JPS62108898A - Purification of nicotinamide adenine dinuclelotide (nad) - Google Patents
Purification of nicotinamide adenine dinuclelotide (nad)Info
- Publication number
- JPS62108898A JPS62108898A JP24720085A JP24720085A JPS62108898A JP S62108898 A JPS62108898 A JP S62108898A JP 24720085 A JP24720085 A JP 24720085A JP 24720085 A JP24720085 A JP 24720085A JP S62108898 A JPS62108898 A JP S62108898A
- Authority
- JP
- Japan
- Prior art keywords
- nad
- adsorbed
- amino acids
- nicotinamide adenine
- divinylbenzene
- 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.)
- Pending
Links
Landscapes
- Saccharide Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
ニコチンアミド・アデニン・ジヌクレオチド(NAD)
は生体内におけるや化還元反応の補酵素として必須の化
合物であり、生体内のエネルギー代謝や生合成反応等に
重要な役J!lを果たしており生化学や臨床検査の分野
で広く使用されている。[Detailed description of the invention] (Industrial application field) Nicotinamide adenine dinucleotide (NAD)
J! is an essential compound as a coenzyme for the oxidation-reduction reaction in the body, and plays an important role in energy metabolism and biosynthesis reactions in the body. It is widely used in the fields of biochemistry and clinical testing.
更に近年ではNADやADPを再生使用する。いわゆる
補酵素再生系を含むバイオリアクターによるアミノ酸な
ど有用物質の生産が試みられ注目を集めている化合物で
ある。Furthermore, in recent years, NAD and ADP are being reused. It is a compound that is attracting attention because attempts have been made to produce useful substances such as amino acids using a bioreactor that includes a so-called coenzyme regeneration system.
(従来の技術)
NADは、微生物体内に微量存在し、工業的には酵母か
らの抽出法や、バクテリアの醗酵法によって製造されて
いるが、NADの精製法としては従来より、活性炭によ
る吸着法や金属イオンによる沈澱法、更にはイオン交換
樹脂を単独もしくは。(Prior art) NAD exists in small amounts in microorganisms, and is industrially produced by extraction from yeast or bacterial fermentation. Conventionally, NAD has been purified by adsorption using activated carbon. or precipitation method using metal ions, or using ion exchange resin alone or using ion exchange resin.
組み合わせ使用する方法1例えば強塩基性陰イオン交換
樹脂による方法(H,Ijichi et、 aL、
J、 BioLChem、 VoL 241.8701
(19(5iり ) 、W<酸性陽イオン交侯樹脂に
よる方法(特開μ(443−24188)強塩基性陰イ
オン交換樹脂と強酸性陽イオン交換樹脂との組み合わせ
による方法(特開昭44−27898)、が一般的に使
用さ汎てきた。又9本発明者等によって見出されたイオ
ン交換樹脂を組み合わせて高度に精製した後NADJ離
塩の結晶として得る方法もある。(特開昭57−675
9(発明が解決しようとする問題点)
酵母か4らの抽出法や、バクテリアの醗酵法によって製
造さ扛たNAD含有液中にはヌクレオチド類やアミノ酸
類、更には無機塩類が多量に含有さ扛るために活性炭吸
着法では、他のヌクレオチド類やアミノ酸類も同時に吸
着され単独でヌクレオチド類などから高純度のNAD−
i分離精製することは困難であり、また、NADを抽出
するためには高濃変のアンモニアと多量の有機溶媒を必
要とする。従来より一般的に用いられてきたイオン交換
樹脂法の場合には共存する無機塩やヌクレオチド類の影
響により大量の樹脂や多種類の樹脂が必要であるので多
くの溶離剤とその再生に多量の酸とアルカリを要するし
、更に不利なことばは、溶離液が希薄なものとなりその
濃縮に多くのエネルギーが費やされてしまう欠点を有し
ている。Combination method 1 For example, a method using a strongly basic anion exchange resin (H, Ijichi et, aL,
J, BioLChem, VoL 241.8701
(19(5i Ri), W -27898) has been widely used. There is also a method of combining ion exchange resins discovered by the present inventors and highly purifying the product and obtaining crystals of NADJ salt release (Unexamined Japanese Patent Publication No. Showa 57-675
9 (Problems to be solved by the invention) NAD-containing liquids produced by yeast extraction or bacterial fermentation contain large amounts of nucleotides, amino acids, and even inorganic salts. In the activated carbon adsorption method, other nucleotides and amino acids are also adsorbed at the same time, and highly pure NAD-
It is difficult to separate and purify NAD, and highly concentrated ammonia and a large amount of organic solvent are required to extract NAD. In the case of the ion exchange resin method that has been commonly used in the past, a large amount of resin and many types of resin are required due to the influence of coexisting inorganic salts and nucleotides. It requires acids and alkalis, and a further disadvantage is that the eluent is dilute and much energy is expended in concentrating it.
(問題全解決するための手段)
酵母からの抽出法や、バクテリアの醗酵法によって製造
さfifcNADの他に無機塩類やアミノ酸類やヌクレ
オチド類が多量に共存するNAD含有液から、NADの
みを選択的、かつ収率良く分離できる方法を鋭意検討し
た結果、スチレンとジビニルベンゼンとの共重合体、も
しくは一部ハロゲン化されているスチレンとジビニルベ
ンゼンとの共重合体よりなる多孔性でかつ非イオン性の
吸着樹脂がNADのみを吸着し、NAD含有液に多量に
共存する無機塩類、アミノ酸類やヌクレオチド類は吸着
せず、水又は希薄な塩で洗うことによって除去できるこ
と、続いて水や希アルカリもしくはそnらを含有する希
アルコール類凍たは希アセトン類によってNADを醇出
することにより極めて高純度のNADがしかも定量的に
得ら扛ることを見出し発明を完成するに至った。(Means for solving all problems) Selectively extract only NAD from an NAD-containing solution that is produced by yeast extraction method or bacterial fermentation method and contains large amounts of fifcNAD, inorganic salts, amino acids, and nucleotides. As a result of intensive research into methods that could separate the styrene and divinylbenzene with high yield, we found a porous and nonionic material made of a copolymer of styrene and divinylbenzene, or a partially halogenated copolymer of styrene and divinylbenzene. The adsorption resin adsorbs only NAD, and does not adsorb inorganic salts, amino acids, or nucleotides that coexist in large amounts in NAD-containing liquids, and can be removed by washing with water or diluted salts. The inventors discovered that NAD of extremely high purity could be obtained quantitatively by distilling NAD with dilute alcohols or dilute acetones containing these substances, and completed the invention.
次に1本発明について詳細に説明する。Next, one aspect of the present invention will be explained in detail.
本発明に使用されるNAD含有液は酵母などの微生物か
らの抽出液やバクテリアによるサルベージ合成により得
られた反応液またはそ几らの部分精製液等生化学反応に
より得られるNADを含有する液であればいずれにも用
いらnる。The NAD-containing liquid used in the present invention is a liquid containing NAD obtained by a biochemical reaction, such as an extract from microorganisms such as yeast, a reaction liquid obtained by salvage synthesis using bacteria, or a partially purified liquid thereof. If available, it can be used in either case.
本発明にN 71)スチレンとジビニルベンゼンを主成
分とする共重合体で、多孔性かつ非イオン性の吸着樹脂
とは2例えば、市販のアンバーライトXAD−2,XA
D−4(ローム・アンド・ハース社製)、ダイヤイオン
HP−20,HP−30(三菱化成工業(株)等)、
デーオライドS −861(ダイヤモンド・シャムロツ
タ社製)カアリ、ステンンとジビニルベンゼン金主成分
トスる共重合体でその一部がハロゲン化されており、多
孔性かつ非イオン性の吸着樹脂とは2例えば、セパピー
ズ 5P=206,5P−207(三菱化成工業(株)
Iり 、 デーオライド ES−8610(ダイヤモ
ンド・シャムロツタ社製)があげられる。NAD含有液
を丙7.0以下に調整したのち。71) What is the porous and nonionic adsorption resin that is a copolymer mainly composed of styrene and divinylbenzene?2For example, commercially available Amberlite XAD-2, XA
D-4 (manufactured by Rohm and Haas), Diaion HP-20, HP-30 (Mitsubishi Chemical Industries, Ltd., etc.),
Deolide S-861 (manufactured by Diamond Shamrotsuta Co., Ltd.) is a copolymer of Kaari, Sten and divinylbenzene with a gold main component, a part of which is halogenated, and is a porous and nonionic adsorption resin.For example, Seppapies 5P=206, 5P-207 (Mitsubishi Chemical Industries, Ltd.)
An example of this is Deolide ES-8610 (manufactured by Diamond Shamrotsuta Co., Ltd.). After adjusting the NAD-containing liquid to 7.0 or less.
5091メタノール等の有機溶剤により再生し、十分水
洗しておいたスチレンとジビニルベンゼンより成る共重
合体、もしくは一部ハロゲン化されているスチレンとジ
ビニルベンゼンとの共重合体よりなる多孔性でかつ非イ
オン性の吸着樹脂金詰めたカラムに通液すると無機塩類
やヌクレオチド類。5091 A porous and non-porous material made of a copolymer of styrene and divinylbenzene that has been regenerated with an organic solvent such as methanol and thoroughly washed with water, or a partially halogenated copolymer of styrene and divinylbenzene. When the liquid is passed through a column filled with ionic adsorption resin gold, inorganic salts and nucleotides are extracted.
更にはアミノ酸類は本樹脂に吸着されずに通過しNAD
は吸着される。付着したヌクレオチド類などを除去する
ために少量の水または希薄な基金カラムに流した後NA
Dを溶離する0浴離剤としては、水又は希アルカリ、更
にそれらを含有する希アルコール類や希アセトンが用い
ら扛る。N A Dより樹脂に対する親和性の強い着色
成分の混入を防止し、NAD画分の純度を高く保つため
には。Furthermore, amino acids pass through this resin without being adsorbed and become NAD.
is adsorbed. After passing through a small amount of water or dilute foundation column to remove attached nucleotides, etc., NA
Water or a dilute alkali, as well as dilute alcohols and dilute acetone containing them, are used as the zero bath release agent for eluting D. In order to prevent the contamination of coloring components that have a stronger affinity for resin than NAD and to maintain high purity of the NAD fraction.
希アルカリでは、pH10,5以下、希アルコール類や
希アセトンを混合する場合は、20係以下の濃度が最適
である。For dilute alkali, the optimum pH is 10.5 or less, and when mixing dilute alcohols or dilute acetone, the optimum concentration is 20 or less.
以上の方法により得たNAD溶液をそのままもしくは必
要な場合は更に精製を続けた後濃縮し結晶化することに
より高純度のNADを得ることができる。Highly purified NAD can be obtained by directly using the NAD solution obtained by the above method or by further purifying the solution if necessary and then concentrating and crystallizing it.
(実施例)
以下本発明の実施例を示すが、何等木発明を限定するも
のではない。(Example) Examples of the present invention will be shown below, but are not intended to limit the invention in any way.
尚1本実施例において高速潜体クロマトグラフィーによ
る純度(HPLC純度)の測定は次の条件で行った。In this example, the purity (HPLC purity) was measured by high performance dilute chromatography under the following conditions.
カラム:東洋曹達(株)製 TSK−GEL○DS−8
0TM
移動相:5%メタノールを含む0.05M燐酸−カリウ
ム水浴液
定 量: 260nmの吸光度により測定した。Column: TSK-GEL○DS-8 manufactured by Toyo Soda Co., Ltd.
0TM Mobile phase: 0.05M phosphate-potassium water bath solution containing 5% methanol Quantification: Measured by absorbance at 260 nm.
酵*法による純度(ADH純度)」す定は5次に示すア
ルコール脱水素法により測定した。Purity by fermentation method (ADH purity) was measured by the alcohol dehydrogenation method shown below.
M、 Kコingenberg、 Methods
of Enzymatic Analysis
: 2nd edition、 Vol、 4+ 20
49 (1974)実施例1
ブレビバクテリウム−ぐアンモニアゲネス[AM 1
641株の醗酵ろ液1,500d (NAD8.112
1含有、 p)(6,5) f、 セハヒース5P−2
07(三菱化成工業(株)製)500−に5V=2で吸
着せしめ、750−の水にて洗浄した。M, K Coingenberg, Methods
of Enzymatic Analysis
: 2nd edition, Vol, 4+20
49 (1974) Example 1 Brevibacterium ammoniagenes [AM 1
1,500 d of fermentation filtrate from 641 strains (NAD 8.112
1 containing, p) (6,5) f, Cehahis 5P-2
07 (manufactured by Mitsubishi Chemical Industries, Ltd.) 500- at 5V=2, and washed with 750-water.
次に、10%メタノール水2,000−にて溶離し。Next, it was eluted with 2,000 ml of 10% methanol water.
NAD画分1.000 d (NAD 7.947 f
を含む)を得た。得られたNAD画分を減圧濃縮後、4
℃で24時間冷却し結晶化した結果、6.785PのN
AD結晶(HPLCM度100%、ADH純度99.1
%)を取得した〇
実施例2
キャンディダ・ユティリス KJS−0582株(FB
RM−7396株)の培養菌体からの熱水抽出液1.0
00ml (NAD 662,4■を含有。NAD fraction 1.000 d (NAD 7.947 f
) obtained. After concentrating the obtained NAD fraction under reduced pressure,
As a result of cooling and crystallizing at ℃ for 24 hours, 6.785P of N
AD crystal (HPLCM degree 100%, ADH purity 99.1
%) Example 2 Candida utilis strain KJS-0582 (FB
RM-7396 strain) hot water extract from cultured bacterial cells 1.0
00ml (Contains NAD 662.4■.
pH1,0)を、アンバーライト XAD−4(ローム
・アンド・ハース社製)500ifc充填したカラムに
、5V=2.0で通液し、水500−で洗浄した。続い
て10%メタノール水で溶離しNAD画分750ml
(NAD 648.9”j’を含む)1−得た。(pH 1.0) was passed through a column filled with Amberlite XAD-4 (manufactured by Rohm and Haas) 500 ifc at 5 V = 2.0, and washed with water 500 ml. Subsequently, 750 ml of NAD fraction was eluted with 10% methanol water.
(containing NAD 648.9"j') 1-obtained.
て溶離り得られたNAD画分全減圧#縮し、4℃で24
時間冷却し結晶化した。その結果、結晶NAD5 5
0.OW CHPLCHFfl l 0 0%、
ADH縄度99,5%)を得た。The NAD fraction obtained by elution was concentrated under reduced pressure and incubated at 4°C for 24 hours.
It was cooled for an hour and crystallized. As a result, crystalline NAD5 5
0. OW CHPLCHFfl l 0 0%,
An ADH degree of 99.5% was obtained.
(発明の幼果)
本発明の方法により無機塩類やアミノ酸類やヌクレオチ
ド類を共存するNAD宮有液から簡単な工程で極めて高
純度のN A l’)を定量的に得らnるため、使用す
る薬剤、エネルギー及び時間が−としく節約できる。(Young Fruit of the Invention) In order to quantitatively obtain NAl') of extremely high purity in a simple process from an NAD solution coexisting with inorganic salts, amino acids, and nucleotides by the method of the present invention, Significant savings in drugs, energy and time are achieved.
Claims (2)
に無機塩類やアミノ酸類やヌクレオチド類の共存するニ
コチンアミド・アデニン・ジヌクレオチド含有液をスチ
レンとジビニルベンゼンとを主成分とする共重合体より
なる多孔性でかつ非イオン性の吸着樹脂に吸着せしめ、
中性ないしアルカリ性の、水または含水有機溶媒で溶離
することを特徴とするNAD(ニコチンアミド・アデニ
ン・ジヌクレオチド)の精製法。(1) A porous solution made of a copolymer mainly composed of styrene and divinylbenzene, containing a nicotinamide/adenine/dinucleotide-containing liquid containing inorganic salts, amino acids, and nucleotides in addition to nicotinamide/adenine/dinucleotide. adsorbed on a neutral and nonionic adsorption resin,
A method for purifying NAD (nicotinamide adenine dinucleotide), which is characterized by elution with neutral to alkaline water or a water-containing organic solvent.
重合体が一部ハロゲン化されていることを特徴とする特
許請求範囲第1項に記載のNADの精製法。(2) The method for purifying NAD according to claim 1, wherein the copolymer mainly composed of styrene and divinylbenzene is partially halogenated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24720085A JPS62108898A (en) | 1985-11-06 | 1985-11-06 | Purification of nicotinamide adenine dinuclelotide (nad) |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24720085A JPS62108898A (en) | 1985-11-06 | 1985-11-06 | Purification of nicotinamide adenine dinuclelotide (nad) |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62108898A true JPS62108898A (en) | 1987-05-20 |
Family
ID=17159937
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24720085A Pending JPS62108898A (en) | 1985-11-06 | 1985-11-06 | Purification of nicotinamide adenine dinuclelotide (nad) |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62108898A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105481923A (en) * | 2015-12-30 | 2016-04-13 | 平光制药股份有限公司 | Preparation method of nicotinamide adenine dinucleotide |
CN108484707A (en) * | 2018-04-10 | 2018-09-04 | 开封康诺药业有限公司 | The technique of trifluoroacetic acid in a kind of removal Coenzyme I |
CN109836469A (en) * | 2019-02-27 | 2019-06-04 | 开封康诺药业有限公司 | A kind of decoloration process of Coenzyme I |
-
1985
- 1985-11-06 JP JP24720085A patent/JPS62108898A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105481923A (en) * | 2015-12-30 | 2016-04-13 | 平光制药股份有限公司 | Preparation method of nicotinamide adenine dinucleotide |
CN108484707A (en) * | 2018-04-10 | 2018-09-04 | 开封康诺药业有限公司 | The technique of trifluoroacetic acid in a kind of removal Coenzyme I |
CN109836469A (en) * | 2019-02-27 | 2019-06-04 | 开封康诺药业有限公司 | A kind of decoloration process of Coenzyme I |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US8088949B2 (en) | Process for purifying L-cysteine | |
JPS58190394A (en) | Production of d-glucose | |
US20190336887A1 (en) | Process for purifying nadph | |
JPS62108898A (en) | Purification of nicotinamide adenine dinuclelotide (nad) | |
US5811271A (en) | Process for producing L-ketohexose | |
JP2001258583A (en) | Method for purifying shikimic acid | |
KR890003597B1 (en) | Method for separating glycine and l-serine from a solution containing same | |
US5180670A (en) | Method for purification of mitomycin C | |
US3810823A (en) | Method for isolation of enzymes | |
JPS62246575A (en) | Method for purifying pyrroloquinolinequinone | |
JP3711296B2 (en) | Method for producing L-psicose | |
US5256788A (en) | Moranoline derivatives and their production and the use of moranoline and its derivatives as a stabilizing agent for enzymes | |
JPH05308984A (en) | Production of l-tagatose | |
JPS62249956A (en) | Purification of carnitine | |
JPS6120268B2 (en) | ||
JP4011496B2 (en) | Method for producing L-glucose | |
EP0533115A1 (en) | Process for production of hydroxocobalamin | |
JP2001292792A (en) | Method for recovering n-acetylglucosamine | |
JPS604168A (en) | Crystallization of tryptophan | |
JP4480100B2 (en) | Method for producing L-ascorbic acid-2-phosphate | |
JPH06345683A (en) | Purification of pyruvic acid | |
JPS63267287A (en) | Method for purifying pyrroloquinolinequinone | |
JPS61128895A (en) | Production of useful substance using coenzyme recovery reaction | |
JPH0383992A (en) | Production of high purity aldosylfructoside | |
JPS58155096A (en) | Preparation of d-alpha-amino-epsilon-caprolactam |