JPS6334B2 - - Google Patents

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Publication number
JPS6334B2
JPS6334B2 JP25919985A JP25919985A JPS6334B2 JP S6334 B2 JPS6334 B2 JP S6334B2 JP 25919985 A JP25919985 A JP 25919985A JP 25919985 A JP25919985 A JP 25919985A JP S6334 B2 JPS6334 B2 JP S6334B2
Authority
JP
Japan
Prior art keywords
enzyme
galactosidase
phosphate buffer
gel
present
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
JP25919985A
Other languages
Japanese (ja)
Other versions
JPS62118886A (en
Inventor
Ryuichi Matsuno
Kazuhiro Nakanishi
Mozafuaa Zaahitsudo
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.)
Daiwa Kasei KK
Original Assignee
Daiwa Kasei KK
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 Daiwa Kasei KK filed Critical Daiwa Kasei KK
Priority to JP25919985A priority Critical patent/JPS62118886A/en
Publication of JPS62118886A publication Critical patent/JPS62118886A/en
Publication of JPS6334B2 publication Critical patent/JPS6334B2/ja
Granted legal-status Critical Current

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  • Enzymes And Modification Thereof (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、β−ガラクトシダーゼの分離方法、
詳しくはβ−ガラクトシダーゼをより簡単な操作
で効率よく、基質特異性、殊にオリゴ糖生成能の
異なる2つのβ−ガラクトシダーゼに分離する改
良された方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention provides a method for isolating β-galactosidase,
Specifically, the present invention relates to an improved method for efficiently separating β-galactosidase into two β-galactosidases that differ in substrate specificity, particularly in oligosaccharide production ability, using simpler operations.

従来の技術 β−ガラクトシダーゼ(β−galactosidase)
は、ラクトース等に含まれるβ−ガラクトシド結
合の加水分解及びガラクトサイド転位反応を触媒
する酵素であり、国際生化学連合委員会の酵素番
号E.C.3.2.1.23に分類され、系統名ではβ−D−
ガラクトシド ガラクトハイドロラーゼ(β−D
−galactoside galactohydrolase)と呼ばれてい
る酵素である。本酵素としては、従来より各種微
生物例えばバチルス サーキユランス(Bacillus
circulans)、エシエリヒア コリー
(Escherichia coli)、クリベロミセス ラクテイ
ス(Kluyveromyces lactis)、アスペルギルス
オリゼー(Aspergillus oryzae)、アスペルギル
ス ニガー(Aspergillus niger)等を起源とす
るものの他、植物及び動物起源のものが知られて
いる。
Conventional technology β-galactosidase
is an enzyme that catalyzes the hydrolysis of β-galactoside bonds contained in lactose, etc. and galactoside rearrangement reaction, and is classified as enzyme number EC3.2.1.23 by the International Union of Biochemistry Committee, and its systematic name is β-D. −
Galactoside galactohydrolase (β-D
It is an enzyme called -galactoside (galactohydrolase). This enzyme has been used in various microorganisms such as Bacillus circulans.
circulans), Escherichia coli, Kluyveromyces lactis, Aspergillus
In addition to those originating from Aspergillus oryzae, Aspergillus niger, etc., those originating from plants and animals are known.

本発明者らは、先にバチルス サーキユランス
起源のβ−ガラクトシダーゼ標品(限外過によ
り精製したもの)につき、更にこれをセフアデツ
クスG−150によるゲル過、イオン交換クロマ
トグラフイー、ポリバツフアー交換体によるクロ
マトフオーカシング及びポリアクリルアミドゲル
を用いる電気泳動に従い精製する時には、上記酵
素が酵素形態の異なる2種のβ−ガラクトシダー
ゼ()及び()に各々分離精製されることを
見出した〔アグリカルチユラル アンド バイオ
ロジカル ケミストリー(Agric.Biol.Chem.)、
48(12)、3053−3061(1984)〕。
The present inventors previously obtained a β-galactosidase specimen (purified by ultrafiltration) originating from Bacillus circulans and further performed gel filtration using Sephadex G-150, ion exchange chromatography, and chromatography using a polybuffer exchanger. It has been found that when purified by focusing and electrophoresis using polyacrylamide gel, the above enzyme is separated and purified into two types of β-galactosidase () and () with different enzyme forms [Agricultural and Biological Chemistry (Agric.Biol.Chem.)
48(12), 3053-3061 (1984)].

発明が解決しようとする問題点 上記2種のβ−ガラクトシダーゼ()及び
()(以下単に「酵素」及び「酵素」と言う
ことがある)は、殊にそれらのオリゴ糖生成能に
おいて顕著な相違があり、之等の分離により、オ
リゴ糖生成能の非常に弱い酵素は、例えばミル
ク中のラクトースの分解に、またオリゴ糖生成能
の強い酵素は、ガラクトオリゴ糖の生産に、
各々有利に使用できると考えられた。しかしなが
ら上記分離方法は、非常に繁雑な工程と操作を要
し、工業的規模での実施は到底困難であり、上記
方法に代り、より簡単な操作で効率よく、上記酵
素ととを分離する方法の開発が望まれた。
Problems to be Solved by the Invention The two types of β-galactosidase () and () (hereinafter sometimes simply referred to as "enzyme" and "enzyme") have remarkable differences, especially in their oligosaccharide-producing ability. By separating these enzymes, enzymes with very weak oligosaccharide-producing ability can be used, for example, to degrade lactose in milk, and enzymes with strong oligosaccharide-producing ability can be used to produce galactooligosaccharides.
It was thought that each could be used advantageously. However, the above separation method requires very complicated steps and operations, and is completely difficult to implement on an industrial scale.Instead of the above method, there is a method that efficiently separates the enzyme with simpler operations. development was desired.

問題点を解決するための手段 上記現状に鑑み、本発明者らは先に開発した分
離精製法に見られる欠点を解消することを目的と
して鋭意研究を重ねた結果、ハイドロキシアパタ
イトゲルを用いるカラムクロマトグラフイーによ
れば、上記目的が達成されることを見出し、ここ
に本発明を完成するに至つた。
Means for Solving the Problems In view of the above-mentioned current situation, the present inventors have conducted extensive research with the aim of eliminating the shortcomings seen in the previously developed separation and purification method, and have developed a column chromatography method using hydroxyapatite gel. According to Graphi, it was discovered that the above object was achieved, and the present invention was completed.

即ち、本発明は、バチルス サーキユランス由
来のβ−ガラクトシダーゼをハイドロキシアパタ
イトゲルを用いたクロマトグラフイーによりオリ
ゴ糖生成能の異なるβ−ガラクトシダーゼとβ
ガラクトシダーゼとに分離することを特徴とす
るβ−ガラクトシダーゼの分離方法に係わる。
That is, the present invention uses β-galactosidase derived from Bacillus circulans to differentiate β-galactosidase and β-galactosidase having different oligosaccharide-producing abilities by chromatography using hydroxyapatite gel.
The present invention relates to a method for separating β-galactosidase and galactosidase.

本発明方法によれば、非常に容易な操作で効率
よく、上記酵素及びを分離することができ、
かくして分離された各酵素は、そのままで精製品
としてそれらの特性を利用した独自の用途に極め
て有効に利用できる。
According to the method of the present invention, the above-mentioned enzymes can be efficiently separated with a very easy operation,
Each of the enzymes thus isolated can be used as a purified product in an extremely effective manner for unique purposes that take advantage of their properties.

本発明方法においては、原料としてバチルス
サーキユランス由来のβ−ガラクトシダーゼを用
いる。該酵素は、前記文献にも記載される通り、
粉末形態で、又は限外過により部分精製された
溶液として入手できるが、例えばバチルス サー
キユランス(ATCC No.31382)等のバチルス
サーキユランスに属する公知の該酵素生産菌の培
養により得ることもできる。この培養による方法
及び得られる酵素の理化学的性質等は、例えば米
国特許第4237230号明細書に記載されている。
In the method of the present invention, Bacillus is used as a raw material.
β-galactosidase derived from P. circulans is used. The enzyme, as also described in the above-mentioned literature,
Bacillus circulans (ATCC No. 31382), which is available in powder form or as a partially purified solution by ultrafiltration,
It can also be obtained by culturing known enzyme-producing bacteria belonging to the genus Circulans. This culture method and the physicochemical properties of the resulting enzyme are described, for example, in US Pat. No. 4,237,230.

本発明では、上記β−ガラクトシダーゼを、ハ
イドロキシアパタイトゲルを用いたクロマトグラ
フイーに付すことを必須の要件とする。ここで用
いられるハイドロキシアパタイトとしては、公知
の各種のもの例えば「ヒドロキシアパタイト25%
solids No.HO252」(シグマ社製)の他、太平化
学産業社製造、半井化学社販売、日本ケミカル社
製製造、生化学工業社販売のヒドロキシアパタイ
トゲル等を例示できる。該ゲルを用いたクロマト
グラフイー操作は、通常のこの種クロマトグラフ
イー操作と同様のものとすることができ、一般に
は、適当なカラムに上記ゲルを充填し、これに酵
素液を通液してゲルに酵素を吸着させ、次いで吸
着された酵素を溶離させればよい。上記酵素の溶
離のための溶離液としては、リン酸バツフアを利
用できる。
In the present invention, it is essential that the β-galactosidase be subjected to chromatography using hydroxyapatite gel. As the hydroxyapatite used here, various known ones such as "Hydroxyapatite 25%
In addition to ``solids No. HO252'' (manufactured by Sigma), examples include hydroxyapatite gel manufactured by Taihei Kagaku Sangyo, sold by Hani Kagaku, manufactured by Nippon Chemical, and sold by Seikagaku Kogyo. Chromatography using this gel can be carried out in the same way as normal chromatography of this type, and generally involves filling a suitable column with the gel and passing the enzyme solution through it. The enzyme may be adsorbed onto the gel using a gel, and then the adsorbed enzyme may be eluted. A phosphate buffer can be used as an eluent for eluating the enzyme.

本発明方法は、特に上記リン酸バツフアによる
酵素の溶離を濃度勾配法に従い行なうのが適当で
ある。即ち、目的酵素の分離は、濃度を約20〜
300mMの範囲で次第に高濃度とした上記リン酸
バツフアを順次カラムに通液させることにより実
施できる。この操作により、まず約20mMリン酸
バツフアで夾雑蛋白が溶離し、110mMリン酸バ
ツフアで目的のβ−ガラクトシダーゼが、また
250〜300mMリン酸バツフアで目的のβ−ガラク
トシダーゼが各々溶離する。
In the method of the present invention, it is particularly appropriate to elute the enzyme using the above-mentioned phosphate buffer according to the concentration gradient method. That is, the separation of the target enzyme requires a concentration of approximately 20 to
This can be carried out by sequentially passing the above-mentioned phosphoric acid buffer with increasing concentration in the range of 300 mM through the column. Through this procedure, contaminant proteins are first eluted with approximately 20mM phosphate buffer, and the target β-galactosidase is eluted with 110mM phosphate buffer.
The β-galactosidase of interest is eluted with 250-300 mM phosphate buffer.

かくして両酵素の分離が行ない得る。分離され
たβ−ガラクトシダーゼ及びは、本発明者ら
が先に報告した文献に記載のそれらと作用、基質
特異性、至適PH、至適温度、分子量、温度安定
性、金属イオン及びその他の薬品の酵素活性に対
する影響等の理化学的性質において各々一致する
ものである。
Separation of both enzymes can thus be carried out. The isolated β-galactosidase and its interaction, substrate specificity, optimal pH, optimal temperature, molecular weight, temperature stability, metal ions, and other chemicals as described in the literature previously reported by the present inventors. They are the same in terms of physicochemical properties such as their effects on enzyme activity.

実施例 以下、本発明を更に詳しく説明するため実施例
を挙げる。
Examples Examples will be given below to explain the present invention in more detail.

尚、実施例におけるβ−ガラクトシダーゼ活性
は、以下の方法により測定した。
Note that β-galactosidase activity in Examples was measured by the following method.

<β−ガラクトシダーゼ活性> 0.25%2−ニトロフエニル−β−D−ガラクト
ピラノシド(ONPG)を含有する0.1M酢酸緩衝
液(PH6.0)4mlに本酵素1mlを加え、40℃で15
分間反応させた後、反応液1mlを10%炭酸ナトリ
ウム1mlに注入して反応を停止させ、生成したo
−ニトロフエノール量を測定してONPGの分解
量を求める。1分間に1μMのONPGを加水分解
する酵素量を1−ONPG単位とする。
<β-galactosidase activity> Add 1 ml of this enzyme to 4 ml of 0.1M acetate buffer (PH6.0) containing 0.25% 2-nitrophenyl-β-D-galactopyranoside (ONPG), and incubate at 40°C for 15 minutes.
After reacting for a minute, 1 ml of the reaction solution was poured into 1 ml of 10% sodium carbonate to stop the reaction, and the o
- Determine the amount of ONPG decomposed by measuring the amount of nitrophenol. The amount of enzyme that hydrolyzes 1 μM ONPG per minute is defined as 1-ONPG unit.

実施例 1 ラクトース0.3g、ポリペプトン3g、肉エ
キス1.5g及びNaCl0.2gを水に加えて全量を
100mlとし、PH7.0に調整後、これを坂口フラス
コに入れ、滅菌した。これにバチルス サーキ
ユランス(ATCC31382)の1白金耳を接種し、
38℃で1日間振盪培養した。
Example 1 Add 0.3 g of lactose, 3 g of polypeptone, 1.5 g of meat extract, and 0.2 g of NaCl to water and mix the whole amount.
The volume was adjusted to 100 ml, and after adjusting the pH to 7.0, it was placed in a Sakaguchi flask and sterilized. One platinum loop of Bacillus circulans (ATCC31382) was inoculated into this,
The cells were cultured with shaking at 38°C for 1 day.

下記各成分 ラクトース 48g 魚 粉 36g フアーマメデイア(トレーダーズオイルミル社
製) 18g コーンデイステイラーズソリユブル 10g 酵母エキス 1.95g CaCO3 4g (NH42SO4 1.5g MnCl2 0.02g Na2CO3 2.1g 大豆油 5ml をミニジヤーフアーメンターに入れ、水を加え
て1とした後、殺菌した。これに上記で得
た培養液10mlを接種し、38℃で2日間、通気攪
拌培養した。
Ingredients listed below: Lactose 48g Fish powder 36g Pharmamedea (Traders Oil Mill) 18g Corn Day Tailor's Soluble 10g Yeast extract 1.95g CaCO 3 4g (NH 4 ) 2 SO 4 1.5g MnCl 2 0.02g Na 2 CO 3 2.1 g of soybean oil (5 ml) was placed in a mini-jar fermentor, water was added to bring the volume to 1, and the mixture was sterilized. This was inoculated with 10 ml of the culture solution obtained above, and cultured with aeration at 38°C for 2 days.

上記で得られた培養液の一部を、遠心分離
して菌体を除き、酵素液を得た。この酵素液
を、55%飽和硫安塩析し、遠心分離により酵素
沈澱を得た。これを20mMリン酸バツフア(PH
6.0)に対して透析し、透析酵素液を得た。
A portion of the culture solution obtained above was centrifuged to remove bacterial cells to obtain an enzyme solution. This enzyme solution was subjected to salting out with 55% saturated ammonium sulfate, and centrifuged to obtain an enzyme precipitate. This was added to 20mM phosphate buffer (PH
6.0) to obtain a dialyzed enzyme solution.

この酵素液の総活性は4800 ONPG単位であ
つた。
The total activity of this enzyme solution was 4800 ONPG units.

ヒドロキシアパタイトゲル(半井化学社)60
mlをカラムに充填し、室温で20mMリン酸バツ
フア(PH6.0)250mlを通液させ、次いで上記
で得た酵素液を通液させ、酵素を吸着させた。
Hydroxyapatite gel (Hani Kagakusha) 60
ml was packed into a column, and 250 ml of 20 mM phosphate buffer (PH6.0) was passed through the column at room temperature, and then the enzyme solution obtained above was passed through the column to adsorb the enzyme.

次に、上記カラムに20mMリン酸バツフア(PH
6.0)250ml、50mMリン酸バツフア(PH6.0)450
ml、110mMリン酸バツフア(PH6.0)450ml、150
mMリン酸バツフア(PH6.0)350ml、200mMリ
ン酸バツフア(PH6.0)500ml、250mMリン酸バ
ツフア(PH6.0)250mlを順次続けて通液させ、酵
素を溶離させた。
Next, add 20mM phosphate buffer (PH) to the above column.
6.0) 250ml, 50mM phosphate buffer (PH6.0) 450
ml, 110mM phosphate buffer (PH6.0) 450ml, 150
350 ml of mM phosphate buffer (PH6.0), 500 ml of 200 mM phosphate buffer (PH6.0), and 250 ml of 250 mM phosphate buffer (PH6.0) were sequentially passed through the tube to elute the enzyme.

上記による酵素の溶離曲線を第1図に示す。第
1図において縦軸は蛋白の280mμにおける吸光
度(UV280、実線で示す)及びβ−ガラクトシ
ダーゼのONPG活性(破線で示す)を表わし、
横軸は溶出量(ml)を示す。また図にはリン酸バ
ツフアの濃度を示した。
The elution curve of the enzyme obtained above is shown in FIG. In Figure 1, the vertical axis represents the absorbance of the protein at 280 mμ (UV280, shown by the solid line) and the ONPG activity of β-galactosidase (shown by the broken line).
The horizontal axis shows the elution volume (ml). The figure also shows the concentration of phosphate buffer.

上記第1図より明らかなように、β−ガラクト
シダーゼは、250mMリン酸バツフアで溶離さ
れ、β−ガラクトシダーゼは110mMリン酸バ
ツフアで溶離されることが判る。
As is clear from FIG. 1 above, β-galactosidase is eluted with 250 mM phosphate buffer, and β-galactosidase is eluted with 110 mM phosphate buffer.

かくして分離されたβ−ガラクトシダーゼ及
びは、それぞれ前記した文献に記載の理化学的
性質に一致する性質を有するものであつた。
The β-galactosidase thus isolated had properties consistent with the physicochemical properties described in the above-mentioned literature.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明実施例に従うβ−ガラクトシ
ダーゼの溶離曲線を示すものである。
FIG. 1 shows an elution curve of β-galactosidase according to an example of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 1 バチルス サーキユランス由来のβ−ガラク
トシダーゼをハイドロキシアパタイトゲルを用い
たクロマトグラフイーによりオリゴ糖生成能の異
なるβ−ガラクトシダーゼとβガラクトシダー
ゼとに分離することを特徴とするβ−ガラクト
シダーゼの分離方法。
1. A method for separating β-galactosidase, which comprises separating β-galactosidase derived from Bacillus circulans into β-galactosidase and β-galactosidase having different oligosaccharide-producing abilities by chromatography using hydroxyapatite gel.
JP25919985A 1985-11-18 1985-11-18 Separation of beta-galactosidase Granted JPS62118886A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25919985A JPS62118886A (en) 1985-11-18 1985-11-18 Separation of beta-galactosidase

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25919985A JPS62118886A (en) 1985-11-18 1985-11-18 Separation of beta-galactosidase

Publications (2)

Publication Number Publication Date
JPS62118886A JPS62118886A (en) 1987-05-30
JPS6334B2 true JPS6334B2 (en) 1988-01-05

Family

ID=17330755

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25919985A Granted JPS62118886A (en) 1985-11-18 1985-11-18 Separation of beta-galactosidase

Country Status (1)

Country Link
JP (1) JPS62118886A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0740870B2 (en) * 1991-07-26 1995-05-10 株式会社いかるが牛乳 Method for producing low-lactose milk
JPH0759176B2 (en) * 1992-03-18 1995-06-28 株式会社いかるが牛乳 Method for producing low-lactose milk

Also Published As

Publication number Publication date
JPS62118886A (en) 1987-05-30

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