JPH0640823B2 - Method for producing purified α-amylase-containing liquid - Google Patents

Method for producing purified α-amylase-containing liquid

Info

Publication number
JPH0640823B2
JPH0640823B2 JP62185460A JP18546087A JPH0640823B2 JP H0640823 B2 JPH0640823 B2 JP H0640823B2 JP 62185460 A JP62185460 A JP 62185460A JP 18546087 A JP18546087 A JP 18546087A JP H0640823 B2 JPH0640823 B2 JP H0640823B2
Authority
JP
Japan
Prior art keywords
amylase
starch
solution
liquid
purified
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
JP62185460A
Other languages
Japanese (ja)
Other versions
JPS6430583A (en
Inventor
昌彦 石田
良一 芳賀
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP62185460A priority Critical patent/JPH0640823B2/en
Publication of JPS6430583A publication Critical patent/JPS6430583A/en
Publication of JPH0640823B2 publication Critical patent/JPH0640823B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • 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)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、酵素の精製方法に係り、特に、純度の低い、
若しくは希薄なα−アミラーゼ含有溶液から、殿粉の液
化に好適で、純度が高く、かつ保存安定性の高い、精製
α−アミラーゼ含有濃縮液の製造方法に関する。
TECHNICAL FIELD The present invention relates to a method for purifying an enzyme, and particularly to a method with low purity,
Alternatively, the present invention relates to a method for producing a purified α-amylase-containing concentrated liquid, which is suitable for starch liquefaction from a dilute α-amylase-containing solution, has high purity, and has high storage stability.

〔従来の技術〕[Conventional technology]

現在、ぶどう糖や異性化糖は、殿粉をα−アミラーゼや
グルコアミラーゼを用いて加水分解して工業生産されて
いる。このように、アミラーゼやプロテアーゼをはじめ
とする高分子加水分解酵素は、天然高分子原料から有用
な低分子物質を工業生産するのに極めて有用である。
Currently, glucose and isomerized sugar are industrially produced by hydrolyzing starch with α-amylase and glucoamylase. As described above, polymer hydrolases such as amylase and protease are extremely useful for industrially producing useful low-molecular substances from natural polymer raw materials.

一般に、酵素は酵素生産菌を液体培養して製造される。
工業用酵素製剤としては、一般には培養液をそのまゝ
濃縮した濃縮液か、培養液若しくは培養液をそのまま
乾燥した粉末、あるいは部分精製して得られる濃縮液、
又はその乾燥粉末が用いられている。しかし、培養液
の濃縮液や粗乾燥品には、培養液中に含まれる有臭成分
及び着臭成分が多量に含まれるため、目的とする反応生
成物を分離精製する際、最終的に除去することが必要と
なつてくる。また、培養液中には、目的酵素を破壊する
プロテアーゼをも含むことが多い。
Generally, an enzyme is produced by liquid-culturing an enzyme-producing bacterium.
As an industrial enzyme preparation, generally, a concentrated solution obtained by concentrating the culture solution as it is, a culture solution or a powder obtained by directly drying the culture solution, or a concentrate solution obtained by partial purification,
Alternatively, its dry powder is used. However, concentrated liquids and roughly dried products of the culture broth contain large amounts of odorous and odorous components contained in the culture broth, so when the reaction product of interest is separated and purified, it is finally removed. It becomes necessary to do. Further, the culture solution often contains a protease that destroys the target enzyme.

特に細菌を酵素生産菌として酵素を培養生産する際には
プロテアーゼの副生を伴うことが多い。このため、酵素
反応を利用して、有用物質を生産する際には、これら不
利益となる不純物を除去することが必要となつてくる。
In particular, when a bacterium is cultured and produced by using a bacterium as an enzyme-producing bacterium, a protease is often produced as a by-product. Therefore, it is necessary to remove these detrimental impurities when the useful substance is produced by utilizing the enzymatic reaction.

酵素の精製は、一般にモレキユラシーブ、イオン交換ク
ロマト、塩折、pH沈殿等の各種の物理的、化学的方法を
組合せた複雑なプロセスにより行うこととなり極めて多
大な労力、時間、経費を必要とする。
The purification of the enzyme is generally carried out by a complicated process in which various physical and chemical methods such as molecular sieve, ion exchange chromatography, salt folding, and pH precipitation are combined, which requires extremely great labor, time and cost.

一方、以前より、α−アミラーゼは基質の殿粉に選択的
に吸着することが知られており、殿粉粒子に吸着後、脱
着する方法も報告されている。しかし、脱着に際して
は、塩溶液、酸若しくはアルカリ溶液を脱離液として用
いることとなり、後処理として塩や酸、アルカリの除去
が必要となる。これらの精製した溶液中の酵素は重量濃
度では極めて希薄であるため、通常の工業的な方法では
損失が多く乾燥しにくい。また、精製した酵素の水溶液
は、室温下ではもちろん、冷所保存においても、失活す
るか、微生物の繁殖により失活するため、長期保存に耐
えず、実用的ではない。一方、これらの不安定性を解決
するため、α−アミラーゼを吸着した殿粉ケーキをその
まま乾燥し、これを酵素として用いることも考えられ
る。
On the other hand, it has long been known that α-amylase is selectively adsorbed to the substrate starch, and a method of adsorbing α-amylase to the starch particles and then desorbing it has also been reported. However, at the time of desorption, a salt solution, an acid or an alkali solution is used as a desorption solution, and it is necessary to remove the salt, acid or alkali as a post-treatment. Since the enzyme in these purified solutions is extremely dilute in weight concentration, it is difficult to dry due to many losses in the usual industrial method. Further, an aqueous solution of the purified enzyme is inactivated not only at room temperature but also when stored in a cold place, or is inactivated by the growth of microorganisms, so that it cannot withstand long-term storage and is not practical. On the other hand, in order to solve these instabilities, it is possible to dry the starch cake to which α-amylase is adsorbed and use it as an enzyme.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかし、このα−アミラーゼ吸着殿粉をα−アミラーゼ
として殿粉糊液の液化反応、すなわち、殿粉を原料とし
てぶどう糖、麦芽糖、異性化糖を製造する際の前工程、
を行おうとすると、原料の殿粉糊液は液化してデキスト
リンになるが、吸着剤として用いた殿粉粉末は液化せ
ず、溶解はしているが未分解の殿粉分子や殿粉の粒子の
状態で残つてしまうことを見出した。α−アミラーゼ吸
着殿粉として乾燥前の湿潤ケーキを用いても同様に分解
されにくいことがわかつた。したがつて、糖化反応に送
る前にこれら未分解の溶解あるいは未溶解の殿粉を分離
除去するか、糖化反応後、目的とする糖製品から分離除
去しなければならない。
However, this α-amylase-adsorbed starch is used as α-amylase in a liquefaction reaction of starch paste solution, that is, glucose, maltose, a pre-process when producing isomerized sugar from starch as a raw material,
The starch starch paste liquid as a raw material liquefies into dextrin, but the starch powder used as an adsorbent does not liquefy, but the dissolved but undegraded starch molecules and starch particles I found that it would remain in the state of. It was found that even if a wet cake before drying was used as the α-amylase-adsorbed starch, it was similarly difficult to decompose. Therefore, the undecomposed dissolved or undissolved starch must be separated and removed before being sent to the saccharification reaction, or must be separated and removed from the target sugar product after the saccharification reaction.

本発明の目的は、α−アミラーゼを含む純度の低い若し
くは希薄な溶液から効率良く該酵素を分離・濃縮して安
定な酵素水溶液を製造する方法を提供することにある。
An object of the present invention is to provide a method for producing a stable aqueous enzyme solution by efficiently separating and concentrating the enzyme from a low-purity or dilute solution containing α-amylase.

〔問題点を解決するための手段〕[Means for solving problems]

本発明を概説すれば、本発明は精製α−アミラーゼ含有
液の製造方法に関する発明であつて、粗α−アミラーゼ
含有溶液を、氷点を越えるが実質的に殿粉の液化反応が
起らない温度で殿粉粒子と接触させて、α−アミラーゼ
を殿粉粒子に吸着させる工程、該α−アミラーゼを吸着
した殿粉粒子を分離する工程、及び該分離した殿粉粒子
から得られるα−アミラーゼ含有液を、グルコアミラー
ゼ及びβ−アミラーゼの少なくとも一方を含有する酵素
で処理してオリゴ糖以下の分子量をもつ糖まで加水分解
する工程、の各工程を包含することを特徴とする。
Briefly describing the present invention, the present invention is an invention relating to a method for producing a purified α-amylase-containing liquid, in which a crude α-amylase-containing solution is heated at a temperature above the freezing point but substantially no liquefaction reaction of starch is caused. And a step of adsorbing α-amylase to the starch particles, separating the starch particles having adsorbed the α-amylase, and containing α-amylase obtained from the separated starch particles. Each step of treating the liquid with an enzyme containing at least one of glucoamylase and β-amylase to hydrolyze to a sugar having a molecular weight equal to or lower than that of an oligosaccharide is included.

以下、本発明について更に詳細に説明する。Hereinafter, the present invention will be described in more detail.

本発明方法に用いうるα−アミラーゼは特に限定はな
い。すなわち、細菌、糸状菌等各種の起源のα−アミラ
ーゼが用いられる。それ故、常温性のα−アミラーゼ、
及び耐熱性のα−アミラーゼのいずれでもよいが、特に
耐熱性のα−アミラーゼが有用である。したがつて、本
発明方法の原料である粗α−アミラーゼ含有溶液の例に
は、α−アミラーゼ生産菌の液体培養液から固形物を除
去した液、及び固体培養物若しくは培養菌体から抽出
し、固形物を除去した抽出液が挙げられる。
The α-amylase that can be used in the method of the present invention is not particularly limited. That is, α-amylases of various origins such as bacteria and filamentous fungi are used. Therefore, room temperature α-amylase,
And a heat-resistant α-amylase may be used, but a heat-resistant α-amylase is particularly useful. Therefore, examples of the crude α-amylase-containing solution, which is the raw material of the method of the present invention, include a liquid obtained by removing solids from a liquid culture of α-amylase-producing bacteria, and extraction from a solid culture or cultured cells. , An extract obtained by removing solid matter can be mentioned.

上記のような原料中のα−アミラーゼを殿粉粒子に吸着
させ、吸着した殿粉粒子を分離するのは、既述の公知の
常法で行うことができる。
Adsorption of the α-amylase in the raw material as described above to the starch particles and separation of the adsorbed starch particles can be carried out by the known conventional method described above.

こうして得られたα−アミラーゼ・殿粉複合体は、次の
処理を行う前に、実質的に殿粉の液化反応が起らない温
度の水で洗浄してもよく、またそうすることが好適であ
る。
The α-amylase-starch complex thus obtained may be washed with water at a temperature at which the starch liquefaction does not substantially occur before the next treatment, and it is preferable to do so. Is.

次いで、グルコアミラーゼ又はβ−アミラーゼ含有酵素
を作用させる方法としては、下記に述べるいくつかの方
法がある。
Next, there are several methods described below as the method for causing the glucoamylase- or β-amylase-containing enzyme to act.

(1) 上記複合体(すなわち、あらかじめ水洗を行つた
もの、又は水洗を行わないもののいずれでもよい。以下
同じ)を、水性スラリーとし、それに酵素を作用させ
る。
(1) The above-mentioned complex (that is, one that has been previously washed with water or one that has not been washed with water; the same applies hereinafter) is made into an aqueous slurry, and an enzyme is allowed to act on it.

(2) 上記(1)の方法において、殿粉の共存下に酵素を作
用させる。
(2) In the method of (1) above, the enzyme is allowed to act in the presence of starch.

(3) 複合体の水性スラリーに、あらかじめ殿粉を作用
させてヨード殿粉反応を陰性としてから酵素を作用させ
る。
(3) The starch is allowed to act in advance on the aqueous slurry of the complex to make the iodine starch reaction negative, and then the enzyme is allowed to act.

(4) 複合体の水性スラリーを加熱処理して、ヨード殿
粉反応を陰性としてから、殿粉の共存下又は不存在下に
酵素を作用させる。
(4) Heat the aqueous slurry of the complex to make the iodine starch reaction negative, and then act the enzyme in the presence or absence of starch.

(5) 複合体の水性スラリーを加熱処理し、ヨード殿粉
反応を陰性としたものに殿粉を作用させてデキストリン
化し、これに酵素を作用させる。いずれの方法において
も、複合体中の殿粉、及び必要に応じて添加した殿粉は
いずれも液化され、更にオリゴ糖以下の分子量をもつ糖
まで加水分解されて、本発明の殿粉及び高分子のデキス
トリンを含まない、精製α−アミラーゼ含有液を生成さ
せる。
(5) An aqueous slurry of the complex is heat-treated, and a substance having a negative iodine starch reaction is treated with starch to form dextrin, and the enzyme is allowed to act on the dextrin. In any of the methods, the starch in the complex and the starch added as necessary were both liquefied and further hydrolyzed to sugars having a molecular weight of oligosaccharide or less, and the starch and high starch of the present invention were obtained. A purified α-amylase-containing liquid, free of molecular dextrin, is produced.

使用する酵素は、グルコアミラーゼ及びβ−アミラーゼ
の少なくとも一方を含有していればよい。したがつて、
両酵素を併用して、同時に、又は別工程で経時的に使用
してもよい。更に他の酵素を同時に、又は別工程で経時
的に併用してもよい。
The enzyme used may contain at least one of glucoamylase and β-amylase. Therefore,
Both enzymes may be used in combination, simultaneously or in separate steps over time. Still another enzyme may be used simultaneously or in combination in a separate step over time.

併用してもよい他の酵素の例としては、α−アミラーゼ
はもちろんのこと、ブルラナーゼ及びグルコースイソメ
ラーゼが挙げられる。
Examples of other enzymes that may be used in combination include .alpha.-amylase, as well as bruranase and glucose isomerase.

また、反応におけるスラリーは、殿粉を30〜50重量
%含有するものが好適である。それは、30重量%未満
では酵素との反応が不充分となりやすく、他方50重量
%を越えると粘度が高くなつて、操作性が低下するから
である。
Further, the slurry in the reaction is preferably one containing 30 to 50% by weight of starch. This is because if it is less than 30% by weight, the reaction with the enzyme tends to be insufficient, while if it exceeds 50% by weight, the viscosity becomes high and the operability is deteriorated.

なお、原料酵素の起源、その形態については、特に制限
はない。
The source enzyme and its form are not particularly limited.

本発明方法によつて得られるα−アミラーゼ含有液は、
室温に10日間保存してもα−アミラーゼ活性が低下せ
ず、かつ微生物の繁殖も認められない極めて安定性の高
い溶液である。
The α-amylase-containing liquid obtained by the method of the present invention is
It is an extremely highly stable solution in which the α-amylase activity does not decrease even after storage at room temperature for 10 days, and the proliferation of microorganisms is not observed.

本発明による酵素液を用いて、殿粉糊の液化を行い、更
に糖化しても、各糖製品液中に未分解の殿粉や高分子の
デキストリンが混入することはなく、殿粉糊液の処理に
極めて有効である。
Using the enzyme solution according to the present invention, starch starch paste is liquefied and further saccharified, but undegraded starch and high-molecular-weight dextrin are not mixed in each sugar product solution. Is extremely effective for the treatment of.

また、本発明による酵素液は、好ましくない有臭、着色
成分を含まず、糖製品をこれらの不純物で汚染しないた
め、そのまま、あるいは濃縮して製品とすることができ
る。
Further, the enzyme solution according to the present invention does not contain an unpleasant odorous or coloring component and does not contaminate the sugar product with these impurities, so that it can be used as it is or concentrated to obtain a product.

〔実施例〕〔Example〕

以下、本発明を実施例により更に具体的に説明するが、
本発明はこれら実施例に限定されない。
Hereinafter, the present invention will be described in more detail with reference to Examples.
The present invention is not limited to these examples.

なお、各例中の%は、特に断らない限り、重量/重量で
ある。
In addition,% in each example is weight / weight unless otherwise specified.

実施例1 可溶性殿粉1.6%、ポリペプトン0.6%、酵母エキ
ス0.5%、りん酸第1カリウム0.7%、りん酸第2
ナトリウム0.35%、硫酸マグネシウム・7水和物
0.001%及び水道水を含む液体倍地(pH 6.0)を、
内容積5の培養槽に1.52kg分注し、120℃で2
0分間殺菌する。これに上記と同組成の培地を用いて嫌
気的に培養した耐熱性α−アミラーゼ生産菌〔クロスツ
リジウム(Clostridium)属細菌RS-0001、微工研条寄第1
043号(FERM BP-1043)〕の菌体懸濁液80gを添加
した。次いで、培養槽気相部をアルゴンガスで置換後、
嫌気条件下で培養した。培養槽内のpHを6.0に、温度
を60℃に自動調整しながら46時間培養した。この培
養液を6000rpmで10分間、遠心分離して菌体を除
去し、α−アミラーゼ活性4.8単位/mlの培養液
1.5を得た。本培養液中には無機塩1.1%、α−
アミラーゼ以外の有機物を2.3%含む。また、本培養
液の固形分当りの比活性は98.2単位/gであつ
た。
Example 1 Soluble starch 1.6%, polypeptone 0.6%, yeast extract 0.5%, potassium phosphate first 0.7%, phosphate second
Liquid medium (pH 6.0) containing 0.35% sodium, 0.001% magnesium sulfate heptahydrate and tap water,
Dispense 1.52 kg into a culture tank with an internal volume of 5 and
Sterilize for 0 minutes. A thermostable α-amylase-producing bacterium [Clostridium genus bacterium RS-0001, Microtechnology, Inc.
No. 043 (FERM BP-1043)] was added. Then, after replacing the gas phase portion of the culture tank with argon gas,
Cultured under anaerobic conditions. The culture was carried out for 46 hours while automatically adjusting the pH in the culture tank to 6.0 and the temperature to 60 ° C. This culture solution was centrifuged at 6000 rpm for 10 minutes to remove the cells, and a culture solution 1.5 having an α-amylase activity of 4.8 units / ml was obtained. Inorganic salt 1.1%, α-
Contains 2.3% of organic substances other than amylase. The specific activity of the main culture solution per solid content was 98.2 units / g.

特に有機物中には、酢酸、プロピオン酸を主成分とする
揮発性脂肪酸を約0.3%含むため、不快な酸臭と硫化
物臭を有する。
In particular, since the organic substance contains about 0.3% of volatile fatty acids containing acetic acid and propionic acid as main components, it has an unpleasant acid odor and sulfide odor.

次に、本培養液0.5(α−アミラーゼ2,100単位
含有、pH 6.0)を5℃に冷却し、局方の馬鈴しよ殿粉1
0gと水15gを混合した殿粉スラリー25gを添加
し、かくはん下で1分間保持した。上記の液を遠心分離
(3,000rpm、5分間)してα−アミラーゼ・殿粉
複合体のスラリー25gと清澄液0.5を得た。上記
清澄液について、α−アミラーゼ活性を測定した結果、
α−アミラーゼの90%をα−アミラーゼ・殿粉複合体
として回収したと推算した。
Next, 0.5 of the main culture broth (containing 2,100 units of α-amylase, pH 6.0) was cooled to 5 ° C.
25 g of starch slurry in which 0 g and 15 g of water were mixed was added, and the mixture was kept under stirring for 1 minute. The above liquid was centrifuged (3,000 rpm, 5 minutes) to obtain 25 g of a slurry of α-amylase / starch complex and 0.5 of a clear liquid. As a result of measuring the α-amylase activity of the above clarified liquid,
It was estimated that 90% of α-amylase was recovered as α-amylase-starch complex.

上記のα−アミラーゼ・殿粉複合体のスラリー25gを
60℃で1時間反応させた。その結果、反応液はヨード
殿粉反応で陰性を示し、液化反応が十分進行したことを
確認した。かつ反応液のα−アミラーゼ総活性を測定し
た結果、1856単位であり、培養液中に含まれていた
α−アミラーゼの88%が残存していることを把握し
た。また、本液はわずかな酸臭を有し、淡黄色を呈して
いる。本液の容積当りの比活性は74.2単位/mlであ
り、容積当り15.5倍に濃縮されている。本液は糖以
外の成分の乾物基準の比活性は5.46×103単位/
gとなり、培養液に対し57倍精製されている。
25 g of the slurry of the above α-amylase-starch complex was reacted at 60 ° C. for 1 hour. As a result, the reaction solution was negative in the iodine starch reaction, and it was confirmed that the liquefaction reaction proceeded sufficiently. Moreover, as a result of measuring the total activity of α-amylase in the reaction solution, it was 1856 units, and it was understood that 88% of the α-amylase contained in the culture solution remained. In addition, this solution has a slight acid odor and has a pale yellow color. The specific activity per volume of this solution was 74.2 units / ml, which was concentrated 15.5 times per volume. This liquid has a specific activity on a dry matter basis of components other than sugar of 5.46 × 10 3 units /
g, which is 57 times as purified as the culture solution.

本液5ml(α−アミラーゼ371単位含有)を、30%
馬鈴しよ殿粉スラリー1000gの100℃、10分加
熱処理したものに添加し、かくはん下70℃、1時間加
熱した。その結果、反応液はヨード殿粉反応が陰性を示
し、下記式: で定義されるデキストロース当量(Dextrose Equivale
nt)DEが12のデキストリン溶液1005gを得た。
30% of 5 ml of this solution (containing 371 units of α-amylase)
It was added to 1000 g of potato shiyo starch powder slurry which had been heat-treated at 100 ° C. for 10 minutes, and heated under stirring at 70 ° C. for 1 hour. As a result, the reaction solution showed a negative iodine starch reaction, and the following formula: Dextrose Equivale
nt) 1005 g of a dextrin solution with a DE of 12 were obtained.

本デキストリン液は無色で、50℃以上に加熱すると培
養液由来の酸臭が極くわずか感じられるが、室温では
無色無臭の透明な液体である。
The dextrin solution is colorless, and when heated to 50 ° C. or higher, a slight acid odor derived from the culture solution is felt, but it is a colorless and odorless transparent liquid at room temperature.

上記のデキストリン液100gにグルコアミラーゼ〔ア
スペルギルス・ニガー(Aspergillus niger)起源、常
温性〕(ノボインダストリー社製、商品名 アミログル
コシダーゼ・ノボAMG-200L、なお、本明細書の下記の実
施例及び比較例で使用しているグルコアミラーゼは、す
べてこのものを意味する)液をセロフアン半透膜チユー
ブに封入し、蒸留水に対して透析後、凍結乾燥して得た
精製粉末200単位(0.1g)を加えて溶解し、50
℃で48時間保温し、デキストリンをぶどう糖に加水分
解した。反応後のぶどう糖濃度は96.5%に達した。
本液は培養液由来の臭いや色もなく透明な液体である。
In 100 g of the above dextrin solution, glucoamylase [Aspergillus niger origin, room temperature] (Novo Industry Co., Ltd., trade name amyloglucosidase novo AMG-200L, the following Examples and Comparative Examples of the present specification) All the glucoamylases used in () mean this) 200 units (0.1 g) of purified powder obtained by encapsulating the liquid in a cellophane semipermeable membrane tube, dialyzing against distilled water, and freeze-drying. Add and dissolve, 50
The dextrin was hydrolyzed to glucose by incubating at 48 ° C for 48 hours. The glucose concentration after the reaction reached 96.5%.
This liquid is a transparent liquid without odor or color derived from the culture liquid.

本液を精製アミラーゼ溶液として、低温及び室温での保
存性を試験した。本液を2℃及び25℃に10日間及び
6か月間保存して、その酵素活性を測定した。その結
果、2℃保存では6か月保存でも99%以上、25℃、
6か月保存では98%以上の活性を保持していることを
確認した。
Using this solution as a purified amylase solution, the storage stability at low temperature and room temperature was tested. This solution was stored at 2 ° C. and 25 ° C. for 10 days and 6 months, and its enzyme activity was measured. As a result, when stored at 2 ° C, 99% or more even at 6 months storage, 25 ° C,
It was confirmed that 98% or more of the activity was retained after 6 months storage.

また、本液1ml(α−アミラーゼ7.4単位を含有)を
精製α−アミラーゼ含有溶液として、30%馬鈴しよ殿
粉スラリー200gに添加し、70℃、1時間加熱し
た。その結果、反応液はヨード殿粉反応が陰性を示し、
DEが12.5のデキストリン溶液を約200g得た。
本デキストリン液は、培養液由来の不快臭もなく無色透
明の液体である。
Further, 1 ml of this solution (containing 7.4 units of α-amylase) was added to 200 g of 30% potato starch starch slurry as a purified α-amylase-containing solution, and heated at 70 ° C. for 1 hour. As a result, the reaction solution showed a negative iodine starch reaction,
About 200 g of a dextrin solution having a DE of 12.5 was obtained.
The dextrin solution is a colorless and transparent liquid without unpleasant odor derived from the culture solution.

実施例2 実施例1と同様に培養して、培養液の固形分当り14
2単位/gの比活性をもつ培養液を得た。
Example 2 Culture was carried out in the same manner as in Example 1 to obtain 14 per solid content of the culture solution.
A culture broth having a specific activity of 2 units / g was obtained.

次にこの培養液を、馬鈴しよ殿粉と実施例1と同様に
反応させて、α−アミラーゼ・殿粉複合体のスラリー2
5gと清澄液0.5gを得た。
Next, this culture solution is reacted with potato starch and starch in the same manner as in Example 1 to prepare a slurry 2 of α-amylase / starch complex.
5 g and clear liquid 0.5 g were obtained.

上記スラリー25gに蒸留水100ml(5℃、pH 6.2)
を添加し、混合した後、遠心分離(3000rpm、5分間)
して、洗浄した複合体スラリー30gと、洗浄廃液95ml
を得た。上記清澄液と洗浄廃液とについて、α−アミラ
ーゼ活性を測定した結果、殿粉に吸着しなかつたα−ア
ミラーゼ活性は102単位以下であつた。したがつて、
供試培養液のα−アミラーゼの95%をα−アミラー
ゼ・殿粉複合体として回収したと推算した。
25 g of the above slurry, 100 ml of distilled water (5 ° C, pH 6.2)
After adding and mixing, centrifuge (3000 rpm, 5 minutes)
Then, washed composite slurry 30g and cleaning waste liquid 95ml
Got As a result of measuring the α-amylase activity of the clarified liquid and the washing waste liquid, the α-amylase activity that was not adsorbed on the starch was 102 units or less. Therefore,
It was estimated that 95% of α-amylase in the test culture solution was recovered as α-amylase-starch complex.

上記のα−アミラーゼ・殿粉複合体のスラリー30gを
60℃で1時間反応させた。その結果、反応液はヨード
殿粉反応で陰性を示し、液化反応が十分進行したことを
確認した。かつ反応液のα−アミラーゼ総活性を測定し
た結果、1990単位であり、培養液中に含まれてい
たα−アミラーゼの95%が残存していることを把握し
た。また、本液はほぼ無色透明、無臭であり、無機塩濃
度は0.01%以下であつた。なお、本液の容積当りの
比活性は74.2単位/mlであり、容積当り15.5倍
に濃縮されている。更に本液は糖以外の成分の乾物基準
の比活性は1.92×104単位/gとなり、培養液
に対し135倍に精製されている。
30 g of the slurry of the above α-amylase / starch complex was reacted at 60 ° C. for 1 hour. As a result, the reaction solution was negative in the iodine starch reaction, and it was confirmed that the liquefaction reaction proceeded sufficiently. Moreover, as a result of measuring the total activity of α-amylase in the reaction solution, it was found that it was 1990 units, and that 95% of α-amylase contained in the culture solution remained. The liquid was almost colorless and transparent and had no odor, and the inorganic salt concentration was 0.01% or less. The specific activity of this solution per volume was 74.2 units / ml, which was concentrated 15.5 times per volume. Furthermore, this liquid has a specific activity on a dry matter basis of components other than sugars of 1.92 × 10 4 units / g, and is purified 135 times that of the culture liquid.

本液5ml(α−アミラーゼ322単位含有)を、30%
馬冷しよ殿粉スラリー1000gに添加し、70℃で1
時間加熱して、ヨード殿粉反応が陰性を示し、DEが1
2のデキストリン溶液1005gを得た。
30% of 5 ml of this solution (containing 322 units of α-amylase)
Add to 1000g of horse-chilled starch powder slurry and add 1 at 70 ℃
After heating for an hour, the iodine starch reaction was negative and the DE was 1
1005 g of the dextrin solution of 2 was obtained.

本デキストリン液は培養液由来の臭いや色もない透明な
液体である。
This dextrin solution is a transparent liquid that has no odor or color derived from the culture solution.

上記のデキストリン液100gにグルコアミラーゼ(ア
スペルギルス・ニガー起源、常温性)の精製粉末180
単位(0.09g)を加えて溶解し、50℃で48時間
保温し、デキストリンをぶどう糖に加水分解した。反応
後のぶどう糖濃度は96.6%に達した。本ぶどう糖液は培
養液由来の臭いや色もなく透明な液体である。
Purified powder of glucoamylase (originating from Aspergillus niger, room temperature) 180 g in 100 g of the above dextrin solution
A unit (0.09 g) was added and dissolved, and the mixture was kept at 50 ° C. for 48 hours to hydrolyze dextrin into glucose. The glucose concentration after the reaction reached 96.6%. This glucose solution is a transparent liquid without odor or color derived from the culture solution.

また、本液1ml(α−アミラーゼ6.4単位含有)を精
製α−アミラーゼ溶液として、30%馬冷しよ殿粉スラ
リー200gの100℃、10分加熱処理したものに添
加し、70℃、1時間加熱した。その結果、反応液はヨ
ード殿粉反応が陰性を示し、DEが12.4のデキスト
リン溶液を約200g得た。本デキストリン液は培養液
由来の不快臭もなく無色透明の液体である。
In addition, 1 ml of this liquid (containing 6.4 units of α-amylase) was added as a purified α-amylase solution to 200 g of 30% horse-cooled starch starch slurry at 100 ° C for 10 minutes, 70 ° C, Heated for 1 hour. As a result, the reaction solution showed a negative iodine starch reaction, and about 200 g of a dextrin solution having a DE of 12.4 was obtained. This dextrin solution is a colorless and transparent liquid without any unpleasant odor derived from the culture solution.

なお、上記の精製アミラーゼ溶液の保存性を試験した。
本液を2℃及び25℃に10日間及び6か月間保存し
て、その酵素活性を測定した。その結果、2℃保存では
6か月保存でも99%以上、25℃、6か月保存では9
9%以上の活性を保持していることを確認した。
The storability of the above purified amylase solution was tested.
This solution was stored at 2 ° C. and 25 ° C. for 10 days and 6 months, and its enzyme activity was measured. As a result, 99% or more was stored at 2 ° C for 6 months and 9% at 25 ° C for 6 months.
It was confirmed that the activity was maintained at 9% or more.

実施例3 実施例2で得られたデキストリン液100gにβ−アミ
ラーゼ(麦芽起源、常温性)の精製粉末500単位
(0.2g)を加えて溶解し、45℃で48時間保温
し、デキストリンを麦芽糖及び少量のマルトトリオース
及びグルコースの混合物に加水分解した。反応後の麦芽
糖濃度は93%に達した。本麦芽糖液は培養液由来の臭
いや色もなく透明な液体である。
Example 3 To 100 g of the dextrin solution obtained in Example 2, 500 units (0.2 g) of purified powder of β-amylase (malt origin, room temperature) was added and dissolved, and the mixture was kept at 45 ° C. for 48 hours to give dextrin. It was hydrolyzed to a mixture of maltose and a small amount of maltotriose and glucose. The maltose concentration after the reaction reached 93%. This maltose liquid is a transparent liquid without odor or color derived from the culture liquid.

本液を精製アミラーゼ溶液として、低温及び室温での保
存性を試験した。本液を2℃及び25℃に10日間及び
6か月間保存して、その酵素活性を測定した。その結
果、2℃及び25℃下で、6か月保存でも98%以上の
活性を保持していることを確認した。
Using this solution as a purified amylase solution, the storage stability at low temperature and room temperature was tested. This solution was stored at 2 ° C. and 25 ° C. for 10 days and 6 months, and its enzyme activity was measured. As a result, it was confirmed that 98% or more of the activity was retained even after 6 months storage at 2 ° C and 25 ° C.

また、本液1ml(α−アミラーゼ6.4単位含有)を精
製アミラーゼ溶液として、30%馬鈴しよ殿粉スラリー
200gの100℃、10分加熱処理したものに添加
し、70℃、1時間加熱した。その結果、反応液はヨー
ド殿粉反応が陰性を示し、DEが12.2のデキストリ
ン溶液を約200g得た。本デキストリン液は培養液由
来の不快臭もなく無色透明の液体である。
In addition, 1 ml of this liquid (containing 6.4 units of α-amylase) was added as a purified amylase solution to 200 g of 30% potato starch starch slurry at 100 ° C for 10 minutes, and 70 ° C for 1 hour. Heated. As a result, the reaction solution showed a negative iodine starch reaction, and about 200 g of a dextrin solution having a DE of 12.2 was obtained. This dextrin solution is a colorless and transparent liquid without any unpleasant odor derived from the culture solution.

実施例4 実施例1と同様に培養して、培養液の固形分当り8
9.0単位/gの比活性をもつ培養液を得た。
Example 4 Culture was carried out in the same manner as in Example 1 to obtain 8 per solid content of the culture solution.
A culture solution having a specific activity of 9.0 units / g was obtained.

次に実施例2と同様に処理して、清澄液、複合体スラリ
ー、及び洗浄廃液を得た。清澄液と洗浄廃液についてα
−アミラーゼ活性を測定した結果、殿粉に吸着しなかつ
たα−アミラーゼ活性は100単位以下であつた。したが
つて、供試培養液中のα−アミラーゼの95.8%をα
−アミラーゼ・殿粉複合体として回収したと推算した。
Then, the same treatment as in Example 2 was performed to obtain a clarified liquid, a composite slurry, and a cleaning waste liquid. Clearing liquid and washing waste liquid α
-As a result of measuring amylase activity, the amount of α-amylase activity not adsorbed on starch was 100 units or less. Therefore, 95.8% of α-amylase in the test culture solution was
-It was estimated that it was recovered as an amylase-starch complex.

上記のα−アミラーゼ・殿粉複合体のスラリー25gに
グルコアミラーゼ(アスペルギルス・ニガー起源、常温
性)の精製粉末50単位(0.05g)を加えて溶解し、5
5℃で48時間保温し、α−アミラーゼ・殿粉複合体の
殿粉を、複合体に含まれているα−アミラーゼと、添加
したグルコアミラーゼにより、同時に液化及び糖化し
た。その結果、反応液はヨード殿粉反応が陰性を示し、
糖組成においてグルコースが95%のα−アミラーゼ、
グルコアミラーゼ含有精製酵素溶液を得た。本酵素液は
ほぼ無色透明で、無臭であり、本液の容積当りのα−ア
ミラーゼ比活性は90単位/mlであり、容積当り18.
9倍に濃縮された。このときの回収した総活性は225
0単位であり、培養液中に含まれていたα−アミラーゼ
活性の97.8%が残存していることを把握した。更
に、糖及びグルコアミラーゼを除外した成分の乾物当り
の比活性は1.8×104単位/gとなり、本培養液
に対し183倍に精製されたことになる。
To 25 g of the above-mentioned α-amylase-starch complex slurry, 50 units (0.05 g) of purified powder of glucoamylase (originating from Aspergillus niger, room temperature) was added and dissolved, and 5
The mixture was incubated at 5 ° C. for 48 hours, and the starch of the α-amylase / starch complex was simultaneously liquefied and saccharified by the α-amylase contained in the complex and the added glucoamylase. As a result, the reaction solution showed a negative iodine starch reaction,
Α-amylase containing 95% glucose in the sugar composition,
A purified enzyme solution containing glucoamylase was obtained. This enzyme solution was almost colorless and transparent and had no odor, and the specific activity of α-amylase per volume of this solution was 90 units / ml, and was 18.
It was concentrated 9 times. Total activity recovered at this time is 225
It was 0 unit, and it was understood that 97.8% of the α-amylase activity contained in the culture solution remained. Furthermore, the specific activity of the components excluding sugar and glucoamylase per dry matter was 1.8 × 10 4 units / g, which means that it was purified 183 times as much as the main culture solution.

上記の精製酵素液1ml(α−アミラーゼ90単位含有)
を精製α−アミラーゼ溶液として、30%馬鈴しよ殿粉
スラリー200gの100℃、10分加熱処理したものに
添加し、70℃、1時間加熱した。その結果、反応液は
ヨード殿粉反応が陰性を示し、DEが12.6の糖溶液
を約200g得た。本糖液は培養液由来の不快臭もな
く、無色透明の液体である。
1 ml of the above purified enzyme solution (containing 90 units of α-amylase)
Was added as a purified α-amylase solution to 200 g of 30% potato starch powder slurry which had been heat-treated at 100 ° C for 10 minutes, and heated at 70 ° C for 1 hour. As a result, the reaction solution showed a negative iodine starch reaction, and about 200 g of a sugar solution having a DE of 12.6 was obtained. This sugar solution is a colorless and transparent liquid with no unpleasant odor derived from the culture solution.

なお、上記の精製アミラーゼ溶液の保存性を試験した。
本液を2℃及び25℃に6か月間保存して、その酵素活
性を測定した。その結果、2℃保存では6か月保存でも
98%以上、25℃では99%以上の活性を保持している
ことを確認した。
The storability of the above purified amylase solution was tested.
This solution was stored at 2 ° C. and 25 ° C. for 6 months, and its enzyme activity was measured. As a result, it was confirmed that 98% or more of the activity was retained at 6 ° C storage at 2 ° C and 99% or more at 25 ° C.

実施例5 実施例1と同様に培養して、5.1単位/mlのα−アミ
ラーゼ活性、及び培養液の固形分当り102単位/g
の比活性をもつ培養液を得た。
Example 5 Culture was carried out in the same manner as in Example 1 to obtain 5.1 units / ml of α-amylase activity, and 102 units / g of solid content of the culture solution.
A culture solution having a specific activity of was obtained.

次に実施例2と同様に処理した。清澄液と洗浄廃液につ
いてα−アミラーゼ活性を測定した結果、殿粉に吸着し
なかつたα−アミラーゼ活性は102単位以下であつた。
したがつて、供試培養液中のα−アミラーゼの96%を
α−アミラーゼ・殿粉複合体として回収したと推算し
た。
Then, the same treatment as in Example 2 was performed. As a result of measuring the α-amylase activity of the clarified liquid and the washing waste liquid, the α-amylase activity which was not adsorbed on the starch was 102 units or less.
Therefore, it was estimated that 96% of α-amylase in the test culture solution was recovered as α-amylase-starch complex.

上記のα−アミラーゼ・殿粉複合体のスラリー25gに
グルコアミラーゼ(アスペルギルス・ニガー起源、常温
性)の精製粉末50単位(0.05g)とブルラナーゼ
〔バシルス・セレウス(Bacillus cereus)起源〕の精製
粉末10単位(0.02g)を添加して溶解し、55℃48
時間保温し、α−アミラーゼ・殿粉複合体の殿粉を、複
合体に含まれるα−アミラーゼと添加したグルコアミラ
ーゼ及びブルラナーゼにより、同時に液化及び糖化し
た。その結果、反応液はヨード殿粉反応が陰性を示し、
糖組成においてグルコースが95%の、グルコアミラー
ゼ及びプルラワーゼを含有したα−アミラーゼ精製酵素
溶液を得た。本液はほぼ無色透明で、無臭であり、本液
の容積当りのα−アミラーゼ比活性は96単位/mlであ
り、容積当り18.8倍に濃縮された。このときの回収
した液の総活性は2401単位であり、培養液中に含ま
れていたα−アミラーゼ活性の98%が残存しているこ
とを把握した。
50 g (0.05 g) of purified powder of glucoamylase (originating from Aspergillus niger, room temperature) and purified powder of vullanase [origin from Bacillus cereus] in 25 g of slurry of the above α-amylase-starch complex. Add 10 units (0.02g) and dissolve, 55 ℃ 48
After keeping the temperature for a while, the starch of the α-amylase-starch complex was simultaneously liquefied and saccharified by the α-amylase contained in the complex and the added glucoamylase and bruranase. As a result, the reaction solution showed a negative iodine starch reaction,
An α-amylase purified enzyme solution containing glucoamylase and pulllawase having a sugar composition of 95% glucose was obtained. The solution was almost colorless and transparent and had no odor. The specific activity of α-amylase per volume of the solution was 96 units / ml, and the solution was concentrated 18.8 times per volume. The total activity of the recovered solution at this time was 2401 units, and it was understood that 98% of the α-amylase activity contained in the culture solution remained.

更に、糖及びグルコアミラーゼ、プルラナーゼを除外し
た成分の乾物当りの比活性は1.9×104単位/gとな
り、本培養液に対し186倍に精製されたことにな
る。
Furthermore, the specific activity per dry matter of the components excluding sugar, glucoamylase, and pullulanase was 1.9 × 10 4 units / g, which means that it was purified 186 times that of the main culture.

上記の精製α−アミラーゼ液1ml(α−アミラーゼ96
単位含有)を30%馬鈴しよ殿粉スラリー200gに添
加し、70℃、1時間加熱した。その結果、反応液はヨ
ード殿粉反応が陰性を示し、DEが12.6の糖液を約
200g得た。本液は培養液由来の不快臭もなく、無色
透明の液体である。
1 ml of the above purified α-amylase solution (α-amylase 96
(Containing unit) was added to 200 g of 30% potato starch powder slurry and heated at 70 ° C. for 1 hour. As a result, the reaction solution showed a negative iodine starch reaction, and about 200 g of a sugar solution having a DE of 12.6 was obtained. This liquid is a colorless and transparent liquid with no unpleasant odor derived from the culture liquid.

なお、上記の精製アミラーゼ溶液の保存性を試験した。
本液を2℃及び25℃に6か月間保存して、その酵素活
性を測定した。その結果、2℃保存では6か月保存でも
98%以上、25℃では99%以上の活性を保持している
ことを確認した。
The storability of the above purified amylase solution was tested.
This solution was stored at 2 ° C. and 25 ° C. for 6 months, and its enzyme activity was measured. As a result, it was confirmed that 98% or more of the activity was retained at 6 ° C storage at 2 ° C and 99% or more at 25 ° C.

実施例6 可溶性殿粉1.5%、ポリペプトン0.5%、酵母エキ
ス0.5%、りん酸第1カリウム0.7%、りん酸第2
ナトリウム0.35%、硫酸マグネシウム・7水和物
0.001%及び水道水を含む液体培地(pH 7.0)を内
容積500mlの坂口フラスコに100mlずつ15本に分注
し、120℃で15分間殺菌する。これに、同上培地で
好気的に培養したバシルス・ズブチリス(Bacillus sub
tilis)属に属するα−アミラーゼ生産菌の好気培養液
を10mlずつ分注し、37℃で15時間(120ストロ
ーク/分)で振とう培養した。この培養液を5000rpmで
15分間遠心分離して菌体を除去し、α−アミラーゼ活
性8.1単位/mlの培養液1.5を得た。本培養
液中には無機塩1.1%、α−アミラーゼ以外の有機物
として1.2%を含む。特に有機物中には酢酸、酪酸を
主成分とする揮発性脂肪酸を約0.05%含む。このた
め不快な酸臭を有する。本培養液の固形分当りの比活
性は352単位/gであつた。
Example 6 Soluble starch 1.5%, polypeptone 0.5%, yeast extract 0.5%, potassium phosphate first 0.7%, phosphate second
Liquid medium (pH 7.0) containing sodium 0.35%, magnesium sulfate heptahydrate 0.001% and tap water was dispensed into 15 Sakaguchi flasks with an internal volume of 500 ml, 100 ml each, at 120 ° C for 15 minutes. Sterilize. To this, Bacillus subtilis (Bacillus subtilis) aerobically cultured in the same medium.
An aerobic culture solution of an α-amylase-producing bacterium belonging to the genus Tilis) was dispensed in 10 ml aliquots and shake-cultured at 37 ° C for 15 hours (120 strokes / minute). This culture solution was centrifuged at 5000 rpm for 15 minutes to remove the cells, and a culture solution 1.5 having an α-amylase activity of 8.1 units / ml was obtained. The main culture liquid contains 1.1% of inorganic salts and 1.2% as organic substances other than α-amylase. Particularly, the organic matter contains about 0.05% of volatile fatty acids containing acetic acid and butyric acid as main components. Therefore, it has an unpleasant acid odor. The specific activity per solid content of the main culture was 352 units / g.

次に、本培養液0.5を5℃に冷却し、これに馬鈴
しよ殿粉10gを添加し、かくはん下で1分間保持し
た。上記の液を遠心分離(3000rpm、5分間)し
て、α−アミラーゼ・殿粉複合体のスラリー25gと清
澄板0.5を得た。上記スラリー25gに蒸留水10
0ml(5℃、pH6.2)を添加し、混合した後、遠心分離
(3000rpm、5分間)して、洗浄したα−アミラー
ゼ・殿粉複合体スラリー25gを洗浄廃液100mlを得
た。上記清澄液と洗浄廃液について、α−アミラーゼ活
性を測定した結果、殿粉に吸着しなかつたα−アミラー
ゼ活性は、全培養液1.5に換算して250単位以
下であることから、供試培養液中のα−アミラーゼの
98%を、α−アミラーゼ・殿粉複合体として回収した
ことになる。
Next, 0.5 of the main culture broth was cooled to 5 ° C., 10 g of potato starch was added thereto, and the mixture was kept under stirring for 1 minute. The above liquid was centrifuged (3,000 rpm, 5 minutes) to obtain 25 g of a slurry of α-amylase / starch complex and a clarification plate 0.5. Distilled water 10 to 25 g of the above slurry
After adding 0 ml (5 ° C., pH 6.2) and mixing, centrifugation (3000 rpm, 5 minutes) was performed to obtain 25 ml of the washed α-amylase-starch complex slurry, and 100 ml of a waste liquid for washing. As a result of measuring the α-amylase activity of the above-mentioned clarified liquid and washing waste liquid, the α-amylase activity which was not adsorbed on starch was 250 units or less in terms of the total culture liquid 1.5. This means that 98% of the α-amylase in the culture solution was recovered as the α-amylase-starch complex.

次いで、局方の馬鈴しよ殿粉100gと50℃の温水2
30mlとの混合物に上記のα−アミラーゼ・殿粉複合体
29g、及びグルコアミラーゼ粉末200単位(アスペ
ルギルス・ニガー起源、0.1g)を添加し、50℃で
48時間反応させた。その後、グルコースイソメラーゼ
粉末300単位〔ストルペトミセス(Streptomyces)属
起源、0.2g〕を添加し、50℃で10時間反応させ
た。反応後の糖化率(液中全固形分に対する果糖とぶど
う糖の合計量の比を%で表示)は96%であつた。この
異性化糖液は、培養液由来の臭いも色もない透明液で、
無機塩濃度は0.01%以下である。なお、本液の容積
当りのα−アミラーゼの比活性は35.3単位/mlであ
り、容積当り4.4倍に濃縮されている。
Next, 100 g of potato shiyo starch of the pharmacopoeia and warm water at 50 ° C 2
To the mixture with 30 ml, 29 g of the above α-amylase / starch complex and 200 units of glucoamylase powder (originating from Aspergillus niger, 0.1 g) were added and reacted at 50 ° C. for 48 hours. Then, 300 units of glucose isomerase powder [Streptomyces genus origin, 0.2 g] was added, and the mixture was reacted at 50 ° C. for 10 hours. The saccharification rate after the reaction (the ratio of the total amount of fructose and glucose to the total solid content in the liquid is expressed in%) was 96%. This high-fructose corn syrup is a clear liquid with no odor or color derived from the culture solution
The inorganic salt concentration is 0.01% or less. The specific activity of α-amylase per volume of this solution was 35.3 units / ml, which was 4.4 times concentrated per volume.

更に、本液は糖、グルコアミラーゼ、グルコースイソメ
ラーゼ以外の成分の乾物基準のα−アミラーゼ比活性は
1.5×104単位/gであり、培養液に対し42.6
倍に精製されている。
Further, this solution has a dry matter-based α-amylase specific activity of components other than sugar, glucoamylase, and glucose isomerase of 1.5 × 10 4 units / g, which is 42.6 with respect to the culture solution.
It is twice as purified.

上記精製アミラーゼ溶液の保存性を試験した。本液を2
5℃に10日間保存して、その酵素活性を測定した。そ
の結果、85%以上の活性を保持していることを確認し
た。
The storability of the purified amylase solution was tested. 2 this solution
It was stored at 5 ° C for 10 days, and its enzyme activity was measured. As a result, it was confirmed that the activity was maintained at 85% or more.

比較例1 実施例1に対応する従来技術として次の実験を行つた。
すなわち、培養液中のα−アミラーゼを吸着させたα
−アミラーゼ・殿粉複合体をグルコアミラーゼで処理し
て複合体の殿粉粒子を糖化して高濃度糖含有精製アミラ
ーゼ液を得、それを殿粉の液化及び糖化に用いる実施例
1に対して、α−アミラーゼ・殿粉複合体をそのままα
−アミラーゼとして殿粉の液化及び糖化に用いた。
Comparative Example 1 The following experiment was conducted as a conventional technique corresponding to Example 1.
That is, α-amylase adsorbed in the culture solution
-The amylase / starch complex is treated with glucoamylase to saccharify the starch particles of the complex to obtain a purified amylase solution containing a high concentration of sugar, which is used for liquefaction and saccharification of starch as compared with Example 1. , Α-amylase-starch complex as α
Used as amylase for liquefaction and saccharification of starch.

実施例1と同じロツトの培養液及び殿粉を用い、同じ
手順でα−アミラーゼ・殿粉複合体のスラリー25gを
調製した。この複合体5g(α−アミラーゼ371単位
含有)を30%馬鈴しよ殿粉スラリーの100℃、10
分加熱処理したものに添加し、かくはん下で70℃に1
時間加熱した。その結果、反応液は未分解の殿粉粒子を
含む、DE9.5のデキストイン溶液1005gを得た。
本デキストリン液には、複合体の殿粉粒子起源の未分解
の殿粉粒子が残存するため、半透明を呈している。
Using the same lot culture solution and starch as in Example 1, 25 g of a slurry of α-amylase / starch complex was prepared by the same procedure. 5% of this complex (containing 371 units of α-amylase) was added to a 30% potato starch slurry at 100 ° C., 10 ° C.
Add to heat treated for 1 minute, and stir to 70 ° C under stirring.
Heated for hours. As a result, 1005 g of a DE9.5 dextoin solution containing undecomposed starch particles was obtained as the reaction liquid.
This dextrin solution is semi-transparent because undecomposed starch particles originating from the complex starch particles remain.

上記のデキストリン液100gにグルコアミラーゼ(ア
スペルギルス・ニガー起源、常温性)の精製粉末200
単位(0.1g)を加えて溶解し、50℃で48時間保
温して糖化反応を行つた。反応後のぶどう糖濃度は8
8.1%で、複合体起源の未分解殿粉粒子を含み半透明
を呈している。本糖液の糖組成を分析した結果、ぶどう
糖のほかにオリゴ糖が9.8%、オリゴ糖より高分子の
グリコースポリマーが2%含有されていることが判明し
た。
Purified powder 200 of glucoamylase (originating from Aspergillus niger, room temperature) in 100 g of the above dextrin solution
A unit (0.1 g) was added and dissolved, and the mixture was incubated at 50 ° C. for 48 hours for saccharification reaction. The glucose concentration after the reaction is 8
It is translucent at 8.1%, containing undegraded starch particles originating from the complex. As a result of analyzing the sugar composition of this sugar solution, it was found that, in addition to glucose, 9.8% oligosaccharide was contained, and 2% of a glycosyl polymer higher than oligosaccharide was contained.

〔発明の効果〕〔The invention's effect〕

以上説明したように、本発明方法により得られる精製α
−アミラーゼ含有液は、臭いや着色がなく、かつこれを
ぶどう糖や異性化糖製造に用いた場合には、吸着担体と
して用いた殿粉が未分解のまま残留、混入することな
く、糖化、異性化を行うことができるという顕著な効果
を奏するものである。
As described above, the purified α obtained by the method of the present invention
-The amylase-containing liquid has no odor or coloration, and when it is used for the production of glucose or isomerized sugar, the starch used as an adsorption carrier does not remain undecomposed and is not saccharified or isomerized. This is a remarkable effect that can be realized.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】粗α−アミラーゼ含有溶液を、氷点を越え
るが実質的に殿粉の液化反応が起らない温度で殿粉粒子
と接触させて、α−アミラーゼを殿粉粒子に吸着させる
工程、該α−アミラーゼを吸着した殿粉粒子を分離する
工程、及び該分離した殿粉粒子から得られるα−アミラ
ーゼ含有液を、グルコアミラーゼ及びβ−アミラーゼの
少なくとも一方を含有する酵素で処理してオリゴ糖以下
の分子量をもつ糖まで加水分解する工程、の各工程を包
含することを特徴とする精製α−アミラーゼ含有液の製
造方法。
1. A step of contacting a crude α-amylase-containing solution with starch particles at a temperature above the freezing point but substantially not causing a liquefaction reaction of starch to adsorb α-amylase to the starch particles. A step of separating the starch particles having adsorbed the α-amylase, and treating the α-amylase-containing liquid obtained from the separated starch particles with an enzyme containing at least one of glucoamylase and β-amylase. A method for producing a purified α-amylase-containing solution, comprising the steps of hydrolyzing a sugar having a molecular weight not higher than that of an oligosaccharide.
【請求項2】該分離した殿粉粒子を、実質的に殿粉の液
化反応が起らない温度の水で洗浄したのち、次の工程を
行う特許請求の範囲第1項記載の精製α−アミラーゼ含
有液の製造方法。
2. The purified α- according to claim 1, wherein the separated starch particles are washed with water at a temperature at which the liquefaction reaction of starch does not substantially occur, and then the following step is carried out. Method for producing amylase-containing liquid.
【請求項3】該粗α−アミラーゼ含有溶液が、α−アミ
ラーゼ生産菌の液体培養液から固形物を除去した液、又
は固体培養物若しくは培養菌体から抽出し固形物を除去
した抽出液である特許請求の範囲第1項又は第2項記載
の精製α−アミラーゼ含有液の製造方法。
3. The crude α-amylase-containing solution is a liquid obtained by removing solids from a liquid culture of α-amylase-producing bacteria, or an extract obtained by extracting from solid cultures or cultured cells to remove solids. A method for producing the purified α-amylase-containing solution according to claim 1 or 2.
JP62185460A 1987-07-27 1987-07-27 Method for producing purified α-amylase-containing liquid Expired - Lifetime JPH0640823B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62185460A JPH0640823B2 (en) 1987-07-27 1987-07-27 Method for producing purified α-amylase-containing liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62185460A JPH0640823B2 (en) 1987-07-27 1987-07-27 Method for producing purified α-amylase-containing liquid

Publications (2)

Publication Number Publication Date
JPS6430583A JPS6430583A (en) 1989-02-01
JPH0640823B2 true JPH0640823B2 (en) 1994-06-01

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Country Link
JP (1) JPH0640823B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2615398B2 (en) * 1991-10-31 1997-05-28 農林水産省食品総合研究所長 Method for producing starch granules with modified properties

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