JPH0560358B2 - - Google Patents

Info

Publication number
JPH0560358B2
JPH0560358B2 JP24492787A JP24492787A JPH0560358B2 JP H0560358 B2 JPH0560358 B2 JP H0560358B2 JP 24492787 A JP24492787 A JP 24492787A JP 24492787 A JP24492787 A JP 24492787A JP H0560358 B2 JPH0560358 B2 JP H0560358B2
Authority
JP
Japan
Prior art keywords
lipopolysaccharide
bacteria
nutrient medium
erwinia
culture
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 - Lifetime
Application number
JP24492787A
Other languages
Japanese (ja)
Other versions
JPS6486892A (en
Inventor
Satoshi Fukuoka
Masao Karube
Yoshio Kobayashi
Hiroshi Ueshima
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP24492787A priority Critical patent/JPS6486892A/en
Publication of JPS6486892A publication Critical patent/JPS6486892A/en
Publication of JPH0560358B2 publication Critical patent/JPH0560358B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 産業上の利用分野 リポ多糖は抗原抗体反応、赤血球の凝集反応な
どを起こす性質があることから、従来、医学、薬
学、生化学などの分野における学術研究用の試薬
として用いられている。
[Detailed Description of the Invention] Industrial Application Fields Lipopolysaccharide has the property of causing antigen-antibody reactions and red blood cell agglutination reactions, so it has been used as a reagent for academic research in fields such as medicine, pharmacy, and biochemistry. It is used.

従来の技術 リポ多糖はエルウイニア属細菌のようなグラム
陰性細菌の細胞外膜の構成物質であり、該細菌類
によつて菌体内に生産されている事は公知であ
る。
BACKGROUND ART Lipopolysaccharide is a component of the extracellular membrane of Gram-negative bacteria such as Erwinia bacteria, and it is known that it is produced within the cells of these bacteria.

リポ多糖の製造に関してはこれまで、公知の例
としては、大腸菌、サルモネラ(Salmonella)
菌などを栄養培地で液相で培養し、しかる後に菌
体を採取しフエノール、水、および石油エーテル
の混合溶液(例えば、ヨーロピアン.ジヤーナ
ル.オブ.バイオケミストリー(Eur.J.
Biochem.)、第9巻、245ページ、1969年)、ある
いはノルマルブタノール、水混合溶液(例えば、
ジヤーナル.オブ.バイオロジカル.ケミストリ
ー(J.Biol.chem.)、第250巻、2911ページ、1975
年)などを用いて、細菌類の菌体から分離する方
法がとられている。しかし、これらの方法はいず
れもリポ多糖が菌体内に留るために、有機溶剤等
を利用して抽出分離するという極めて煩雑な操作
を必要とする。また、菌体内の蓄積量にも制限が
あり多量に生産するのは困難である。
Regarding the production of lipopolysaccharide, known examples include Escherichia coli, Salmonella
Bacteria, etc. are cultured in a liquid phase in a nutrient medium, and then the bacterial bodies are collected and added to a mixed solution of phenol, water, and petroleum ether (e.g., European Journal of Biochemistry (Eur.J.)).
Biochem.), Vol. 9, p. 245, 1969), or a mixed solution of n-butanol and water (e.g.
Journal. of. Biological. Chemistry (J.Biol.chem.), Volume 250, Page 2911, 1975
(2013) and other methods are used to isolate it from bacterial bodies. However, in all of these methods, the lipopolysaccharide remains inside the microbial cells, and therefore requires an extremely complicated operation of extraction and separation using an organic solvent or the like. Furthermore, there is a limit to the amount that can be accumulated within the bacterial body, making it difficult to produce in large quantities.

発明が解決しようとする問題点 本発明の目的はこのような従来の技術の欠点を
排除し、簡便に多量のリポ多糖を菌体外に生産さ
せる方法を提供することにある。すなわち、リポ
多糖が細菌の体内に留る機構を解除してリポ多糖
を培養液中に生産させ、従来有機溶剤等を用いて
抽出することにより得ていた該物質を、培養液中
に放出させる新規な方法を提供することにある。
Problems to be Solved by the Invention It is an object of the present invention to eliminate the drawbacks of the conventional techniques and to provide a method for easily producing a large amount of lipopolysaccharide outside a bacterial cell. That is, the mechanism by which lipopolysaccharide remains in the bacterial body is released to produce lipopolysaccharide in the culture solution, and the substance, which was conventionally obtained by extraction using an organic solvent, etc., is released into the culture solution. The purpose is to provide a new method.

問題点を解決するための手段 本発明者らは、エルウイニア属細菌の培養方法
及び、生産する物質に関する研究を行い、その結
果、それぞれ異なる炭素源を用いた栄養培地を使
用し、2段階で該エルウイニア属細菌を培養する
事により、前記目的を達成しうる事をみいだし、
この知見に基ずいて本発明を完成するに至つた。
すなわち、本発明の方法はエルウイニア属細菌を
ペクチン質を炭素源とする栄養培地を用いて好気
的に培養し、殆どペクチン質がなくなる増殖定常
期の終末以内の期間までの第一次増殖と、非ペク
チン質を炭素源とする栄養培地を用いて、前記細
菌を再び培養する第二次増殖の2段階の培養から
なつている。
Means for Solving the Problems The present inventors have conducted research on the culture method of Erwinia bacteria and the substances produced, and as a result, they have found that they can be cultured in two stages using nutrient media each using a different carbon source. We have discovered that the above objective can be achieved by culturing Erwinia bacteria,
Based on this knowledge, we have completed the present invention.
That is, the method of the present invention involves aerobically cultivating Erwinia bacteria using a nutrient medium containing pectin as a carbon source, and culturing the primary growth until the end of the stationary growth phase when almost no pectin is present. The method consists of two stages of secondary growth, in which the bacteria are cultured again using a nutrient medium containing non-pectin as a carbon source.

本発明の方法に於いて、用いるエルウイニア属
細菌としては、カロトボラ種群の細菌、例えば、
エルウイニア.カロトボラ.サブスプ.カロトボ
ラ(Erwinia carotovora.subsp.carotovora)、
エルウイニア.クリサンセミ(Erwinia
Chrysanthemi)、エルウイニア.ラポンテイシイ
(Erwinia rhapontici)などが好ましく上げられ
る。
In the method of the present invention, the bacteria of the genus Erwinia used include bacteria of the Carotobora species group, for example,
Erwinia. Calotobora. Subsp. Carotovora (Erwinia carotovora.subsp.carotovora),
Erwinia. Chrysanthemum (Erwinia)
Chrysanthemi), Erwinia. Preferred examples include Erwinia rhapontici.

本発明の方法に於ける第一次増殖には、栄養培
地として、ペクチン質を炭素源とし、かつ栄養源
として、例えばグルタミン酸モノナトリウムや硫
酸アンモニウムなどの窒素化合物、リン酸第一カ
リウムやリン酸第二ナトリウム、硫酸マグネシウ
ムなどを添加した液体培地が用いられる。
The primary growth in the method of the present invention involves using pectic material as a nutrient medium as a carbon source, and nitrogen compounds such as monosodium glutamate and ammonium sulfate, potassium phosphate and potassium phosphate as a nutrient source. A liquid medium to which disodium, magnesium sulfate, etc. are added is used.

一方、第二次増殖には栄養培地として、炭素源
に非ペクチン質を、かつ栄養源として前記の化合
物などを添加した液体培地が用いられる。該非ペ
クチン質としては、グリセリンやソルビツトなど
の緩慢代謝性の炭素化合物が好適である。
On the other hand, for secondary growth, a liquid medium containing a non-pectic substance as a carbon source and the above-mentioned compounds as a nutrient source is used as a nutrient medium. As the non-pectic substance, slowly metabolizing carbon compounds such as glycerin and sorbitol are suitable.

前記エルウイニア属細菌の培養は、第一次及び
第二次増殖ともに、空気を吹込みながら好気的
に、通常10〜60℃、好ましくは20〜40℃の温度範
囲で行われる。また、PHについては第一次及び第
二次増殖のいずれにおいても必ずしも調整する必
要はない。
The cultivation of the Erwinia bacteria is carried out aerobically while blowing air, usually at a temperature range of 10 to 60°C, preferably 20 to 40°C, for both primary and secondary growth. Furthermore, it is not necessarily necessary to adjust the pH during either primary or secondary proliferation.

このような2段階培養法により、本来は菌体内
に留るリポ多糖が培養液中にまで生産されるよう
になる。
By such a two-step culture method, lipopolysaccharide, which normally remains within the bacterial cells, can be produced even into the culture solution.

生産されたリポ多糖は、液体培地中に存在する
ので、該菌体を遠心分離やろ過などの手段によつ
て除去した後、ろ液を通常行われている方法で処
理することにより粗リポ多糖として回収される。
このようにして得られた粗リポ多糖は、必要なら
ばさらに公知の精製法に従つて精製することも可
能である。
The produced lipopolysaccharide is present in the liquid medium, so after removing the bacterial cells by centrifugation or filtration, the filtrate is treated with a commonly used method to obtain crude lipopolysaccharide. will be collected as.
The crude lipopolysaccharide thus obtained can be further purified according to known purification methods, if necessary.

発明の効果 従来のリポ多糖の製造方法に於いては、該物質
はグラム陰性細菌の細胞内に留るため、細胞を崩
壊し、有機溶剤等を用いる抽出分離の操作を必要
としていた。また、菌体内に蓄積しているために
生産性が極めて低かつた。これに対し、本発明の
方法によると、培養液中に生産され、リポ多糖の
分離が容易になるばかりではなく、同時に生産性
が顕著に拡大される。
Effects of the Invention In the conventional method for producing lipopolysaccharide, since the substance remains within the cells of Gram-negative bacteria, it was necessary to disintegrate the cells and perform extraction and separation using an organic solvent or the like. In addition, productivity was extremely low due to accumulation within the bacterial body. On the other hand, according to the method of the present invention, lipopolysaccharide is produced in the culture solution, which not only facilitates the separation of lipopolysaccharide, but also significantly increases productivity.

また、本発明の方法は当該菌体以外のものにつ
いても応用が可能である。
Furthermore, the method of the present invention can be applied to cells other than the above-mentioned bacterial cells.

実施例 次に実施例により本発明をさらに詳細に説明す
る。
Examples Next, the present invention will be explained in more detail with reference to Examples.

実施例 エルウイニア.カロトボラFERM P−7576の
菌体を10のジヤーフアーメンターを用いて、ま
ず次の組成を有する栄養培地中で、温度28℃、送
風量2.5/min、かきまぜ速度480rpmの条件で
一次培養を行つた。
Example Erwinia. Carotovora FERM P-7576 cells were first cultured in a nutrient medium with the following composition using a 10 jar fermenter under conditions of a temperature of 28°C, an air flow rate of 2.5/min, and a stirring speed of 480 rpm. Ivy.

一次培養栄養培地の組成 ペクチン 25g グルタミン酸モノナトリウム(一水和物) 25g 硫酸アンモニウム 15g リン酸第一カリウム 12g リン酸第二ナトリウム 4g 硫酸マグネシウム(7水和物) 1g シリコン消泡剤 2.5g 水 5 この結果、該細菌は培養開始16時間までは菌体
が増殖するが、それ以降は定常期となる。この一
次培養において、該菌体を除去した培養液中に公
知の物質分離方法により高分子量の物質が分離さ
れる。該物質は公知の分析方法に準じて成分分析
を行つたところ、糖、リン酸、脂肪酸を成分とし
て有していた。これは、一般にリポ多糖と称され
る公知の物質の構成成分に等しい。また、該物質
をポリアクリルアミドゲル電気泳動法に準じて電
気泳動した後、ゲルをリポ多糖の公知の染色方法
(例えば、アナリテイカル.バイオケミストリー
(Anal.Biochem.)第119巻、115ページ、1982年)
に準じて銀染色を行つたところ、明瞭に染色され
る物質であることが分つた。このことからも、該
物質はリポ多糖であることが確認された。
Composition of primary culture nutrient medium Pectin 25g Monosodium glutamate (monohydrate) 25g Ammonium sulfate 15g Potassium phosphate 12g Disodium phosphate 4g Magnesium sulfate (heptahydrate) 1g Silicone antifoam agent 2.5g Water 5 As a result, the bacteria proliferate until 16 hours after the start of culture, but after that, the cells enter the stationary phase. In this primary culture, a high molecular weight substance is separated from the culture solution from which the bacterial cells have been removed by a known substance separation method. Component analysis of this substance according to a known analytical method revealed that it contained sugar, phosphoric acid, and fatty acid as components. This is equivalent to the constituents of the known substance commonly referred to as lipopolysaccharide. In addition, after electrophoresing the substance according to polyacrylamide gel electrophoresis method, the gel is dyed using a known lipopolysaccharide staining method (for example, Analytical Biochem. Vol. 119, p. 115, 1982). )
When silver staining was carried out according to the method described in 2007, it was found that the material stained clearly. This also confirmed that the substance was lipopolysaccharide.

一次培養に於いて培養液中に生産されるリポ多
糖は0.1g/であつた。次に、16時間一次培養
した培養液に、グリセリン100gとグルタミン酸
モノナトリウム(一水和物)100gを溶解した水
溶液からなる栄養培地300mlを加えて、二次培養
を行うと培養の開始後16時間までは細菌が増殖す
る。16時間二次培養した培養液を遠心分離により
該細菌の菌体を除去し、除菌培養液を得る。該溶
液を透析用のセロフアンチユーブに入れ、該溶液
20mlあたり1の蒸留水を用いて24時間透析す
る。透析により、栄養培養中の無機イオンなどを
分離して得られる溶液を凍結乾燥し水分を除去す
ると、1の除菌培養液から2gのリポ多糖を含
む粉末3.3gが得られる。
The amount of lipopolysaccharide produced in the culture solution in the primary culture was 0.1 g/. Next, 300 ml of a nutrient medium consisting of an aqueous solution containing 100 g of glycerin and 100 g of monosodium glutamate (monohydrate) dissolved in the culture solution after 16 hours of primary culture is added to perform secondary culture, and 16 hours after the start of culture. Bacteria proliferate until The bacterial cells are removed by centrifugation from the culture solution that has been subcultured for 16 hours to obtain a sterilized culture solution. Put the solution in a cellophane tube for dialysis, and
Dialyze for 24 hours using 1 part distilled water per 20 ml. When the solution obtained by separating inorganic ions and the like in the nutrient culture by dialysis is freeze-dried to remove water, 3.3 g of powder containing 2 g of lipopolysaccharide is obtained from 1 sterilized culture solution.

Claims (1)

【特許請求の範囲】 1 エルウイニア(Erwinia)属細菌をペクチン
質を炭素源とする栄養培地を用いて、増殖定常期
の終末以内の期間まで培養し、次いで該培養液中
に非ペクチン質を炭素源とする栄養培地を加えて
培養することを特徴とするリポ多糖の製造方法。 2 ペクチン質と緩慢代謝性の炭素化合物とを組
合せたものを炭素源に用いた栄養培地で該細菌を
培養する事を特徴とする特許請求の範囲第1項記
載の方法。 3 非ペクチン質が緩慢代謝性の炭素化合物であ
る特許請求の範囲第1項記載の方法。
[Scope of Claims] 1. Bacteria of the genus Erwinia are cultured in a nutrient medium containing pectic substances as a carbon source until the end of the stationary growth phase, and then non-pectic substances are added to the culture medium as a carbon source. A method for producing lipopolysaccharide, which comprises adding and culturing a nutrient medium as a source. 2. The method according to claim 1, characterized in that the bacteria are cultured in a nutrient medium using a combination of pectin and a slowly metabolizing carbon compound as a carbon source. 3. The method according to claim 1, wherein the non-pectic substance is a slowly metabolizing carbon compound.
JP24492787A 1987-09-29 1987-09-29 Production of lipopolysaccharide Granted JPS6486892A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24492787A JPS6486892A (en) 1987-09-29 1987-09-29 Production of lipopolysaccharide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24492787A JPS6486892A (en) 1987-09-29 1987-09-29 Production of lipopolysaccharide

Publications (2)

Publication Number Publication Date
JPS6486892A JPS6486892A (en) 1989-03-31
JPH0560358B2 true JPH0560358B2 (en) 1993-09-02

Family

ID=17126039

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24492787A Granted JPS6486892A (en) 1987-09-29 1987-09-29 Production of lipopolysaccharide

Country Status (1)

Country Link
JP (1) JPS6486892A (en)

Also Published As

Publication number Publication date
JPS6486892A (en) 1989-03-31

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