JPH0449399B2 - - Google Patents

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Publication number
JPH0449399B2
JPH0449399B2 JP4619684A JP4619684A JPH0449399B2 JP H0449399 B2 JPH0449399 B2 JP H0449399B2 JP 4619684 A JP4619684 A JP 4619684A JP 4619684 A JP4619684 A JP 4619684A JP H0449399 B2 JPH0449399 B2 JP H0449399B2
Authority
JP
Japan
Prior art keywords
nad
nadh
reaction
hydrogen
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
JP4619684A
Other languages
Japanese (ja)
Other versions
JPS60188091A (en
Inventor
Tadashi Matsunaga
Naoki Matsunaga
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.)
Unitika Ltd
Original Assignee
Unitika Ltd
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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP4619684A priority Critical patent/JPS60188091A/en
Publication of JPS60188091A publication Critical patent/JPS60188091A/en
Publication of JPH0449399B2 publication Critical patent/JPH0449399B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は、ニコチンアミドアデニンジヌクレオ
チド(以下NADと略記する。)の還元法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for reducing nicotinamide adenine dinucleotide (hereinafter abbreviated as NAD).

近年、酵素反応を各種の物質の合成に利用する
と、通常の化学的手段では合成困難な物質が容易
に得られる場合のあることがわかつている。した
がつて、酵素反応の利用は化学的手段による合成
の壁を打ち破るものとしてその将来に大きい期待
がもたれている。
In recent years, it has been found that when enzyme reactions are used to synthesize various substances, substances that are difficult to synthesize using normal chemical means can sometimes be easily obtained. Therefore, there are great expectations for the future of the use of enzymatic reactions as a means of breaking down the barriers of synthesis by chemical means.

酵素反応には種々の型の反応があるが、その一
つに酸化還元反応がある。酸化還元反応を酵素的
に行う場合、その多くは補酵素としてNADある
いはNADH(ニコチンアミドアデニンジヌクレオ
チド還元型)を必要とする。しかし、NADや
NADHは極めて高価な物質であるので、これを
使い捨て的に使用することを実用的でなく、酸化
還元反応を酵素的に行う場合の最大の問題点にな
つていた。
There are various types of enzymatic reactions, one of which is redox reaction. When redox reactions are carried out enzymatically, most of them require NAD or NADH (reduced nicotinamide adenine dinucleotide) as a coenzyme. However, NAD and
Since NADH is an extremely expensive substance, it is impractical to use it disposablely, and this has become the biggest problem when performing enzymatic redox reactions.

NAD、NADHを補酵素として使用すると
NADはNADHに、NADHはNADに消費され
る。したがつて、NADをNADHから、NADH
をNADから再生することが可能になれば上に述
べた問題点は回避できることになる。
Using NAD and NADH as coenzymes
NAD is consumed by NADH, and NADH is consumed by NAD. Therefore, NAD from NADH, NADH
If it becomes possible to reproduce the data from the NAD, the above-mentioned problems can be avoided.

このような観点から、NADやNADHの再生に
ついて研究が行われており、電気化学的な方法
や、酵素的な方法が提案されている。しかし、電
気化学的な方法ではNADやNADH以外の化合物
への変換反応も併発するので好ましくない。酵素
的な方法は各種デヒドロゲナーゼを使用するもの
であるが、この場合、別に副原料(基質)を必要
とするので、副原料の未反応物、副原料からの生
成物、などから目的物のNADやNADHを分離、
精製するという面倒な工程を必要とするので、こ
れも好ましいものではなかつた。
From this perspective, research is being conducted on the regeneration of NAD and NADH, and electrochemical methods and enzymatic methods have been proposed. However, electrochemical methods are not preferable because conversion reactions to compounds other than NAD and NADH also occur. Enzymatic methods use various dehydrogenases, but in this case, additional auxiliary raw materials (substrates) are required. and NADH,
This was also not desirable because it required a troublesome process of purification.

本発明者らは、特にNADHの再生について、
上述の観点から、工業的に利用可能な方法につい
て鋭意研究を重ねた結果、高圧の水素の存在下で
特定の微生物をNADに作用させると、従来の方
法にみられた問題点を克服したすぐれた方法とな
ることを見出し、本発明に到達した。
The present inventors particularly focused on the regeneration of NADH.
From the above point of view, as a result of intensive research on industrially available methods, we found that allowing specific microorganisms to act on NAD in the presence of high-pressure hydrogen is an excellent method that overcomes the problems seen in conventional methods. The present invention was achieved based on the discovery that a method is possible.

すなわち、本発明は、10気圧以上の水素圧下で
クロストリジウム属に属し、NADをNADHに還
元する能力を有する微生物をNADに作用させる
ことを特徴とするNADの還元法である。
That is, the present invention is a method for reducing NAD, which is characterized in that a microorganism belonging to the genus Clostridium and having the ability to reduce NAD to NADH is allowed to act on NAD under a hydrogen pressure of 10 atmospheres or more.

以下、本発明につき詳細に説明する。 Hereinafter, the present invention will be explained in detail.

本発明によりNADを還元するには、例えば
NADを含有した緩衝液にクロストリジウム属に
属し、NADをNADHに還元する能力を有する微
生物を懸濁させて、水素を導入し10気圧以上の水
素圧下で反応させればよい。このような簡単な操
作でNADが還元されNADHへ再生される。この
場合、副生成物は生成せず、介入してくるのは未
反応の水素だけであり、この水素も特に手段を講
ずる必要はなく自然に除去されるので、工業上極
めて有利である。通常、このような生物的反応は
常圧下で行うのが常識であるが、本反応は常圧下
ではほとんど進行せず、高圧下で初めて進行する
ものであつて、従来の常識をくつがえす驚くべき
ことであつた。
To reduce NAD according to the present invention, for example,
Microorganisms belonging to the genus Clostridium and having the ability to reduce NAD to NADH may be suspended in a buffer containing NAD, and hydrogen may be introduced to cause a reaction under a hydrogen pressure of 10 atmospheres or more. With such a simple operation, NAD is reduced and regenerated into NADH. In this case, no by-products are produced, and only unreacted hydrogen intervenes, and this hydrogen is also removed naturally without the need for special measures, which is extremely advantageous industrially. Normally, it is common knowledge that biological reactions like this are carried out under normal pressure, but this reaction hardly progresses under normal pressure and only progresses under high pressure, which is surprising and overturns conventional wisdom. It was hot.

本発明に使用する微生物はクロストリジウム属
に属する微生物であり、例えばクロストリジウ
ム・ブチリカム、クロストリジウム・アセトブチ
リカム、クロストリジウム・ペリフリンジエンス
などがあげられ、これらは培養菌体のまま使用し
てもよいしまた適当な担体に固定化して使用して
もよい。本発明を手軽に実施するには培養菌体の
ままでもよいが、担体に固定化して使用した方が
再生変換率が高く、また長時間の運転に耐えると
いつた利点がある。固定化を行うに当たつては公
知の方法が支障なく利用される。担体としては、
例えば寒天、アルギン酸、ゼラチン、カラギーナ
ンといつた天然物、ポリアクリルアミドゲルのよ
うな合成物などが好ましく使用される。
The microorganisms used in the present invention belong to the genus Clostridium, and examples include Clostridium butylicum, Clostridium acetobutylicum, and Clostridium perifringiens. It may be used after being immobilized on a carrier. In order to carry out the present invention easily, the cultured cells may be used as they are, but using them after immobilization on a carrier has the advantage of having a higher regeneration conversion rate and being able to withstand long-term operation. For immobilization, known methods can be used without any problem. As a carrier,
For example, natural products such as agar, alginic acid, gelatin, and carrageenan, and synthetic products such as polyacrylamide gel are preferably used.

本発明は、高い水素圧下で行うことが必要であ
り、10気圧以上、特に30気圧以上、50気圧以上、
80気圧以上、さらには100気圧以上が好ましい。
The present invention needs to be carried out under high hydrogen pressure, 10 atmospheres or more, especially 30 atmospheres or more, 50 atmospheres or more,
The pressure is preferably 80 atm or higher, more preferably 100 atm or higher.

使用する緩衝液には特に制限はなく、一般によ
く使われているトリス緩衝液、リン酸緩衝液、ク
エン酸緩衝液、トリシン緩衝液などを利用すれば
よい。PHは6〜9、好ましくは7〜8の範囲で設
定すればよい。菌体量は多ければ反応が速く、少
なければ反応が遅くなるだけてあつて、特定の範
囲内でないと本発明が実施できないというもので
はない。NAD濃度も特定の範囲内である必要は
なく、反応系に投入しただけで還元することが可
能である。反応温度は20℃ないし50℃、好ましく
は30℃ないし40℃が適用される。反応時間は、条
件により異なるが、おおむね1時間ないし10時間
程度でよい。
There are no particular limitations on the buffer used, and commonly used Tris buffer, phosphate buffer, citrate buffer, tricine buffer, etc. may be used. PH may be set in the range of 6 to 9, preferably 7 to 8. The larger the amount of bacterial cells, the faster the reaction, and the smaller the amount, the slower the reaction; however, this does not mean that the present invention cannot be carried out unless the amount is within a specific range. The NAD concentration does not need to be within a specific range, and reduction can be achieved simply by adding it to the reaction system. The reaction temperature is 20°C to 50°C, preferably 30°C to 40°C. The reaction time varies depending on the conditions, but may be approximately 1 to 10 hours.

以上のように、本発明の方法によれば、補酵素
として重要なNADHをNADより極めて容易に短
時間で製造し、再生することが可能である。
As described above, according to the method of the present invention, NADH, which is important as a coenzyme, can be produced and regenerated much more easily than NAD in a shorter time.

次に本発明を実施例により具体的に説明する。 Next, the present invention will be specifically explained using examples.

実施例 1 水素産生微生物クロストリジウム・ブチリカム
IFO3858を、グルコース1g、ペプトン0.4g、
酵母エキス0.4g、肉エキス0.2g、リン酸二カリ
ウム12.5g及び硫酸第一鉄0.05gを含有する培地
(PH7.0)100mlを使用して、嫌気条件下で37℃、
9時間培養した。
Example 1 Hydrogen-producing microorganism Clostridium butyricum
IFO3858, glucose 1g, peptone 0.4g,
Using 100 ml of a medium (PH7.0) containing 0.4 g of yeast extract, 0.2 g of meat extract, 12.5 g of dipotassium phosphate and 0.05 g of ferrous sulfate, at 37°C under anaerobic conditions.
It was cultured for 9 hours.

このようにして得られた菌体6mgを2mlの
0.1Mリン酸緩衝液(PH7.8)に懸濁したものを0.8
mMのNADを含有する0.1Mリン酸緩衝液(PH
7.8)8mlに加え、水素圧100気圧のオートクレー
ブ中で37℃、5時間反応させた。340nmの吸光
度からNADHの生成量を測定したところ、63%
の変換率でNADからNADHの得られることが認
められた。
6 mg of the bacterial cells obtained in this way was added to 2 ml of
0.8 suspended in 0.1M phosphate buffer (PH7.8)
0.1M phosphate buffer (PH
7.8) and reacted in an autoclave with a hydrogen pressure of 100 atm at 37°C for 5 hours. When the amount of NADH produced was measured from the absorbance at 340 nm, it was 63%.
It was observed that NADH could be obtained from NAD with a conversion rate of .

なお、生成したNADHの量はアルコールデヒ
ドロゲナーゼに対する活性測定値と一致すること
も確認した。
It was also confirmed that the amount of NADH produced was consistent with the measured value of activity against alcohol dehydrogenase.

また、比較のため、同条件下で水素圧1気圧
(常圧)下で行うと、NADHはほとんど生成しな
かつた。
For comparison, when the same conditions were used under a hydrogen pressure of 1 atm (normal pressure), almost no NADH was produced.

実施例 2 実施例1で得たクロストリジウム・ブチリカム
の菌体6mgを1mlの0.1Mリン酸緩衝液(PH7.8)
に懸濁させた。この懸濁液を1mlの4%寒天溶液
(上と同じリン酸緩衝液使用)と急速に混合、冷
却(0℃)し、固定化菌体を得た。
Example 2 6 mg of Clostridium butylicum cells obtained in Example 1 was added to 1 ml of 0.1M phosphate buffer (PH7.8)
suspended in. This suspension was rapidly mixed with 1 ml of 4% agar solution (using the same phosphate buffer as above) and cooled (0°C) to obtain immobilized bacterial cells.

このようにして得た固定化菌体を小片(約5
mm3)に細断し、生理食塩水で洗浄したのち、実施
例1と同様にしてNADを含有するリン酸緩衝液
に加えて、反応を行つた。変換率ほぼ100%で
NADHが得られた。
The immobilized bacterial cells obtained in this way were divided into small pieces (approximately 5
mm 3 ), washed with physiological saline, and added to a phosphate buffer containing NAD in the same manner as in Example 1 to carry out a reaction. Conversion rate is almost 100%
NADH was obtained.

上記反応終了後、同じ固定化菌体を再使用して
NADの還元版応を行つた。同条件下で5時間反
応を行つたところ、変換率がほぼ100%でNADH
が得られた。すなわち、NAD→NADHの変換を
連続的に運転できることがわかつた。
After the above reaction is completed, reuse the same immobilized bacterial cells.
A reduced version of NAD was performed. When the reaction was carried out under the same conditions for 5 hours, the conversion rate was almost 100% and NADH
was gotten. In other words, it was found that the conversion from NAD to NADH can be operated continuously.

実施例 3 実施例1の培養条件に従つて水素産生微生物ク
ロストリジウム・アセトブチリカムIAM19011の
菌体を得た。この菌体を実施例2と同様にして固
定化し、同条件下でNADの還元を行つたところ、
76%の変換率でNADHが得られた。
Example 3 Cells of the hydrogen-producing microorganism Clostridium acetobutylicum IAM19011 were obtained according to the culture conditions of Example 1. This bacterial cell was immobilized in the same manner as in Example 2, and NAD was reduced under the same conditions.
NADH was obtained with a conversion rate of 76%.

また、同様にして水素産生微生物クロストリジ
ウム・アセトブチリカルIAM19012及び
IAM19013も行つたところ、上記と同様な結果が
得られた。
Similarly, hydrogen-producing microorganisms Clostridium acetobutyrical IAM19012 and
When IAM19013 was also used, the same results as above were obtained.

Claims (1)

【特許請求の範囲】[Claims] 1 10気圧以上の水素圧下で、クロストリジウム
属に属し、ニコチンアミドアデニンジヌクレオチ
ドをニコチンアミドアデニンジヌクレオチド還元
型に還元する能力を有する微生物をニコチンアミ
ドアデニンジヌクレオチドに作用させることを特
徴とするニコチンアミドアデニンジヌクレオチド
の還元法。
1. Nicotinamide, characterized in that a microorganism belonging to the genus Clostridium and having the ability to reduce nicotinamide adenine dinucleotide to the reduced form of nicotinamide adenine dinucleotide is made to act on nicotinamide adenine dinucleotide under a hydrogen pressure of 10 atmospheres or more. Reduction method of adenine dinucleotide.
JP4619684A 1984-03-09 1984-03-09 Method for reducing nicotinamide adenine dinucleotide Granted JPS60188091A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4619684A JPS60188091A (en) 1984-03-09 1984-03-09 Method for reducing nicotinamide adenine dinucleotide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4619684A JPS60188091A (en) 1984-03-09 1984-03-09 Method for reducing nicotinamide adenine dinucleotide

Publications (2)

Publication Number Publication Date
JPS60188091A JPS60188091A (en) 1985-09-25
JPH0449399B2 true JPH0449399B2 (en) 1992-08-11

Family

ID=12740314

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4619684A Granted JPS60188091A (en) 1984-03-09 1984-03-09 Method for reducing nicotinamide adenine dinucleotide

Country Status (1)

Country Link
JP (1) JPS60188091A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5826226B2 (en) * 2013-08-23 2015-12-02 内山 俊一 Hydrogen activated catalyst

Also Published As

Publication number Publication date
JPS60188091A (en) 1985-09-25

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