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JPH06197778A - Production of phosphoenolpyruvic acid - Google Patents

Production of phosphoenolpyruvic acid

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Publication number
JPH06197778A
JPH06197778A JP34963392A JP34963392A JPH06197778A JP H06197778 A JPH06197778 A JP H06197778A JP 34963392 A JP34963392 A JP 34963392A JP 34963392 A JP34963392 A JP 34963392A JP H06197778 A JPH06197778 A JP H06197778A
Authority
JP
Japan
Prior art keywords
yeast
acid
phosphoenolpyruvic acid
torulopsis
carbon source
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.)
Granted
Application number
JP34963392A
Other languages
Japanese (ja)
Other versions
JP3151982B2 (en
Inventor
Reiko Miyata
令子 宮田
Toru Yonehara
徹 米原
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP34963392A priority Critical patent/JP3151982B2/en
Publication of JPH06197778A publication Critical patent/JPH06197778A/en
Application granted granted Critical
Publication of JP3151982B2 publication Critical patent/JP3151982B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To easily separate and purify a phosphoenolpyruvic acid under mild condition by forming the phosphoenolpyruvic acid from a carbon source using cultured product of yeast of the genus Saccharomyces, Hansenula, Pichia, Candida, Torulopsis, etc., and collecting the produced acid. CONSTITUTION:A yeast the belongs to the genus Saccharomyces, Hansenula, Pichia, Candida or Torulopsis (e.g. Torulopsis glabrata IFO 0622) is inoculated to a medium and cultured at 30 deg.C for 24 hr under shaking. The cultured liquid is subjected to centrifugal separation to collect the yeast cells. The yeast is made to react with a carbon source assimilable by the yeast (e.g. glucose) at 30 deg.C for 30hr and the produced and accumulated phosphoenolpyruvic acid is separated from phosphoric acid with a reverse osmosis membrane, etc. The phosphoenolpyruvic acid is incorporated with an alkali metal hydroxide and concentrated and crystallized in the form of an alkali metal salt to obtain the objective phosphoenolpyruvic acid under mild condition without using complicate operations.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、酵母の生産する炭素源
資化酵素系を用いて炭素源よりホスホエノールピルビン
酸を生成蓄積せしめ採取する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for collecting and collecting phosphoenolpyruvate from a carbon source by using a carbon source assimilation enzyme system produced by yeast.

【0002】ホスホエノールピルビン酸(以下PEPと
略す)は高エネルギーリン酸化合物であり、アデノシン
三リン酸(ATP)の再生系には必須かつ重要な化合物
である。
Phosphoenolpyruvate (hereinafter abbreviated as PEP) is a high energy phosphate compound and is an essential and important compound in the regeneration system of adenosine triphosphate (ATP).

【0003】[0003]

【従来の技術】PEPの化学合成は古くから公知(Ch
em.Pev.,Vol.61,607(1961))
であり、生化学的手段によりPEPを生成させる方法と
しては、デバリオマイセス(Debaryomyce
s)属の乾燥菌体を用いる方法(J.Ferment.
Technol.,Vol.65,225(198
7))が知られている。
2. Description of the Related Art The chemical synthesis of PEP has long been known (Ch
em. Pev. , Vol. 61, 607 (1961))
As a method for producing PEP by biochemical means, Debaryomyces (Debaryomyces) is used.
s) Method using dried bacterial cells of the genus (J. Ferment.
Technol. , Vol. 65,225 (198
7)) is known.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、化学合
成は収率、収量が低く、また乾燥菌体による酵素法は、
乾燥菌体調整など、操作が煩雑であるという問題があっ
た。
However, the yield of chemical synthesis is low and the yield is low, and the enzymatic method using dried cells is
There is a problem that the operation is complicated, such as adjustment of dried cells.

【0005】[0005]

【課題を解決するための手段】本発明者らは、収率、収
量が高くかつ操作が簡便なPEPの製造方法について鋭
意検討した結果、以下の本発明に到達した。
Means for Solving the Problems The inventors of the present invention have earnestly studied the yield and the method for producing PEP with high yield and simple operation, and as a result, have reached the following invention.

【0006】すなわち、本発明は、サッカロミセス(S
accharomyces)属、ハンゼヌラ(Hans
enula)属、ピキア(Pichia)属、キャンデ
ィダ(Candida)属またはトルロプシス(Tor
ulopsis)属に属する酵母の培養物を用いて、前
記酵母の資化し得る炭素源よりホスホエノールピルビン
酸を生成蓄積せしめ、これを単離採取することを特徴と
するホスホエノールピルビン酸の製造方法である。
That is, the present invention relates to Saccharomyces (S
genus accharomyces, Hansenula (Hans)
genus enula, Pichia genus, Candida genus or Torrlopsis (Tor)
A method for producing phosphoenolpyruvate characterized in that a phosphoenolpyruvate is produced and accumulated from a carbon source which can be assimilated by the yeast, using a culture of a yeast belonging to the genus is there.

【0007】本発明において使用され得る酵母として
は、サッカロミセス属、ハンゼヌラ属、ピキア属、トル
ロプシス属、キャンディダ属に属する酵母であれば、い
かなるものも使用できる。このうち、各種炭素源資化能
力の高いものが好ましく使用できる。好ましい酵母の具
体例としては、たとえば、サッカロミセス・セレビシェ
Saccharomyces cerevisie(I
FO 0213、0538、1950)、サッカロミセ
ス・クルイベリ Saccharomyceskluy
veri(IFO 1982)、ハンゼヌラ・グルコザ
イマ Hansenula glucozyma(IF
O 1472)、ピキア・パストリスPichia p
astoris(IFO 0948)、キャンディダ・
メタノリカ Candida methanolica
(ATCC 26175)、キャンディダ・リポリティ
カ Candida lipolytica(IFO0
717)、トルロプシス・ピナス Torulopsi
s pinus(IFO 0741)、トルロプシス・
グラブラータ Torulopsis glabrat
a(IFO 0622)などが挙げられる。
Any yeast can be used in the present invention as long as it is a yeast belonging to the genera Saccharomyces, Hansenula, Pichia, Torlopsis and Candida. Among these, those having high ability to utilize various carbon sources can be preferably used. Specific examples of preferred yeast include, for example, Saccharomyces cerevisiae (I
FO 0213, 0538, 1950), Saccharomyces kluy.
veri (IFO 1982), Hansenula glucozyma Hansenula glucozyma (IF
O 1472), Pichia pastoris Pichia p
astoris (IFO 0948), Candida
Methanolica candida methanolica
(ATCC 26175), Candida lipolytica Candida lipolytica (IFO0
717), Torulopsis pinas Torulopsi
s pinus (IFO 0741), Torrlopsis
Grabrata Torulopsis grabrat
a (IFO 0622) and the like.

【0008】本発明においては、酵母の培養物を用い
る。培養物は上記酵母を適当な栄養培地に培養すること
によって調整できる。これらの酵母を培養するための培
地としては、通常の天然あるいは合成培地が用いられる
が、好ましくはアミノ酸を適当に含んだ天然培地が良好
に用いられる。
In the present invention, a yeast culture is used. The culture can be prepared by culturing the above yeast in a suitable nutrient medium. As a medium for culturing these yeasts, an ordinary natural or synthetic medium is used, but a natural medium containing an appropriate amino acid is preferably used.

【0009】本発明で用いる酵母の培養物の形態は任意
であり、酵母の培養した培養物そのもの、培養された生
菌体、真空乾燥菌体、凍結乾燥菌体、有機溶媒による乾
燥菌体などの乾燥菌体、処理菌体などが本発明の範囲に
含まれる。このうち、工業的には酵母を栄養培地に培養
した培養物そのものが有利に用いられる。
The form of the yeast culture to be used in the present invention is arbitrary, and the yeast culture itself, cultured live cells, vacuum-dried cells, freeze-dried cells, dried cells by an organic solvent, etc. The dried bacterial cells, treated bacterial cells, etc. are included in the scope of the present invention. Of these, industrially, a culture itself obtained by culturing yeast in a nutrient medium is advantageously used.

【0010】ピルビン酸生成原料である炭素源として
は、本発明で使用する酵母が資化し得るものであればい
かなるものでもよい。好ましい炭素源の具体例として
は、グルコース、フラクトース、シュクロース、マンノ
ース、マンニトール、キシロース、ガラクトース、糖
蜜、ソルビトール、グリセリンなどの糖もしくは糖アル
コール、酢酸、クエン酸、乳酸などの有機酸、メタノー
ル、エタノール、プロパノールなどのアルコール類、そ
の他炭化水素などを挙げることができる。糖もしくは糖
アルコールを用いることにより、より好ましい結果を得
ることができる。
Any carbon source which is a raw material for producing pyruvic acid may be used as long as it can be assimilated by the yeast used in the present invention. Specific examples of preferred carbon sources include glucose, fructose, sucrose, mannose, mannitol, xylose, galactose, molasses, sorbitol, sugars or sugar alcohols such as glycerin, acetic acid, citric acid, organic acids such as lactic acid, methanol, ethanol. , Alcohols such as propanol, and hydrocarbons. By using sugar or sugar alcohol, more preferable results can be obtained.

【0011】本発明で使用する酵母の培養物の量は、乾
燥菌体濃度に換算して1〜50g/lが好ましく、より
好ましくは5〜20g/lの範囲である。
The amount of the yeast culture used in the present invention is preferably 1 to 50 g / l, more preferably 5 to 20 g / l in terms of dry cell concentration.

【0012】また、生成蓄積系中の酵素反応はATP、
マグネシウムイオン、カリウムイオンおよびリン酸を必
要とするものが多く、ATPが0.1mM〜15mM、
好ましくは1mM〜5mMであり、MgSO4 ・7H2
Oが0.01〜0.2%、好ましくは0.02〜0.1
%であり、KH2 PO4 が3〜14%、好ましくは6〜
13%の濃度で用いられるのが通常である。
The enzyme reaction in the product accumulation system is ATP,
Many require magnesium ions, potassium ions and phosphoric acid, and ATP is 0.1 mM to 15 mM,
Preferably 1mM~5mM, MgSO 4 · 7H 2
O is 0.01 to 0.2%, preferably 0.02 to 0.1
%, And KH 2 PO 4 is 3 to 14%, preferably 6 to
It is usually used at a concentration of 13%.

【0013】生成蓄積反応中は有機酸の生成に伴ってp
Hの低下が生じるので、炭酸カルシウムまたは苛性カリ
などのアルカリで通常pH5〜10、好ましくは7〜9
に調節することがホスホエノールピルビン酸生産のため
には有効である。
During the production-accumulation reaction, p is generated as the organic acid is produced.
Since a decrease in H occurs, pH is usually 5 to 10, preferably 7 to 9 with an alkali such as calcium carbonate or caustic potash.
Is effective for phosphoenolpyruvate production.

【0014】反応中の温度は20〜37℃、好ましくは
25〜32℃が適当である。
The temperature during the reaction is suitably 20 to 37 ° C, preferably 25 to 32 ° C.

【0015】反応終了後、生成蓄積系中に生成蓄積した
ホスホエノールピルビン酸は逆浸透膜などを使い、ホス
ホエノールピルビン酸とリン酸を分離し、水酸化アルカ
リを加え、ホスホエノールピルビン酸のアルカリ金属塩
水溶液とし、濃縮・晶析により単離できる。
After completion of the reaction, the phosphoenolpyruvate produced and accumulated in the production and accumulation system is separated into phosphoenolpyruvate and phosphoric acid using a reverse osmosis membrane or the like, alkali hydroxide is added, and phosphoenolpyruvate alkali is added. It can be isolated by concentration and crystallization as an aqueous metal salt solution.

【0016】[0016]

【実施例】以下、実施例によって本発明を説明する。EXAMPLES The present invention will be described below with reference to examples.

【0017】実施例において生成したピルビン酸の確認
と定量は、高速液体クロマトグラフィー、ピルベートキ
ナーゼと乳酸デヒドロゲナーゼを用いる酵素法などによ
り行った。以下の分析結果については上記両分析法とも
よく合致しており、同じ分析数値を示した。
Confirmation and quantification of pyruvic acid produced in the examples were carried out by high performance liquid chromatography, an enzymatic method using pyruvate kinase and lactate dehydrogenase, and the like. The following analytical results were in good agreement with both of the above analytical methods and showed the same analytical values.

【0018】実施例1 表1に示した各種酵母を、グリコース0.5%、KH2
PO4 0.2%、MgSO4 ・7H2 O0.05%、ペ
プトン1.0%、酵母エキス0.1%、pH6.0から
なる倍地100mlを500ml容振盪フラスコに分注滅菌
後、1白金植菌し、24時間、30℃で振盪培養した。
Example 1 Various yeasts shown in Table 1 were mixed with 0.5% glucose and KH 2
PO 4 0.2%, MgSO 4 · 7H 2 O0.05%, 1.0% peptone, 0.1% yeast extract, after dispensing sterilized twice locations 100ml consisting pH6.0 to 500ml-volume shaking flask, 1 The cells were inoculated with platinum and cultured with shaking at 30 ° C. for 24 hours.

【0019】培養終了後遠心分離して集菌し、これをグ
ルコース1%、KH2 PO4 9%、MgSO4 ・7H2
O0.05%、ATP5mMを含有する反応液60ml
(KOH水溶液でpHを7.5に調整)に添加し、30
℃で30時間反応した。
After the completion of the culture, the cells were collected by centrifugation to collect the cells, which were glucose 1%, KH 2 PO 4 9% and MgSO 4 .7H 2.
60 ml of reaction solution containing 0.05% O and 5 mM ATP
(PH adjusted to 7.5 with KOH aqueous solution), 30
Reacted at 30 ° C. for 30 hours.

【0020】各反応液中に生成したホスホエノールピル
ビン酸は、表1のとおりであった。
The phosphoenolpyruvate produced in each reaction solution is shown in Table 1.

【表1】 [Table 1]

【0021】実施例2 実施例1で用いた反応液の炭素源を表2に示す炭素源に
おきかえ、表2に示す菌株を用いて培養した結果を表2
に示す。
Example 2 The carbon source of the reaction solution used in Example 1 was replaced with the carbon source shown in Table 2, and the results of culturing with the strains shown in Table 2 were shown in Table 2.
Shown in.

【0022】[0022]

【表2】 [Table 2]

【0023】[0023]

【発明の効果】本発明によれば、酵母の生産する炭素源
資化酵素系を用いて、炭素源よりホスホエノールピルビ
ン酸を温和な条件下で煩雑な操作を要することなく製造
することができる。
INDUSTRIAL APPLICABILITY According to the present invention, phosphoenolpyruvate can be produced from a carbon source under mild conditions without complicated operations using a carbon source-utilizing enzyme system produced by yeast. .

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 (C12P 9/00 C12R 1:78) (C12P 9/00 C12R 1:84) (C12P 9/00 C12R 1:72) (C12P 9/00 C12R 1:73) (C12P 9/00 C12R 1:88) ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Internal reference number FI Technical indication (C12P 9/00 C12R 1:78) (C12P 9/00 C12R 1:84) (C12P 9/00 C12R 1:72) (C12P 9/00 C12R 1:73) (C12P 9/00 C12R 1:88)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 サッカロミセス(Saccharomy
ces)属、ハンゼヌラ(Hansenula)属、ピ
キア(Pichia)属、キャンディダ(Candid
a)属またはトルロプシス(Torulopsis)属
に属する酵母の培養物を用いて、前記酵母の資化し得る
炭素源よりホスホエノールピルビン酸を生成蓄積せし
め、これを単離採取することを特徴とするホスホエノー
ルピルビン酸の製造方法。
1. Saccharomyces
ces, Hansenula, Pichia, Candida
a) Phosphoenols characterized by producing and accumulating phosphoenolpyruvate from a carbon source that can be assimilated by the yeast using a culture of yeast belonging to the genus or the genus Torulopsis, and isolating and collecting the phosphoenolpyruvate. Method for producing pyruvic acid.
JP34963392A 1992-12-28 1992-12-28 Method for producing phosphoenolpyruvate Expired - Fee Related JP3151982B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34963392A JP3151982B2 (en) 1992-12-28 1992-12-28 Method for producing phosphoenolpyruvate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34963392A JP3151982B2 (en) 1992-12-28 1992-12-28 Method for producing phosphoenolpyruvate

Publications (2)

Publication Number Publication Date
JPH06197778A true JPH06197778A (en) 1994-07-19
JP3151982B2 JP3151982B2 (en) 2001-04-03

Family

ID=18405059

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34963392A Expired - Fee Related JP3151982B2 (en) 1992-12-28 1992-12-28 Method for producing phosphoenolpyruvate

Country Status (1)

Country Link
JP (1) JP3151982B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1081230A3 (en) * 1999-08-30 2002-06-05 Kyowa Hakko Kogyo Co., Ltd. Process for producing N-acetyl-neuraminic acid

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1081230A3 (en) * 1999-08-30 2002-06-05 Kyowa Hakko Kogyo Co., Ltd. Process for producing N-acetyl-neuraminic acid
US6846656B1 (en) 1999-08-30 2005-01-25 Kyowa Hakko Kogyo Co., Ltd. Process for producing N-acetylneuraminic acid
US7579175B2 (en) 1999-08-30 2009-08-25 Kyowa Hakko Bio Co., Ltd. Process for producing N-acetylneuraminic acid

Also Published As

Publication number Publication date
JP3151982B2 (en) 2001-04-03

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