JPH0773495B2 - Heat and salt resistant glutaminase - Google Patents
Heat and salt resistant glutaminaseInfo
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- JPH0773495B2 JPH0773495B2 JP24508687A JP24508687A JPH0773495B2 JP H0773495 B2 JPH0773495 B2 JP H0773495B2 JP 24508687 A JP24508687 A JP 24508687A JP 24508687 A JP24508687 A JP 24508687A JP H0773495 B2 JPH0773495 B2 JP H0773495B2
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- enzyme
- salt
- glutaminase
- glutamine
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Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は新規な耐熱・耐塩性グルタミナーゼに関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of use] The present invention relates to a novel heat- and salt-resistant glutaminase.
グルタミナーゼは食品工業、特に蛋白質を酵素的に分解
して調味食品を製造する場合に重要な役割を果たす酵素
である(例えば、特公昭49−48759号公報等参照)。Glutaminase is an enzyme that plays an important role in the food industry, particularly when a protein is enzymatically decomposed to produce a seasoned food (see, for example, Japanese Patent Publication No. 49-48759).
従来公知のグルタミナーゼは、上記した特公昭49−4875
9号公報記載のものを含め、何れも耐塩性が全くない
か、あるいは比較的弱いものであるため、このようなグ
ルタミナーゼを用いて食塩を多量に含む調味料等の食品
を製造するには問題があった。The conventionally known glutaminase is the above-mentioned Japanese Patent Publication No. 49-4875.
There is no salt tolerance at all, including those described in No. 9, or it is relatively weak, so there is a problem in producing foods such as seasonings containing a large amount of salt using such glutaminase. was there.
蛋白質を酵素的に分解する場合、原料蛋白質は種々の蛋
白質分解酵素の作用により、ペプタイドを経て最終的に
構成アミノ酸にまで分解される。斯かる場合に生成した
グルタミンは、グルタミナーゼ非存在下においては、非
酵素的に容易にフエノール臭、および苦味を有するピロ
グルタミン酸へと変化する。またグルタミンがプログル
タミン酸へ変化してゆく速度は高温になるほど増加す
る。このような分解系にグルタミナーゼを共存させれ
ば、グルタミンがピログルタミン酸になる変化を防止す
ることが可能であるのみならず、遊離のグルタミンに見
合う量のグルタミン酸に転換されることが知れている。
食塩存在下において高温で蛋白質を酵素的に分解し、ア
ミノ酸調味食品を製造することは、蛋白質の分解速度を
高め、雑菌による汚染を極力防止し優良な調味料を製造
する手段として極めて有効な方法である。しかしなが
ら、このような条件を採用するためには使用するグルタ
ミナーゼが耐熱性および耐塩性を有することが必要であ
る。When a protein is enzymatically decomposed, a raw material protein is finally decomposed into constituent amino acids through peptides by the action of various proteolytic enzymes. Glutamine produced in such a case is easily converted into pyroglutamic acid having a phenol odor and a bitter taste in a non-enzymatic manner in the absence of glutaminase. Also, the rate of conversion of glutamine to proglutamic acid increases as the temperature increases. It is known that coexistence of glutaminase in such a decomposition system can prevent glutamine from changing into pyroglutamic acid, and can be converted into glutamic acid in an amount commensurate with free glutamine.
Producing amino acid seasoned foods by enzymatically decomposing proteins at high temperature in the presence of salt is an extremely effective method as a means for producing good seasonings by increasing the rate of protein degradation and preventing contamination by various bacteria as much as possible. Is. However, in order to adopt such conditions, it is necessary that the glutaminase used has heat resistance and salt resistance.
斯かる現状に鑑み、本発明者は高濃度の食塩を含有する
食品の製造に用いることのできる耐熱・耐塩性グルタミ
ナーゼを提供すべく鋭意検討を重ねた結果、新たにプレ
ラ属に属する菌の培養物から耐熱性、耐塩性に優れ、か
つ食品衛生上問題のない新規なグルタミナーゼが得られ
ることを見出し、本発明を完成した。In view of such a current situation, the present inventor has conducted extensive studies to provide a heat-resistant and salt-tolerant glutaminase that can be used for the production of foods containing high-concentration salt, and as a result, newly cultivated bacteria belonging to the genus Prera. It was found that a novel glutaminase excellent in heat resistance and salt resistance and free from food hygiene problems can be obtained from a product, and the present invention has been completed.
すなわち、本発明はブレラ属に属する菌により生産され
る次の理化学的性質を有する耐熱・耐塩性グルタミナー
ゼを提供するものである。That is, the present invention provides a thermostable and salt-tolerant glutaminase produced by a bacterium belonging to the genus Brera and having the following physicochemical properties.
(a) 作 用 L−グルタミンを加水分解してL−グルタミン酸とアン
モニアを生成する酵素である。(A) Working This is an enzyme that hydrolyzes L-glutamine to produce L-glutamic acid and ammonia.
(b) 基質特異性 L−グルタミンに対するKm値(ミカエリス定数)は、30
℃、pH7.5(リン酸緩衝液)で8.1×10-4Mである。(B) Substrate specificity The Km value (Michaelis constant) for L-glutamine is 30.
It is 8.1 × 10 -4 M at pH 7.5 (phosphate buffer) at ℃.
(c) 至適pH及び定数pH定数 至適pHはL−グルタミンを基した場合5.0〜9.0であり、
安定pH範囲は5.〜8.0である。(C) Optimum pH and constant pH constant The optimum pH is 5.0 to 9.0 based on L-glutamine,
The stable pH range is 5.-8.0.
(d) 耐熱性 pH7.5にて各温度で30分間保存したときのグルタミナー
ゼ活性の残存率は、50℃で90%以上、60℃で71%であ
る。(D) Thermostable The residual rate of glutaminase activity when stored at pH 7.5 for 30 minutes at each temperature is 90% or more at 50 ° C and 71% at 60 ° C.
(e) 耐塩性 食塩非存在下での酵素活性を100%とした場合、10%w/
v)食塩濃度で約80%以上の相対活性を示し、20%(w/
v)食塩濃度で約70%以上の相対活性を示す(pH7.5、30
℃)。(E) Salt Tolerance 10% w / when the enzyme activity in the absence of salt is 100%
v) Relative activity of about 80% or more at salt concentration, 20% (w /
v) About 70% or more relative activity at salt concentration (pH 7.5, 30
C).
(f) 分子量 約150,000(ゲル過法) 以下、本発明の耐熱・耐塩性酵素の理化学的性質につい
て詳細に説明する。(F) Molecular weight about 150,000 (gel permeation method) Hereinafter, the physicochemical properties of the heat and salt tolerant enzyme of the present invention will be described in detail.
(1) 作 用 本酵素は、L−グルタミンを加水分解してL−グルタミ
ン酸とアンモニアを生成する酵素である。(1) Operation This enzyme is an enzyme that hydrolyzes L-glutamine to produce L-glutamic acid and ammonia.
(2) 基質特異性 第1表に示す各基質(0.25M)1.0mlを0.4Mリン酸緩衝液
(pH7.5)0.25mlに加え、これに本酵素1.25mlを加え30
℃で60分間反応させた。これに0.75N過塩素酸液0.625ml
を添加して反応を停止させ、0.75N水酸化ナトリウム0.6
25mlを加えて反応液を中和させた。なお、ブランク値は
本酵素1.25mlに0.75N過塩素酸液0.625mlを加え、これに
各基質及び緩衝液(pH7.5)を夫々、1.0ml、0.25ml加え
た液を上記と同条件で処理したもの(反応時間が0時間
のもの)を用いた。(2) Substrate specificity 1.0 ml of each substrate (0.25M) shown in Table 1 was added to 0.25 ml of 0.4M phosphate buffer (pH 7.5), and 1.25 ml of this enzyme was added to this.
The reaction was carried out at 60 ° C for 60 minutes. 0.75N perchloric acid solution 0.625ml
Was added to stop the reaction, and 0.75N sodium hydroxide 0.6
The reaction solution was neutralized by adding 25 ml. The blank value was obtained by adding 0.75N perchloric acid solution 0.625 ml to 1.25 ml of this enzyme, and adding 1.0 ml and 0.25 ml of each substrate and buffer solution (pH 7.5) under the same conditions as above. The treated product (with a reaction time of 0 hours) was used.
次に、前記酵素反応により生成したアンモニアをF−キ
ツト尿素/アンモニア定量用キツト〔ベーリンガー社
製〕を用いて測定した。相対活性(%)は、L−グルタ
ミンを基質として酵素反応させて得られるアンモニア量
を100%とし、他の物質を基質とした場合の比較値
(%)で示した。Next, the ammonia produced by the enzyme reaction was measured using an F-kittourea / ammonia quantifying kit (manufactured by Boehringer). The relative activity (%) was shown as a comparative value (%) when the amount of ammonia obtained by enzymatic reaction with L-glutamine as a substrate was 100% and other substances were used as substrates.
本酵素のL−グルタミンに対するKm値(ミカエリス定
数)は30℃、pH7.5(リン酸緩衝液)で8.1×10-4Mであ
る。 The Km value (Michaelis constant) of this enzyme for L-glutamine is 8.1 × 10 −4 M at 30 ° C. and pH 7.5 (phosphate buffer solution).
(3) 至適pHおよび安定pH範囲 本酵素の至適pHはL−グルタミンを基質とした場合、第
1図に示す如く、pH5.0〜9.0である。なお第1図中○−
○はマクイルベイン緩衝液(pH4.5〜8.0)、△−△はリ
ン酸緩衝液(pH7.5〜9.0)を用いたものである。(3) Optimum pH and stable pH range When L-glutamine is used as a substrate, the optimum pH of this enzyme is pH 5.0 to 9.0, as shown in FIG. In addition, in Figure 1
◯ indicates that McIlvein buffer (pH 4.5 to 8.0) and Δ-Δ indicates that phosphate buffer (pH 7.5 to 9.0) was used.
また、安定pH範囲は、0.25単位の本酵素を含有する各緩
衝液6mlを30℃で24時間放置後、残存活性を測定するこ
とによつて調べた。その結果は第2図に示す如くであ
り、pH5.0〜8.0で安定であつた。なお第2図中、緩衝液
はマクイルベイン緩衝液(pH4.5〜8.0)を用いたもので
ある。The stable pH range was examined by measuring the residual activity after leaving 6 ml of each buffer solution containing 0.25 unit of the enzyme at 30 ° C. for 24 hours. The results are shown in Fig. 2, and were stable at pH 5.0 to 8.0. Incidentally, in FIG. 2, the buffer is a Macilvain buffer (pH 4.5 to 8.0).
(4) グルタミナーゼ活性の測定法 250mM L−グルタミン溶液4.0mlに0.4Mリン酸緩衝液1.
0ml(pH7.5)及び本酵素液5.0mlを加え、30℃で60分間
反応させた後、沸騰水中で10分間加熱して反応を停止さ
せる。次に、ベーリンガー社製、L−グルタミン酸測定
用キツトにより上記の反応液0.2mlにトリエタノールア
ミン200mMを含む25mMリン酸緩衝液2.3ml(pH8.6)、6.7
mM NAD+溶液0.2ml、1.19mMヨードニトロテトラゾリウム
クロライド溶液0.2ml、0.1%(w/v)ジアホラーゼ溶液
0.05ml及びグルタミン酸脱水素酵素0.05mlを添加し、室
温で反応させ、分光光度計により492nmにおける吸光度
値を測定する。(4) Method for measuring glutaminase activity 0.4 M phosphate buffer solution was added to 4.0 ml of 250 mM L-glutamine solution.
Add 0 ml (pH 7.5) and 5.0 ml of this enzyme solution, react at 30 ° C for 60 minutes, and then heat in boiling water for 10 minutes to stop the reaction. Next, using a kit for measuring L-glutamic acid manufactured by Boehringer, 2.3 ml of 25 mM phosphate buffer solution (pH 8.6) containing 6.7 mM of 200 mM triethanolamine in 0.2 ml of the above reaction solution, 6.7.
mM NAD + solution 0.2 ml, 1.19 mM iodonitrotetrazolium chloride solution 0.2 ml, 0.1% (w / v) diaphorase solution
Add 0.05 ml and 0.05 ml glutamate dehydrogenase, react at room temperature, and measure the absorbance value at 492 nm with a spectrophotometer.
更に、予め作成したL−グルタミン酸の検量線より、そ
の生成量を求めた。30℃、1分間当り1マイクロモルの
L−グルタミン酸を生産する酵素量を1単位とした。Furthermore, the amount of L-glutamic acid produced was determined from the calibration curve prepared in advance. The amount of enzyme that produces 1 micromol of L-glutamic acid per minute at 30 ° C. was defined as 1 unit.
(5) 作用適温の範囲 第3図に示す如く、本酵素の作用適温の範囲は55〜65℃
にある(反応時間60分間・pH7.5)。(5) Optimum temperature range for action As shown in Fig. 3, the optimum temperature range for this enzyme is 55-65 ° C.
(Reaction time 60 minutes, pH 7.5).
(6) 熱安定性 本酵素を0.25単位含有する酵素液6ml(pH7.5)を各温度
に30分間放置し、残存する酵素活性量を測定した結果、
第4図に示す如く、60℃において70%の残存活性を示
し、50℃において95%の残存活性を示した。(6) Thermostability 6 ml of enzyme solution (pH 7.5) containing 0.25 unit of this enzyme was left at each temperature for 30 minutes, and the residual enzyme activity was measured.
As shown in FIG. 4, 70% residual activity was exhibited at 60 ° C. and 95% residual activity was exhibited at 50 ° C.
(7) 分子量 本酵素の分子量はセフアクリルS−300(フアルマシア
社製)を用い、ゲル過法により、0.2M食塩を含有する
0.1Mリン酸緩衝液(pH7.0)にて測定した結果、約15万
であつた。(7) Molecular Weight The enzyme has a molecular weight of 0.2M sodium chloride by gel permeation method using Cefacrylic S-300 (manufactured by Pharmacia).
As a result of measurement with 0.1 M phosphate buffer (pH 7.0), it was about 150,000.
(8) 耐塩性 本酵素を0.25単位含有する酵素液5.0mlに、反応液中食
塩濃度が0〜20%となるように食塩を加えた250mM L
−グルタミンを含有する0.4Mリン酸緩衝液5.0mlを加
え、酵素活性(pH7.5、30℃、反応時間60分)を調べ
た。その結果、第5図に示す如く、食塩非存在下での酵
素活性を100%とした場合、食塩濃度10%(w/v)では約
80%以上、20%(w/v)では約70%以上の相対活性を示
した。(8) Salt tolerance To 5.0 ml of enzyme solution containing 0.25 unit of this enzyme, salt was added so that the salt concentration in the reaction solution was 0 to 20% 250 mM L
-5.0 ml of 0.4 M phosphate buffer containing glutamine was added, and the enzyme activity (pH 7.5, 30 ° C, reaction time 60 minutes) was examined. As a result, as shown in Fig. 5, when the enzyme activity in the absence of salt was 100%, it was about 10% (w / v) in salt concentration.
The relative activity was 80% or higher, and about 70% or higher at 20% (w / v).
(9) 精製方法 本酵素は後記する精製方法により精製することが出来
る。(9) Purification method The present enzyme can be purified by the purification method described below.
(10) デイスク電気泳動 デーヴイス〔B.J.Davis,Ann.New York Acad.Sei.,121,4
04(1964)〕のpH8.9のゲルを用いて2mA/ゲル・カラム
で5℃,90分(分離用ゲルの泳動時間)泳動し、その後
アミドブラツクにて染色すると、陽極側に移動した単一
なバンドが認められた。(10) disc electrophoresis Devuisu [BJDavis, Ann.New York Acad.Sei., 121 , 4
04 (1964)] pH 8.9 gel was run on a 2 mA / gel column at 5 ° C for 90 minutes (migration time of the separating gel), and then stained with amide black, which migrated to the anode side. One band was recognized.
(11) 等電点 アンフオライン・キヤリアー・アンフオライト(pH3.5
〜10)を使用して本酵素の等電点を測定したところ、4.
5±0.2であつた。(11) Isoelectric point Ampholin, Carrier, Ampholite (pH3.5
~ 10) was used to measure the isoelectric point of this enzyme.
It was 5 ± 0.2.
以上の如く、本酵素はその酵素化学的、物理化学的な諸
性質が従来のグルタミナーゼの何れとも異つており、殊
に著しく耐熱性、耐塩性が強い。従つて、本酵素の高濃
度の食塩存在下での使用に際し、食塩により酵素活性が
ほとんど阻害されないため有利である。As described above, this enzyme is different from the conventional glutaminase in various enzymatic and physicochemical properties, and is particularly highly thermostable and salt resistant. Therefore, when the present enzyme is used in the presence of high-concentration salt, the salt hardly inhibits the enzyme activity, which is advantageous.
次に本発明に係る耐熱・耐食塩グルタミナーゼの製造法
について説明する。Next, a method for producing the heat-resistant and salt-resistant glutaminase according to the present invention will be described.
本発明において使用されるブレラ属に属する菌として
は、例えばブレラ・オリゼー(Bullera oryzae)JCM528
1が挙げられる。尚、この菌は理化学研究所に保存され
ていて常に何人も容易に入手できるものである。Examples of the bacterium belonging to the genus Brera used in the present invention include, for example, Brera oryzae JCM528.
One is. This bacterium is stored in RIKEN and is always easily available to any person.
ブレラ・オリゼーJCM5281を培養し、培養物より耐熱・
耐塩性グルタミナーゼを製造する方法は次の如くして実
施される。Brerera oryzae JCM5281 is cultivated and heat-resistant from the culture.
The method for producing salt-tolerant glutaminase is carried out as follows.
先ず、培養法としては、通常液体好気培養法が有利であ
り、例えばフラスコによる振盪培養法や通気撹拌装置の
付いたジヤーフアーメンター,タンクフアーメンター等
による好気培養法が挙げられる。培養温度は15〜30℃、
好ましくは20〜25℃であり、培養時間は通常16時間程度
以上である。First, as the culture method, a liquid aerobic culture method is usually advantageous, and examples thereof include a shake culture method using a flask and an aerobic culture method using a jar fermenter equipped with an aeration and stirring device, a tank fermenter, and the like. Culture temperature is 15 to 30 ℃,
The temperature is preferably 20 to 25 ° C., and the culture time is usually about 16 hours or longer.
また使用する培地としては、液体培地が好適であり、培
地に加えられる栄養源としては、一般に微生物を培養す
る際に用いられる種々の栄養源を使用できる。即ち、炭
素源としては、例えばグルコース、マルトース等の単糖
類や少糖類等が用いられ、窒素源としては、例えばペプ
トン、肉エキス、酵母エキス、コーンステイープリカ
ー、カザミノ酸、脱脂大豆抽出液、小麦グルテンの加水
分解物、アンモニウム塩、硝酸塩等が用いられる。この
他マグネシウム、カルシウム、ナトリウム、リン酸塩等
の塩類、微量栄養物質等を添加しても良い。The medium used is preferably a liquid medium, and various nutrient sources generally used for culturing microorganisms can be used as the nutrient source added to the medium. That is, as the carbon source, for example, glucose, maltose and other monosaccharides and oligosaccharides are used, and as the nitrogen source, for example, peptone, meat extract, yeast extract, corn steep liquor, casamino acid, defatted soybean extract, A hydrolyzate of wheat gluten, an ammonium salt, a nitrate or the like is used. In addition, salts such as magnesium, calcium, sodium and phosphate, trace nutrients and the like may be added.
このような培養法を用いて得られる培養液もしくは、該
培養液を過、遠心分離等により固液分離し、集菌して
得られる培養菌体に、細胞壁溶解酵素含有物、例えば細
胞壁溶解酵素生産能を有するリゾープス属起源の培養液
もしくは該培養液より得られる酵素液を加え、該グルタ
ミナーゼを可溶化させる。A culture solution obtained by using such a culture method, or a culture cell obtained by solid-liquid separation of the culture solution by centrifugation, centrifugation or the like, and collecting the cells, a cell wall lysing enzyme-containing substance, for example, a cell wall lysing enzyme The glutaminase is solubilized by adding a culture broth originating from the genus Rhizopus or an enzyme solution obtained from the culture broth having productivity.
なお、上記耐熱・耐塩性グルタミナーゼを可溶化する際
の温度は30〜50℃、好ましくは35〜45℃、液性はpH3.0
〜7.0、好ましくはpH4.0〜6.0、時間は2〜72時間、好
ましくは16〜48時間程度であり、作用時の細胞壁溶解酵
素含有濃度は0.1%(w/v)以上、好ましくは0.5〜1.5%
(w/v)程度である。The temperature for solubilizing the heat- and salt-resistant glutaminase is 30 to 50 ° C, preferably 35 to 45 ° C, and the liquidity is pH 3.0.
~ 7.0, preferably pH 4.0 ~ 6.0, time is 2 ~ 72 hours, preferably about 16 ~ 48 hours, the concentration of cell wall lysing enzyme during action is 0.1% (w / v) or more, preferably 0.5 ~ 1.5%
(W / v).
得られた耐塩性グルタミナーゼ含有液より該酵素を採取
する手段としては、例えば本酵素含有液を常法により遠
心分離して菌体を除去し、更に必要により透析、イオン
交換樹脂に吸着、溶出させる方法、ゲル過等により本
発明に係る耐熱・耐塩性グルタミナーゼを単離すること
ができる。As a means for collecting the enzyme from the obtained salt-tolerant glutaminase-containing liquid, for example, the enzyme-containing liquid is centrifuged by a conventional method to remove bacterial cells, and further dialyzed, if necessary, adsorbed on an ion exchange resin and eluted. The heat- and salt-resistant glutaminase according to the present invention can be isolated by a method, gel filtration, or the like.
本発明に係る耐熱・耐塩性グルタミナーゼは、高濃度の
食塩存在下においても食塩により酵素の活性がほとんど
阻害されないため、高濃度の食塩を含む調味料等の食品
を製造するのに用いれば、旨味成分であるグルタミン酸
が著しく増強された食品を効率良く得ることができ、食
品生産上極めて有意義である。The heat- and salt-tolerant glutaminase according to the present invention has almost no inhibition of the enzyme activity by salt even in the presence of high-concentration salt, so if it is used for producing a food such as a seasoning containing high-concentration salt, the umami taste is improved. It is possible to efficiently obtain a food in which glutamic acid, which is a component, is remarkably enhanced, which is extremely significant in food production.
以下に本発明の実施例示す。 Examples of the present invention are shown below.
実施例1 プレラ・オリゼー(Bullera Oryzae)JCM5281を500ml坂
口フラスコ中でグルコース1%、酵母エキス0.3%、麦
芽エキス0.3%、ペプトン0.5%を含みpH5.5に調整した
液体培地100mlに植菌し、25℃、48時間培養した。この
種培養物を5ジヤーフアーメンター中、上記の組成と
同じ培地3に接種し、通気量1/min、撹拌速度300r
pmの条件下で25℃、48時間培養し、培養物を遠心分離機
にて遠心分離して集菌した。Example 1 Bullera Oryzae JCM5281 was inoculated in a 500 ml Sakaguchi flask in 100 ml of a liquid medium containing glucose 1%, yeast extract 0.3%, malt extract 0.3% and peptone 0.5% and adjusted to pH 5.5, It was cultured at 25 ° C for 48 hours. This seed culture was inoculated into the medium 3 having the same composition as described above in a 5-jar fermenter, the aeration rate was 1 / min, and the stirring speed was 300r.
After culturing at 25 ° C. for 48 hours under the condition of pm, the culture was centrifuged with a centrifuge to collect the cells.
得られた菌体のうち、150gに0.2M酢酸緩衝液(pH5.0)
を1加え、菌をよく分散させた。次に、これに細胞壁
溶解酵素としてグルクザイム6000(天野製薬社製)を8g
加え、40℃で16時間撹拌し、その後遠心分離後にて遠心
分離(10000rpm、10分間)して上清液を得た。Of the cells obtained, 150 g of 0.2 M acetate buffer (pH 5.0)
1 was added to disperse the bacteria well. Next, 8 g of Gluczyme 6000 (manufactured by Amano Pharmaceutical Co., Ltd.) as a cell wall lytic enzyme was added to this.
In addition, the mixture was stirred at 40 ° C. for 16 hours, then centrifuged and then centrifuged (10,000 rpm, 10 minutes) to obtain a supernatant.
上記の上清液に、0.02M酢酸緩衝液(pH5.0)で緩衝化し
たアンバーライトCG−50を添加し、1時間撹拌して酵素
を吸着させ、0.02M酢酸緩衝液(pH5.0)で良く洗浄し、
続いて7%(w/v)硫酸アンモニウム(pH7.0)で溶出し
て活性区分を集めた。Amberlite CG-50 buffered with 0.02M acetate buffer (pH 5.0) was added to the above supernatant, and the mixture was stirred for 1 hour to adsorb the enzyme, and 0.02M acetate buffer (pH 5.0) was added. Wash well with
Then, the active fraction was collected by elution with 7% (w / v) ammonium sulfate (pH 7.0).
次に、この酵素溶液に硫酸アンモニウムを0.8飽和とな
るように加えた後、遠心分離機にて、遠心分離(10,000
rpm、10分間)して沈澱物を得た。Next, ammonium sulfate was added to this enzyme solution to 0.8 saturation, followed by centrifugation (10,000
At 10 rpm for 10 minutes), a precipitate was obtained.
得られた沈澱物を0.02Mリン酸緩衝液(pH6.5)にて溶解
し、さらに0.02Mリン酸緩衝液(pH6.5)で透析し、粗酵
素液を得た。The obtained precipitate was dissolved in 0.02 M phosphate buffer (pH 6.5) and dialyzed against 0.02 M phosphate buffer (pH 6.5) to obtain a crude enzyme solution.
上記の粗酵素液を、0.02Mリン酸緩衝液(pH6.5)で緩衝
化したDEAE−トヨパール650Mカラム(東洋ソーダ社製)
に通し、酵素を吸着させ、0.02M酢酸緩衝液(pH6.5)で
よく洗浄し、続いてNaCl0〜0.5モルの濃度勾配で溶出し
て活性区分を集めた。次にこの酵素溶液を限外過装置
(分画膜10,000,アミコン社製)にて濃縮した。濃縮さ
れた酵素液を0.2Mの食塩を含む0.1Mリン酸緩衝液(pp7.
0)で緩衝化しておいたセフアクリルS−300を充填した
カラム(5.0×80cm)にかけゲル過した。DEAE-Toyopearl 650M column (manufactured by Toyo Soda Co., Ltd.) obtained by buffering the above crude enzyme solution with 0.02M phosphate buffer (pH 6.5)
The enzyme was adsorbed through the column, washed well with 0.02 M acetate buffer (pH 6.5), and then eluted with a concentration gradient of NaCl 0 to 0.5 mol to collect the active fraction. Next, this enzyme solution was concentrated with an ultrafiltration device (fractionation membrane 10,000, manufactured by Amicon). The concentrated enzyme solution was added with 0.1 M phosphate buffer solution containing 0.2 M sodium chloride (pp. 7.
The gel was applied to a column (5.0 × 80 cm) packed with Cefacrylic S-300 buffered in (0).
得られた活性区分を限外過装置にて濃縮し単一な酵素
標品4.7mgを得た。その結果、本酵素の比活性は5.5単位
/mgであつた。The obtained active fraction was concentrated with an ultrafiltration device to obtain 4.7 mg of a single enzyme preparation. As a result, the specific activity of this enzyme was 5.5 units.
It was / mg.
実施例2 ブレラ・オリゼー(Bullera Oryzae)JCM5281を500ml坂
口フラスコ中でグルコース1%、酵母エキス0.3%、麦
芽エキス0.3%、ペプトン0.5%を含みpH5.5に調整した
液体培地100mlに植菌し、25℃、48時間培養した。この
種培養物を5ジヤーフアーメンター中、上記の組成と
同じ培地3に接種し、通気量1/min、撹拌速度300r
pmの条件下で25℃、48時間培養し、培養物を遠心分離機
にて遠心分離して集菌した。Example 2 Bullera Oryzae JCM5281 was inoculated in a 500 ml Sakaguchi flask into 100 ml of a liquid medium containing glucose 1%, yeast extract 0.3%, malt extract 0.3% and peptone 0.5% and adjusted to pH 5.5, It was cultured at 25 ° C for 48 hours. This seed culture was inoculated into the medium 3 having the same composition as described above in a 5-jar fermenter, the aeration rate was 1 / min, and the stirring speed was 300r.
After culturing at 25 ° C. for 48 hours under the condition of pm, the culture was centrifuged with a centrifuge to collect the cells.
得られた菌体のうち、150gに0.2M酢酸緩衝液(pH5.0)
を1加え、菌をよく分散させた。次に、細胞壁溶解酵
素としてグルクザイム6000(天野製薬社製)を0.02M酢
酸緩衝液に溶解し、0.02M酢酸緩衝液(pH5.0)で緩衝化
したセフアデツクスG−50(フアルマシア社製)を充填
したカラム(580cm)にかけゲル過し、得られた細胞
壁溶解活性を有する画分を全量加えて、40℃、16時間撹
拌し、その後、遠心分離機にて遠心分離(10,000rpm,10
分間)して上静液を得た。Of the cells obtained, 150 g of 0.2 M acetate buffer (pH 5.0)
1 was added to disperse the bacteria well. Next, Gluczyme 6000 (manufactured by Amano Pharmaceutical Co., Ltd.) as a cell wall lysing enzyme was dissolved in 0.02M acetate buffer and filled with Sephadex G-50 (manufactured by Pharmacia) buffered with 0.02M acetate buffer (pH 5.0). The gel was applied to a column (580 cm), and the whole amount of the obtained fraction having cell wall lysing activity was added, and the mixture was stirred at 40 ° C for 16 hours and then centrifuged (10,000 rpm, 10 rpm).
To give a supernatant.
上記の上静液に、0.02M酢酸緩衝液(pH5.0)で緩衝化し
たアンバーライトCG−50添加し、1時間撹拌して酵素を
吸着させ、0.02M酢酸緩衝液(pH5.0)で良く洗浄し、続
いて7%(w/v)硫酸アンモニウム(pH7.0)で溶出して
活性区分を集めた。次にこの酵素溶液に硫酸アンモニウ
ムを0.8飽和となるように加えた後、遠心分離機にて遠
心分離(10,000rpm,10分間)して沈澱を得た。得られた
沈澱物を0.02Mリン酸緩衝液(pH6.5)にて溶解し、さら
に0.02Mリン酸緩衝液(pH6.5)で透析し、粗酵素液を得
た。Amberlite CG-50 buffered with 0.02M acetate buffer (pH 5.0) was added to the above supernatant and stirred for 1 hour to adsorb the enzyme, and then 0.02M acetate buffer (pH 5.0) was added. The active fraction was collected by thorough washing, followed by elution with 7% (w / v) ammonium sulfate (pH 7.0). Next, ammonium sulfate was added to this enzyme solution so as to have a saturation of 0.8, and then centrifuged (10,000 rpm, 10 minutes) with a centrifuge to obtain a precipitate. The obtained precipitate was dissolved in 0.02 M phosphate buffer (pH 6.5) and dialyzed against 0.02 M phosphate buffer (pH 6.5) to obtain a crude enzyme solution.
上記の粗酵素液を、0.02Mリン酸緩衝液(pH6.5)で緩衝
化したDEAE−トヨパール650M(東洋ソーダ社製)に通
し、酵素を吸着させ、0.02Mリン酸緩衝液(pH6.5)でよ
く洗浄し、続いてNaCl0〜0.5Mの濃度勾配で溶出して活
性区分を集めた。次に、この酵素溶液を限外過装置
(分画膜10,000,アミコン社製)にて濃縮した。濃縮さ
れた酵素液を0.2Mの食塩を含む0.1Mリン酸緩衝液(pH7.
0)で緩衝化しておいたセフアクリルS−300を充填した
カラム(5×80cm)にかけゲル過した。The above crude enzyme solution was passed through DEAE-Toyopearl 650M (manufactured by Toyo Soda Co., Ltd.) buffered with 0.02 M phosphate buffer (pH 6.5) to adsorb the enzyme, and 0.02 M phosphate buffer (pH 6.5). ), Followed by elution with a concentration gradient of NaCl 0 to 0.5 M to collect active fractions. Next, this enzyme solution was concentrated with an ultrafiltration device (fractionation membrane 10,000, manufactured by Amicon). The concentrated enzyme solution was added with 0.1 M phosphate buffer (pH 7.
The gel was applied to a column (5 × 80 cm) packed with Cefacrylic S-300 buffered in (0).
得られた活性区分を0.02M酢酸緩衝液(pH5.0)で透析
し、0.02M酢酸緩衝液(pH5.0)で緩衝化したDEAE−トヨ
パール650M(東洋ソーダ社製)に通し、酵素を吸着さ
せ、0.02M酢酸緩衝液(pH5.0)でよく洗浄し、続いてNa
Cl0〜0.1Mの濃度勾配で溶出して活性区分を集めた。次
に、この酵素溶液を限外過装置(分画膜10,000,アミ
コン社製)にて濃縮した。濃縮された酸素液を0.2Mの食
塩を含む0.1Mリン酸緩衝液(pH7.0)で緩衝化しておい
たセフアクリルS−300を充填したカラム(5×80cm)
にかけゲル過した。得られた活性区分を限外過装置
にて濃縮し、単一な酵素標品1.15mgを得た。この結果、
本酵素の比活性は22.5単位/mgであつた。The obtained active fraction was dialyzed against 0.02M acetate buffer (pH 5.0) and passed through DEAE-Toyopearl 650M (manufactured by Toyo Soda) buffered with 0.02M acetate buffer (pH 5.0) to adsorb the enzyme. And wash well with 0.02M acetate buffer (pH 5.0), followed by Na
The active fractions were collected by elution with a gradient of Cl0 to 0.1M. Next, this enzyme solution was concentrated with an ultrafiltration device (fractionation membrane 10,000, manufactured by Amicon). A column (5 x 80 cm) packed with Cefacryl S-300 in which the concentrated oxygen solution was buffered with 0.1 M phosphate buffer (pH 7.0) containing 0.2 M sodium chloride.
I ran through the gel. The obtained active fraction was concentrated with an ultrafiltration device to obtain 1.15 mg of a single enzyme preparation. As a result,
The specific activity of this enzyme was 22.5 units / mg.
第1図は本酵素の至適pHを示す図面、第2図は安定pH範
囲を示す図面、第3図は作用適温の範囲を示す図面、第
4図は熱安定性を示す図面、第5図は耐塩性を示す図面
である。FIG. 1 is a drawing showing the optimum pH of the enzyme, FIG. 2 is a drawing showing a stable pH range, FIG. 3 is a drawing showing a suitable temperature range of action, FIG. 4 is a drawing showing thermostability, and FIG. The figure is a drawing showing salt resistance.
フロントページの続き (72)発明者 田中 俊夫 滋賀県長浜市神前町10―52 エクセレント 神前105号 (72)発明者 原 文雄 埼玉県川越市大字的場947―3 (72)発明者 祢宜 博 埼玉県入間郡大井町緑ケ岡2―23―16Front page continuation (72) Inventor Toshio Tanaka 10-52 Kamimae-cho, Nagahama-shi, Shiga Excellent No. 105 Kamimae (72) Inventor Fumio Hara 947-3, Masagoba, Kawagoe-shi, Saitama Prefecture (72) Hiroshi Nagi, Saitama Prefecture 2-23-16 Midorigaoka, Oi-cho, Iruma-gun
Claims (1)
理化学的性質を有する耐熱・耐塩性グルタミナーゼ。 (a) 作用 L−グルタミンを加水分解してL−グルタミン酸とアン
モニアを生成する酵素である。 (b) 基質特異性 L−グルタミンに対するKm値(ミカエリス定数)は、30
℃、pH7.5(リン酸緩衝液)で8.1×10-4Mである。 (c) 至適pH及び安定pH範囲 至適pHはL−グルタミンを基質とした場合5.0〜9.0であ
り、安定pH範囲は5.0〜8.0である。 (d) 耐熱性 pH7.5にて各温度で30分間保存したときのグルタミナー
ゼ活性の残存率は、50℃で90%以上、60℃で71%であ
る。 (e) 耐塩性 食塩非存在下での酵素活性を100%とした場合、10%(w
/v)食塩濃度で約80%以上の相対活性を示し、20%(w/
v)食塩濃度で約70%以上の相対活性を示す(pH7.5、30
℃)。 (f) 分子量 約150,000(ゲル過法)1. A heat- and salt-resistant glutaminase having the following physicochemical properties, which is produced by a bacterium belonging to the genus Brera. (A) Action It is an enzyme that hydrolyzes L-glutamine to produce L-glutamic acid and ammonia. (B) Substrate specificity The Km value (Michaelis constant) for L-glutamine is 30.
It is 8.1 × 10 -4 M at pH 7.5 (phosphate buffer) at ℃. (C) Optimum pH and stable pH range The optimum pH is 5.0 to 9.0 when L-glutamine is used as a substrate, and the stable pH range is 5.0 to 8.0. (D) Thermostability The residual rate of glutaminase activity when stored at pH 7.5 for 30 minutes at each temperature is 90% or more at 50 ° C and 71% at 60 ° C. (E) Salt-tolerance 10% (w
/ v) Relative activity of about 80% or more at salt concentration, 20% (w /
v) About 70% or more relative activity at salt concentration (pH 7.5, 30
C). (F) Molecular weight about 150,000 (gel method)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24508687A JPH0773495B2 (en) | 1987-09-29 | 1987-09-29 | Heat and salt resistant glutaminase |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24508687A JPH0773495B2 (en) | 1987-09-29 | 1987-09-29 | Heat and salt resistant glutaminase |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6486873A JPS6486873A (en) | 1989-03-31 |
| JPH0773495B2 true JPH0773495B2 (en) | 1995-08-09 |
Family
ID=17128398
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24508687A Expired - Fee Related JPH0773495B2 (en) | 1987-09-29 | 1987-09-29 | Heat and salt resistant glutaminase |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0773495B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1290951A1 (en) * | 2001-09-10 | 2003-03-12 | Societe Des Produits Nestle S.A. | Glutaminase |
-
1987
- 1987-09-29 JP JP24508687A patent/JPH0773495B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6486873A (en) | 1989-03-31 |
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