた結果を次に示す。The concentration of glutamine in the obtained culture solution was measured by a conventional method to determine the yield relative to sugar. The results obtained are shown below.
脱塩廃液添加量 L−グルタミン収率 (総窒素、rv/l) (%) 0 38】 100 38.6 500 39.0 1000 39.7 2000 4.1.8 5000 42.5Desalination waste liquid addition amount L-glutamine yield (Total nitrogen, rv/l) (%) 0 38] 100 38.6 500 39.0 1000 39.7 2000 4.1.8 5000 42.5
Claims (1)
ークロース含有液をイオン交換樹脂に接触させ、該イオ
ン交換樹脂に吸着した成分を溶離して、これをL−グル
タミン発酵に用いる培地に添加することを特徴とする、
発酵法によるL−グルタミンの製造法A method of contacting beet juice or a liquid containing sucrose in the process of producing refined sugar from it with an ion exchange resin, eluating the components adsorbed to the ion exchange resin, and adding this to the medium used for L-glutamine fermentation. Characterized by
Method for producing L-glutamine by fermentation method
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10173184A JPS60248195A (en) | 1984-05-22 | 1984-05-22 | Preparation of l-glutamine by fermentation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10173184A JPS60248195A (en) | 1984-05-22 | 1984-05-22 | Preparation of l-glutamine by fermentation |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60248195A true JPS60248195A (en) | 1985-12-07 |
JPH0543356B2 JPH0543356B2 (en) | 1993-07-01 |
Family
ID=14308413
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10173184A Granted JPS60248195A (en) | 1984-05-22 | 1984-05-22 | Preparation of l-glutamine by fermentation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60248195A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002040643A1 (en) * | 2000-11-17 | 2002-05-23 | Cheil Jedang Corporation | Microorganisms producing l-glutamine and processes for producing l-glutamine using the same |
-
1984
- 1984-05-22 JP JP10173184A patent/JPS60248195A/en active Granted
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002040643A1 (en) * | 2000-11-17 | 2002-05-23 | Cheil Jedang Corporation | Microorganisms producing l-glutamine and processes for producing l-glutamine using the same |
AU783498B2 (en) * | 2000-11-17 | 2005-11-03 | Cj Cheiljedang Corporation | Microorganisms producing L-glutamine and processes for producing L-glutamine using the same |
US6984506B2 (en) | 2000-11-17 | 2006-01-10 | Cheil Jedang Corporation | Microorganisms and processes for producing L-glutamine |
US7192760B2 (en) | 2000-11-17 | 2007-03-20 | Cheil Jedang Corporation | Microorganisms and processes for producing L-glutamine |
Also Published As
Publication number | Publication date |
---|---|
JPH0543356B2 (en) | 1993-07-01 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |