JPH082297B2 - Alginic acid-degrading enzyme, its production method, bacteria used, and alginic acid-degrading method - Google Patents

Alginic acid-degrading enzyme, its production method, bacteria used, and alginic acid-degrading method

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Publication number
JPH082297B2
JPH082297B2 JP1230511A JP23051189A JPH082297B2 JP H082297 B2 JPH082297 B2 JP H082297B2 JP 1230511 A JP1230511 A JP 1230511A JP 23051189 A JP23051189 A JP 23051189A JP H082297 B2 JPH082297 B2 JP H082297B2
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JP
Japan
Prior art keywords
alginate
enzyme
degrading enzyme
optimum
alginic acid
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 - Fee Related
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JP1230511A
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Japanese (ja)
Other versions
JPH0394675A (en
Inventor
克巳 村田
和雄 村上
功 日下部
稔秀 佐藤
Original Assignee
株式会社紀文
株式会社紀文フードケミファ
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Priority to JP1230511A priority Critical patent/JPH082297B2/en
Priority to CA002005398A priority patent/CA2005398A1/en
Publication of JPH0394675A publication Critical patent/JPH0394675A/en
Priority to US08/132,223 priority patent/US5348875A/en
Publication of JPH082297B2 publication Critical patent/JPH082297B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

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  • Enzymes And Modification Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、エンテロバクター属菌によって生産された
アルギン酸分解酵素及びその製造法と使用菌並びにアル
ギン酸分解法に関するものである。
TECHNICAL FIELD The present invention relates to an alginate-degrading enzyme produced by an Enterobacter bacterium, a method for producing the same, a bacterium to be used, and an alginate-decomposing method.

本発明のアルギン酸分解酵素はエンテロバクター・ク
ロエカエ(Enterobacter cloacae)M−1菌によって著
量生産されるので、本酵素を用いてアルギン酸の部分分
解、分解等を行い、物性の変化をもたらして新らしいア
ルギン酸製品を製造したり、アルギン酸の構造の研究に
役立てるなど、本発明はきわめて有用である。
Since the alginic acid-degrading enzyme of the present invention is produced in a large amount by Enterobacter cloacae M-1 bacterium, this enzyme is used to partially decompose and decompose alginic acid to bring about a change in physical properties, which is likely to be new. The present invention is extremely useful for manufacturing alginic acid products and for studying the structure of alginic acid.

(従来技術及び問題点) 従来、アルギン酸分解酵素はフラボバクテリウム属
菌、シュードモナス属菌(特開昭59−143597)やビブリ
オ属菌(日本水産学会誌55(4)、709〜713(1989)な
どによって生産されることが知られている。
(Prior Art and Problems) Conventionally, alginate-degrading enzymes are flavobacterium, Pseudomonas sp. (Japanese Patent Laid-Open No. 59-143597) and Vibrio sp. (Journal of the Fisheries Society of Japan 55 (4), 709-713 (1989). It is known to be produced by

しかしながら、近時、アルギン酸の加工、処理等にお
いてアルギン酸分解酵素の需要が高まり、よりすぐれた
アルギン酸分解酵素の大量生産が望まれているのであ
る。
However, in recent years, the demand for alginate-degrading enzymes has increased in the processing and treatment of alginate, and there has been a demand for superior mass production of alginate-degrading enzymes.

(問題点を解決するための手段) 本発明者らは、アルギン酸分解酵素を著量生産する菌
株を求めて鋭意探索したところ、アルギン酸抽出残渣を
廃棄した土壌からアルギン酸分解酵素を著量生産する細
菌一株を分離するに到った。この細菌をM−1菌と名付
け、分類検索を行ったところエンテロバクター・クロエ
カエに属するものと認められた。また、M−1菌は微工
研にFERM BP−2577として寄託されている。
(Means for Solving the Problems) The inventors of the present invention have made an intensive search for a strain that produces a large amount of alginic acid degrading enzyme, and found that a bacterium that produces a large amount of alginic acid degrading enzyme from soil in which the alginic acid extraction residue was discarded. It came to separate one strain. This bacterium was designated as M-1 bacterium, and when classified and searched, it was recognized as belonging to Enterobacter chloecae. In addition, M-1 bacterium has been deposited as FERM BP-2577 at the Micro Incorporated Research Institute.

エンテロバクター・クロエカエM−1菌の菌学的性質
は次の通りである。
The mycological properties of Enterobacter chloecae M-1 are as follows.

形態 桿菌 グラク染色性 − 芽胞 − 運動性 + オキシダーゼ − カタラーゼ + OF F グルコースからのガスの産生 + インドール産生 − メチルレッド − V−P + クエン酸塩利用 + 硫化水素産生 − 尿素分解 − フェニルアラニン脱アミノ − リジン脱炭酸 − アルギニンジヒドロラーゼ + オルニチン脱炭素 + ゼラチン液化 − 硝酸塩還元 + ONPG + 黄色色素の産生 − 酸の産生 アドニトール − アラビノース + イノシトール − シュークロース + ズルシトール − ソルビトール + マンニトール + メリビオース + ラクトース + ラムノース + エンテロバクター・クロエカエM−1菌の増殖はきわ
めて速く、菌の増殖にともなってアルギン酸分解酵素の
活性も高まり、本培養を開始して12時間後に最高に達す
る。
Morphology Bacillus Grac stain − Spores − Motility + Oxidase − Catalase + OF F Gas production from glucose + Indole production − Methyl red − VP + citrate utilization + Hydrogen sulfide production − Urea decomposition − Phenylalanine deamino − Lysine decarboxylation-Arginine dihydrolase + Ornithine decarbonation + Gelatin liquefaction-Nitrate reduction + ONPG + Yellow pigment production-Acid production Adonitol-Arabinose + Inositol-Sucrose + Dulucitol-Sorbitol + Mannitol + Mellibiose + Lactose enol The growth of Bacterus chloejeae M-1 bacterium is extremely fast, and the activity of alginate-degrading enzyme increases with the growth of the bacterium, and reaches its maximum 12 hours after starting the main culture.

本菌の培養培地としては、アルギン酸ソーダを適量含
有し、その他窒素源、無機塩類を含むものが使用され
る。ここで窒素源としては、ペプトン、酵母エキス、硫
安、硝安などがあり、また、無機塩類としては、燐酸1
カリ、燐酸2カリ、硫酸マグネシウムなどが適宜使用さ
れる。
As a culture medium for the bacterium, a medium containing an appropriate amount of sodium alginate, a nitrogen source, and inorganic salts is used. Here, as the nitrogen source, there are peptone, yeast extract, ammonium sulfate, ammonium nitrate and the like, and as inorganic salts, phosphoric acid 1
Potassium, 2 potassium phosphate, magnesium sulfate and the like are used as appropriate.

培養温度は30〜40℃で、通気撹拌培養によって、約12
時間程度で酵素生産量が最高になるまで培養される。
The culture temperature is 30 to 40 ° C, and about 12
Incubate for about an hour until the enzyme production reaches the maximum.

アルギン酸分解酵素は菌体外に生成するので、得られ
た培養液を10,000G程度で遠心分離し、上清を酵素液と
して得る。
Since alginate-degrading enzyme is produced outside the cells, the obtained culture solution is centrifuged at about 10,000 G to obtain the supernatant as the enzyme solution.

本酵素は、得られた上清液からアセトン分画、硫安分
画、DEAE−Sephadex A−50、CM−Sephadex C−50などの
イオン交換クロマトグラフィー、Bio−Gel P−100によ
るゲルろ過、Hydroxyapatiteによる吸着クロマトグラフ
ィーなどによって精製することができる。
The enzyme was subjected to ion fractionation chromatography such as acetone fractionation, ammonium sulfate fractionation, DEAE-Sephadex A-50, CM-Sephadex C-50, etc. from the obtained supernatant, gel filtration by Bio-Gel P-100, Hydroxyapatite. Can be purified by adsorption chromatography or the like.

アセトン分画は、冷アセトン2に対して粗酵素液1を
ゆっくり加えて行った。しかし、粗酵素液中の残存アル
ギン酸の沈殿も同時に起こってしまい、回収率が10%未
満とかなり低い。
Acetone fractionation was performed by slowly adding the crude enzyme solution 1 to 2 parts of cold acetone. However, precipitation of residual alginic acid in the crude enzyme solution also occurred at the same time, and the recovery rate was considerably low at less than 10%.

硫安分画は、20,40,60,80,90%の各飽和硫安により行
った。その結果、90%飽和硫安での沈殿分画で最もよい
回収率が得られ、およそ70%であった。しかしこの場合
も硫安分画後の上清には約25%の活性が残存していた。
Ammonium sulfate fractionation was performed with 20, 40, 60, 80, 90% saturated ammonium sulfate. As a result, the best recovery was obtained in the precipitation fraction with 90% saturated ammonium sulfate, which was about 70%. However, in this case as well, about 25% of the activity remained in the supernatant after the ammonium sulfate fractionation.

イオン交換クロマトグラフィーは、0.02Mのリン酸1
カリウムbuffer(pH7.8)を用いてカラムを平衡化し、
そこに同bufferで透析した粗酵素液を供することにより
行った。また溶出は同bufferでのNaClグラジエントによ
り行った。その結果、本酵素はDEAE−Sephadex A−50で
は非吸着画分として溶出され、その回収率は65%、精製
倍率は15倍であった。CM−Sephadex C−50の場合には吸
着画分として溶出され、その回収率は25%、精製倍率は
35倍であった。なお、本酵素が金属イオン要求性である
ことより、同bufferに1mMのカルシウムを加えて同様にC
M−Sephadex C−50を行った。その結果、回収率は45
%、精製倍率は90倍に上昇した。。Bio−Gel P−100に
よるゲロろ過は、0.02Mのリン酸1カリウムbuffer(pH
7.8)でカラムを平衡化させた後に、粗酵素液を供する
ことにより行った。その結果、回収率は42%で、精製倍
率は34倍であった。
Ion exchange chromatography shows 0.02M phosphoric acid 1
Equilibrate the column with potassium buffer (pH 7.8),
It was carried out by supplying a crude enzyme solution dialyzed with the same buffer thereto. Elution was performed with a NaCl gradient in the same buffer. As a result, this enzyme was eluted as a non-adsorbed fraction in DEAE-Sephadex A-50, the recovery rate was 65%, and the purification rate was 15 times. In the case of CM-Sephadex C-50, it was eluted as an adsorption fraction, the recovery rate was 25%, and the purification rate was
It was 35 times. Since the enzyme is auxotrophic for metal ions, 1 mM calcium was added to the same buffer to give C
M-Sephadex C-50 was performed. As a result, the recovery rate is 45
%, The purification rate increased to 90 times. . Gelo filtration with Bio-Gel P-100 is performed with 0.02M monopotassium phosphate buffer (pH
After equilibrating the column in 7.8), the crude enzyme solution was supplied. As a result, the recovery rate was 42% and the purification rate was 34 times.

吸着クロマトグラフィーは、0.02Mのリン酸1カリウ
ムbuffer(pH7.8)で平衡化したカラムに、同bufferで
透析した粗酵素液を供することにより行った。また溶出
は0.2Mのリン酸1カリウムbuffer(pH7.8)で行った。
その結果、回収率は80%で、精製倍率は3.3倍であっ
た。
The adsorption chromatography was carried out by supplying a crude enzyme solution dialyzed with the same buffer to a column equilibrated with 0.02 M monopotassium phosphate buffer (pH 7.8). The elution was performed with 0.2 M potassium phosphate buffer (pH 7.8).
As a result, the recovery rate was 80% and the purification rate was 3.3 times.

本発明においては、培養上清酵素液、濃縮液、アセン
ト分画等の粗酵素、各種精製手段による精製酵素などい
ずれも本発明のアルギン酸分解酵素となり、それぞれの
用途に応じて使用することができるものである。
In the present invention, a culture supernatant enzyme solution, a concentrated solution, a crude enzyme such as ascent fractionation, a purified enzyme obtained by various purification means, etc. all become the alginate-degrading enzyme of the present invention, and can be used according to each application. It is a thing.

次に、実施例1で得た上清アルギン酸分解酵素液を用
いて測定した本発明のアルギン酸分解酵素の理化学的性
質を示す。
Next, the physicochemical properties of the alginate-degrading enzyme of the present invention measured using the supernatant alginate-degrading enzyme solution obtained in Example 1 are shown.

1.作用 アルギン酸に作用し、アルギン酸をリアーゼ的に脱離
分解する。
1. Action It acts on alginic acid, and desorbs and decomposes alginic acid like lyase.

2.基質特異性 アルギン酸をリアーゼ的に脱離分解し、不飽和ウロン
酸もしくは不飽和ウロン酸残基を持つオリゴ糖を生成す
る。
2. Substrate specificity Alginate is cleaved and decomposed by lyase to produce unsaturated uronic acid or oligosaccharide having unsaturated uronic acid residue.

1%アルギン酸ナトリウム(M/G=0.93)溶液(pH7.
8)と100℃で5分間加熱失活した粗酵素液を1:1で混合
し、ブランクとした。反応液は一定時間毎に200μlず
つサンプリングし、同様な処理を行った。続いて各サン
プルをTBA反応により測定した。つまりサンプル200μl
に0.025NのHI04を含む0.125N H2S04溶液0.25mlを加えて
20分間静置し、サンプルの過ヨウ素酸酸化を行った。こ
れに、2%の亜ヒ素酸ナトリウムを含む0.5N HCl溶液を
加えて2分間静置することにより反応を停止させ、その
後、0.3%のチオバルビツール酸溶液を2ml加え、100℃
の湯浴中で10分間加熱し、縮合反応を行った。赤色を呈
した反応液は、放冷後、吸光度計により548nmにおける
吸光度を測定した。ただし、548nmでの吸光度が1.0を越
える場合には、酵素反応液を蒸留水で適当に希釈し、TB
A反応での吸光度が1.0以下になるようにして測定した。
1% sodium alginate (M / G = 0.93) solution (pH 7.
8) and the crude enzyme solution which had been inactivated by heating at 100 ° C. for 5 minutes were mixed at a ratio of 1: 1 to give a blank. The reaction solution was sampled by 200 μl at regular intervals and subjected to the same treatment. Subsequently, each sample was measured by TBA reaction. That is, 200 μl of sample
It was added with 0.125NH 2 S0 4 solution 0.25ml containing HI0 4 of 0.025N
The sample was allowed to stand for 20 minutes to perform periodate oxidation of the sample. The reaction was stopped by adding 0.5N HCl solution containing 2% sodium arsenite and letting it stand for 2 minutes, and then 2 ml of 0.3% thiobarbituric acid solution was added to 100 ° C.
This was heated in a hot water bath for 10 minutes to carry out the condensation reaction. The reaction liquid showing red color was allowed to cool, and then the absorbance at 548 nm was measured with an absorptiometer. However, if the absorbance at 548 nm exceeds 1.0, dilute the enzyme reaction solution with distilled water and add TB
It was measured so that the absorbance in the A reaction was 1.0 or less.

結果は第1図に示される。 The results are shown in Figure 1.

第1図から明らかなように、本酵素による不飽和ウロ
ン酸もしくは不飽和ウロン酸残基を持つオリゴ糖の生成
は6時間でほぼ終了する。
As is clear from FIG. 1, the production of unsaturated uronic acid or oligosaccharide having an unsaturated uronic acid residue by this enzyme is almost completed in 6 hours.

また、アルギン酸から赤色化合物の生成系は次の通り
である。
The system for producing a red compound from alginic acid is as follows.

3.作用pHおよび安定pH 第2図Aに酵素反応の至適pHが7.8であることが示さ
れ、第2図Bに安定pHが示される。第2図Bにおいて、
各種のpHで30℃、3時間処理した後の酵素の残存活性
は、pH8付近では安定であったが、pH6.5以下およびpH9
以上では50%以下に低下した。
3. Action pH and stable pH Fig. 2A shows that the optimum pH of the enzyme reaction is 7.8, and Fig. 2B shows the stable pH. In FIG. 2B,
The residual activity of the enzyme after treatment at 30 ℃ for 3 hours at various pHs was stable around pH8, but below 6.5 and pH9.
Above, it fell to below 50%.

4.作用温度および温度安定性 第2図Cに示すように、酵素反応の至適温度は35℃で
あり、各種温度でpH7.8で3時間処理後の酵素の残存活
性は、30℃までは安定であったが、温度の上昇と共に残
存活性は低下し、60℃では完全に失活した(第2図
D)。
4. Action temperature and temperature stability As shown in Fig. 2C, the optimum temperature of the enzyme reaction is 35 ° C, and the residual activity of the enzyme after treatment for 3 hours at pH 7.8 at various temperatures is up to 30 ° C. Was stable, but the residual activity decreased with increasing temperature, and it was completely deactivated at 60 ° C (Fig. 2D).

5.金属塩の影響 第3図に酵素活性に対する金属塩の影響を示す。本酵
素の活性は1mMのEDTAの添加により強く阻害されたが、
その活性は、2mMのカドミウムやカルシウムなどの添加
により著しく賦活された。
5. Effect of metal salts Figure 3 shows the effect of metal salts on enzyme activity. The activity of this enzyme was strongly inhibited by the addition of 1 mM EDTA.
The activity was remarkably activated by the addition of 2 mM cadmium or calcium.

6.酵素作用によるアルギン酸Naの粘度低下 1%アルギン酸Na溶液(pH7.8)5mlに上清酵素液5ml
を加え、35℃でオストワルド粘度計による粘度の経時変
化を測定した。
6. Decrease in viscosity of sodium alginate due to enzymatic action 5 ml of supernatant enzyme solution in 5 ml of 1% sodium alginate solution (pH 7.8)
Was added and the change with time in viscosity was measured by an Ostwald viscometer at 35 ° C.

その結果を第4図に示す。5分間後の反応液の比粘度
(α)は0.83、60分間後は0.97に達し、最終的にはほぼ
純水と同じ値にまで粘度は低下した。
The results are shown in FIG. The specific viscosity (α) of the reaction solution after 5 minutes reached 0.83 and after 60 minutes reached 0.97, and finally the viscosity decreased to almost the same value as pure water.

第4図において、 to=O時における反応混合物の流下時間(秒) tt=t時における反応混合物の流下時間(秒) tw=水の流下時間(秒) を示す。In FIG. t o = falling time (second) of the reaction mixture at the time of 0 t t = falling time (second) of the reaction mixture at the time t t w = falling time of water (second)

7.アルギン酸Naの分解生成物 1%アルギン酸Na溶液(pH7.8)5mlに酵素液5ml加
え、35℃で酵素反応させ、反応液を経時的に採取し、生
成物の変化をTLCで追跡した(展開溶媒はn−ブタノー
ル:酢酸:水=5:2:3)。その結果を第5図に示す。
7. Degradation product of sodium alginate 5 ml of 1% sodium alginate solution (pH 7.8) was added with 5 ml of enzyme solution, and the enzyme reaction was carried out at 35 ° C. The reaction solution was sampled with time, and the change of the product was traced by TLC. (The developing solvent is n-butanol: acetic acid: water = 5: 2: 3). The result is shown in FIG.

8.アルギン酸Na分解物のチオバルビツール酸反応 1%アルギン酸Na溶液(pH7.8)5mlに酵素液5mlを加
え、35℃で酵素反応を行い、反応液を経時的に採取し、
チオバルビツール酸反応で生成する赤色化合物を548nm
で測定した。その結果を第1図に示す。反応の進行に伴
って548nmの吸光度は急激に上昇したことから、本酵素
はアルギン酸を脱離的に分解するリアーゼと認められ
る。
8. Thiobarbituric acid reaction of sodium alginate decomposition product Add 5 ml of enzyme solution to 5 ml of 1% sodium alginate solution (pH 7.8), carry out enzyme reaction at 35 ° C, and sample the reaction solution over time.
548 nm of red compound produced by thiobarbituric acid reaction
It was measured at. The results are shown in FIG. Since the absorbance at 548 nm increased rapidly with the progress of the reaction, this enzyme is considered to be a lyase that cleaves alginate desorbingly.

9.分子量 アルギン酸分解酵素の分子量は38,000(SDS−PAGE
法)である。
9. Molecular weight The molecular weight of alginate degrading enzyme is 38,000 (SDS-PAGE
Law).

次に、本発明の実施例を示す。 Next, examples of the present invention will be described.

実施例1 B培地組成:アルギン酸Na1.0%。、ペプトン0.6%、
酵母エキス0.3%、KH2P04 0.5%およびMgS04・7H2 0.05
%。
Example 1 B medium composition: Na alginate 1.0%. , Peptone 0.6%,
0.3% yeast extract, KH 2 P0 4 0.5% and MgS0 4 · 7H 2 0.05
%.

エンテロバクター・クロエカエM−1菌、FERM BP−2
577を上記B培地組成の培地に植菌し、35℃で24時間振
とう培養して種菌液を得た。
Enterobacter chloecae M-1 bacterium, FERM BP-2
577 was inoculated into the medium having the above-mentioned medium B composition and shake-cultured at 35 ° C. for 24 hours to obtain a seed culture solution.

上記B培地組成の培地6.4lを10l培養槽に仕込み、120
℃で20分間オートクレーブで殺菌した後、35℃に冷却す
る。
Prepare 6.4 liters of the above medium B composition in a 10 liter culture tank and
Sterilize by autoclaving at ℃ for 20 minutes, then cool to 35 ℃.

この培地に上記種菌液600mlを培養槽に植菌し、35
℃、350〜450rpm、通気量1.5l/分で培養した。
This culture medium was inoculated with 600 ml of the above inoculum solution in a culture tank,
Culturing was carried out at a temperature of 350 to 450 rpm and an aeration rate of 1.5 l / min.

第6図に酵素生産の経時変化を示す。 Figure 6 shows the time course of enzyme production.

酵素生産は培養開始12時間後に最高に達した。培養終
了後、10,000Gで20分間遠心分離によって除菌した上清
をアルギン酸分解酵素液とした。
Enzyme production reached a maximum 12 hours after the start of culture. After completion of the culture, the supernatant obtained by removing the bacteria by centrifugation at 10,000 G for 20 minutes was used as an alginate-degrading enzyme solution.

得られたアルギン酸分解酵素液中の酵素活性は20×10
-3u/mlであった。
The enzyme activity in the obtained alginate-degrading enzyme solution was 20 × 10
-3 u / ml.

なお、アルギン酸分解酵素の活性測定法は以下に示す
とおりである。1mM CaCl2を含むトリス塩酸緩衝液にア
ルギン酸Naが1%濃度になるように溶解した溶液0.5ml
に酵素液0.5mlを加え、35℃で30分間反応させ、チオバ
ルビツール酸法により活性を測定した。酵素活性は、同
条件下で1分間に1μモルのウロン酸相当物を生成する
酵素量を1単位とした。
The method for measuring the activity of alginate-degrading enzyme is as follows. 0.5 ml solution of Na alginate dissolved in Tris-HCl buffer containing 1 mM CaCl 2 to a concentration of 1%
The enzyme solution (0.5 ml) was added to the mixture, the mixture was reacted at 35 ° C for 30 minutes, and the activity was measured by the thiobarbituric acid method. The enzyme activity was defined as 1 unit of the amount of enzyme that produced 1 μmol of uronic acid equivalent per minute under the same conditions.

実施例2 D−マンニュロン酸(M)とL−グルロン酸(G)の
M/G比が0.93であるアルギン酸ナトリウム1%水溶液(p
H7.8)5mlに実施例1で得た上清アルギン酸分解酵素液5
mlを加え、35℃で酵素反応を行った。
Example 2 of D-mannuronic acid (M) and L-guluronic acid (G)
1% aqueous solution of sodium alginate with M / G ratio of 0.93 (p
H7.8) 5 ml of the supernatant alginate-degrading enzyme solution 5 obtained in Example 1
ml was added, and the enzyme reaction was performed at 35 ° C.

反応液を経時的に採取し、チオバルビツール酸反応で
生成する赤色化合物を548nmで測定し、第1図の結果を
得た。
The reaction solution was sampled with time, and the red compound produced by the thiobarbituric acid reaction was measured at 548 nm to obtain the results shown in FIG.

【図面の簡単な説明】[Brief description of drawings]

第1図はM/G比が0.93のアルギン酸ナトリウムに本上清
アルギン酸分解酵素液を作用させて、チオバルビツール
酸反応で生成する赤色化合物を経時的に測定した図で、
第2図は本酵素の作用pH(A)、安定pH(B)、作用温
度(C)および温度安定性(D)を示す図で、第3図は
本酵素のEDTAによる阻害及び各種金属塩添加による賦活
を示す図で、第4図は本酵素作用によるアルギン酸Naの
粘度低下を示す図で、第5図は本酵素によるアルギン酸
Naの分解生成物の経時的変化を薄層クロマトグラフィー
追跡した図で、第6図は実施例1における培養と酵素生
産の経時変化を示す図である。
Fig. 1 is a graph showing the time course of the measurement of the red compound produced by the thiobarbituric acid reaction by allowing this supernatant alginate-degrading enzyme solution to act on sodium alginate with an M / G ratio of 0.93.
Fig. 2 shows the action pH (A), stable pH (B), action temperature (C) and temperature stability (D) of this enzyme. Fig. 3 shows the inhibition of this enzyme by EDTA and various metal salts. Fig. 4 is a diagram showing activation by addition, Fig. 4 is a diagram showing a decrease in viscosity of sodium alginate by the action of this enzyme, and Fig. 5 is an alginate by this enzyme.
FIG. 6 is a diagram showing changes over time in the decomposition products of Na by thin layer chromatography, and FIG. 6 is a diagram showing changes over time in culture and enzyme production in Example 1.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C12R 1:01) (C12N 1/20 C12R 1:01) ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C12R 1:01) (C12N 1/20 C12R 1:01)

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】エンテロバクター属に属するアルギン酸分
解酵素生産菌が生産し、下記の性質を有する、アルギン
酸をリアーゼ的に分解するアルギン酸分解酵素: (a)基質特異性 アルギン酸をリアーゼ的に脱離分解し、不飽和ウロン酸
もしくは不飽和ウロン酸残基を持つオリゴ糖を生成す
る。 (b)至適pH及び安定pH範囲 至適pHは7.8であり、安定pH範囲は5.5〜9.5である。 (c)至適温度及び作用温度範囲 至適温度は35℃であり、作用温度範囲は20〜40℃であ
る。 (d)分子量 38,000(SDS−PAGE法による)
1. An alginate-degrading enzyme which is produced by an alginate-degrading enzyme-producing bacterium belonging to the genus Enterobacter and has the following properties and which decomposes alginate in a lyase-like manner: (a) Substrate specificity Alginate is detached and decomposed in a lyase-like manner. Then, an unsaturated uronic acid or an oligosaccharide having an unsaturated uronic acid residue is produced. (B) Optimum pH and stable pH range The optimum pH is 7.8 and the stable pH range is 5.5 to 9.5. (C) Optimum temperature and working temperature range The optimum temperature is 35 ° C and the working temperature range is 20 to 40 ° C. (D) Molecular weight 38,000 (by SDS-PAGE method)
【請求項2】エンテロバクター属に属するアルギン酸分
解酵素生産菌を培養し、培養物からアルギン酸分解酵素
を採取することを特徴とするアルギン酸分解酵素の製造
法。
2. A method for producing an alginate-degrading enzyme, which comprises culturing an alginate-degrading enzyme-producing bacterium belonging to the genus Enterobacter and collecting the alginate-degrading enzyme from the culture.
【請求項3】エンテロバクター属に属するアルギン酸分
解酵素生産菌M−1菌。
3. An alginate-degrading enzyme-producing bacterium M-1 bacterium belonging to the genus Enterobacter.
【請求項4】エンテロバクター属に属し、下記の性質を
有するアルギン酸分解酵素を生産する微生物の培養物、
その処理物、粗酵素もしくは精製酵素をアルギン酸ナト
リウム含有液に添加し、作用せしめることを特徴とする
アルギン酸分解法: (a)基質特異性 アルギン酸をリアーゼ的に脱離分解し、不飽和ウロン酸
もしくは不飽和ウロン酸残基を持つオリゴ糖を生成す
る。 (b)至適pH及び安定pH範囲 至適pHは7.8であり、安定pH範囲は5.5〜9.5である。 (c)至適温度及び作用温度範囲 至適温度は35℃であり、作用温度範囲は20〜40℃であ
る。 (d)分子量 38,000(SDS−PAGE法による)
4. A culture of a microorganism which belongs to the genus Enterobacter and produces an alginate-degrading enzyme having the following properties:
An alginic acid decomposition method characterized by adding the treated product, a crude enzyme or a purified enzyme to a sodium alginate-containing solution and allowing them to act: (a) Substrate specificity Alginic acid is lyase-eliminating and decomposed to give unsaturated uronic acid or It produces oligosaccharides with unsaturated uronic acid residues. (B) Optimum pH and stable pH range The optimum pH is 7.8 and the stable pH range is 5.5 to 9.5. (C) Optimum temperature and working temperature range The optimum temperature is 35 ° C and the working temperature range is 20 to 40 ° C. (D) Molecular weight 38,000 (by SDS-PAGE method)
JP1230511A 1989-09-07 1989-09-07 Alginic acid-degrading enzyme, its production method, bacteria used, and alginic acid-degrading method Expired - Fee Related JPH082297B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP1230511A JPH082297B2 (en) 1989-09-07 1989-09-07 Alginic acid-degrading enzyme, its production method, bacteria used, and alginic acid-degrading method
CA002005398A CA2005398A1 (en) 1989-09-07 1989-12-13 Alginase and a process for production thereof and bacteria used, as well as a method for decomposition of alginic acid
US08/132,223 US5348875A (en) 1989-09-07 1993-10-06 Production of alginase from Enterobacter cloacae M-1 (FERM BP-2577)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1230511A JPH082297B2 (en) 1989-09-07 1989-09-07 Alginic acid-degrading enzyme, its production method, bacteria used, and alginic acid-degrading method

Publications (2)

Publication Number Publication Date
JPH0394675A JPH0394675A (en) 1991-04-19
JPH082297B2 true JPH082297B2 (en) 1996-01-17

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Country Status (2)

Country Link
JP (1) JPH082297B2 (en)
CA (1) CA2005398A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101239757B1 (en) * 2012-11-15 2013-03-06 주식회사 지디 Novel paenibacillus lautus gd-a2 producing breaking down alginate lyase, biocatalyst for alginic acid and method for manufacturing alginic acid oligosaccaride by using the same

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8283338B2 (en) 2007-11-30 2012-10-09 Kao Corporation GIP secretion inhibitor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101239757B1 (en) * 2012-11-15 2013-03-06 주식회사 지디 Novel paenibacillus lautus gd-a2 producing breaking down alginate lyase, biocatalyst for alginic acid and method for manufacturing alginic acid oligosaccaride by using the same

Also Published As

Publication number Publication date
CA2005398A1 (en) 1991-03-07
JPH0394675A (en) 1991-04-19

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