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JP3484917B2 - Method for producing hypoxanthine - Google Patents
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JP3484917B2 - Method for producing hypoxanthine - Google Patents

Method for producing hypoxanthine

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Publication number
JP3484917B2
JP3484917B2 JP9523497A JP9523497A JP3484917B2 JP 3484917 B2 JP3484917 B2 JP 3484917B2 JP 9523497 A JP9523497 A JP 9523497A JP 9523497 A JP9523497 A JP 9523497A JP 3484917 B2 JP3484917 B2 JP 3484917B2
Authority
JP
Japan
Prior art keywords
hypoxanthine
adenine
medium
negative
culture
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 - Fee Related
Application number
JP9523497A
Other languages
Japanese (ja)
Other versions
JPH1028593A (en
Inventor
康弘 長島
徹 宇田
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.)
Nok Corp
Original Assignee
Nok Corp
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 Nok Corp filed Critical Nok Corp
Priority to JP9523497A priority Critical patent/JP3484917B2/en
Publication of JPH1028593A publication Critical patent/JPH1028593A/en
Application granted granted Critical
Publication of JP3484917B2 publication Critical patent/JP3484917B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、ヒポキサンチンの
製造方法に関する。更に詳しくは、微生物を用いてヒポ
キサンチンを製造する方法に関する。
TECHNICAL FIELD The present invention relates to a method for producing hypoxanthine. More specifically, it relates to a method for producing hypoxanthine using a microorganism.

【0002】[0002]

【従来の技術】ヒポキサンチンは、動物、植物、微生物
中などに広く存在する核酸の中間代謝物であって、イノ
シン、イノシン酸生産の前駆物質である。ヒポキサンチ
ンはまた、DNA、RNA成分の前駆物質としてあるいは食品
の旨味成分として用いられているイノシン酸等の塩基部
として存在し、多くのプリン系核酸代謝の中核をなす重
要な物質でもある。ヒポキサンチンは、アデニンの脱ア
ミノ酵素反応(アデニンデアミナーゼ反応)または亜硝
酸によるアデニンの脱アミド反応によって、あるいはヌ
クレオシドホスホリラーゼによるイノシンの加リン酸分
解によって製造されるが、これを多量に製造する場合、
脱アミノ酵素を用いる方法では大量のアデニンの脱アミ
ノ酵素が必要であり、また亜硝酸によるアデニンの脱ア
ミド化方法では、反応後の物質の処理を行う必要がある
などの問題点がある。
BACKGROUND OF THE INVENTION Hypoxanthine is an intermediate metabolite of nucleic acid widely existing in animals, plants, microorganisms and the like, and is a precursor of inosine and inosine acid production. Hypoxanthine also exists as a base of inosinic acid, which is used as a precursor of DNA and RNA components or as an umami component of foods, and is an important substance that forms the core of many purine-based nucleic acid metabolisms. Hypoxanthine is produced by deaminase reaction of adenine (adenine deaminase reaction) or deamidation reaction of adenine by nitrous acid, or by phosphorolysis of inosine by nucleoside phosphorylase, and when it is produced in a large amount,
The method using a deaminase requires a large amount of adenine deaminase, and the method for deamidating adenine with nitrous acid has a problem that a substance after the reaction needs to be treated.

【0003】[0003]

【発明が解決しようとする課題】本発明は、ヒポキサン
チンを微生物を用いて効率的に製造する方法を提供する
ことを目的とする。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for efficiently producing hypoxanthine using a microorganism.

【0004】[0004]

【課題を解決するための手段】かかる本発明の目的は、
ヒポキサンチンを生成せしめる能力を有するシュードモ
ナス属に属する微生物を、アデニン添加完全培地、好ま
しくはpHを7.5〜10.5に調整したアデニン添加完全培地
において培養することによりヒポキサンチンを生成蓄積
せしめ、これを採取することによって達成される。
The object of the present invention is as follows.
A microorganism belonging to the genus Pseudomonas having the ability to produce hypoxanthine is cultured in an adenine-added complete medium, preferably an adenine-added complete medium whose pH is adjusted to 7.5 to 10.5 to allow hypoxanthine to be produced and accumulated, and this is collected. To be achieved.

【0005】[0005]

【発明の実施の形態】ヒポキサンチンを生成せしめる能
力を有するシュードモナス属に属する微生物としては、
例えば P. solanacearum No.206-04 (FERM P-15545)が
用いられる。この微生物は、長野県小谷村の温泉水から
下記の方法により、培養、分離されたものである。
BEST MODE FOR CARRYING OUT THE INVENTION As a microorganism belonging to the genus Pseudomonas having an ability to produce hypoxanthine,
For example, P. solanacearum No. 206-04 (FERM P-15545) is used. This microorganism was cultivated and separated from hot spring water in Otari Village, Nagano Prefecture by the following method.

【0006】即ち、完全培地としてのL-broth(トリプト
ン1%、酵母エキス 0.5%、NaCl 0.5%、殺菌前のpH7.0)に
約0.005%以上、一般には0.05%のアデニンを添加した培
地3mlを試験管に入れ、これに採取した温泉水1mlを添
加し、40℃で72時間振とう培養され、その後分離され
た。
That is, L-broth as a complete medium (tryptone 1%, yeast extract 0.5%, NaCl 0.5%, pH 7.0 before sterilization) about 0.005% or more, generally 0.05% adenine 3 ml medium Was placed in a test tube, 1 ml of the hot spring water collected was added thereto, and the mixture was incubated at 40 ° C. for 72 hours with shaking, and then separated.

【0007】このP. solanacearum No.206-04は、下記
の如き菌学的性質を有する。 A.形態 (1)細胞の形、大きさ:桿菌、0.5μm×1μm (2)運動性:あり (3)胞子:なし (4)グラム染色性:陰性 B.培地における成育状態 肉汁寒天平板培養:黄褐色、滑らか C.生理学的性質 (1)硝酸塩の還元:陰性 (2)VPテスト:陽性 (3)インドールの生成:陰性 (4)硫化水素の生成:陰性 (5)クエン酸の利用:陰性 (6)色素の生成:陰性 (7)ウレアーゼ:陰性 (8)オキシダーゼ:陽性 (9) リジンの分解:陰性 (10)オルニチンの分解:陰性 (11)アルギニンの分解:陰性 (12)生育の範囲:pH5〜8 、温度30〜50℃ (13)酸素に対する態度:通性嫌気性 (14)糖類からの酸生成 培地:ペプトン2g、NaCl 5g、K2HPO4 0.3g、炭水化物10
g、ブロムチモールブルー0.08g、寒天15g、蒸留水1000m
l(pH7.1) 添加濃度:1% D-グルコース + D-マンニット + アドニット − L-アラビノーズ + イノシット − D-ソルビット − 麦芽糖 − 白糖 +
This P. solanacearum No. 206-04 has the following mycological properties. A. Morphology (1) Cell shape and size: bacillus, 0.5 μm × 1 μm (2) Motility: Yes (3) Spores: No (4) Gram stainability: Negative B. Growth state broth agar plate culture in medium: yellowish brown, smooth C.I. Physiological properties (1) Reduction of nitrate: Negative (2) VP test: Positive (3) Indole formation: Negative (4) Hydrogen sulfide formation: Negative (5) Citric acid utilization: Negative (6) Dye formation : Negative (7) Urease: Negative (8) Oxidase: Positive (9) Lysine degradation: Negative (10) Ornithine degradation: Negative (11) Arginine degradation: Negative (12) Growth range: pH 5-8, temperature 30-50 ℃ (13) Attitude toward oxygen: Facultative anaerobic (14) Acid production medium from sugars: Peptone 2g, NaCl 5g, K 2 HPO 4 0.3g, carbohydrate 10
g, bromthymol blue 0.08g, agar 15g, distilled water 1000m
l (pH7.1) Concentration of addition: 1% D-glucose + D-mannitol + Adnit-L-arabinose + inosit-D-sorbit-maltose-sucrose +

【0008】以上の菌学的性質に基いて、本菌を Berge
y's Mannual of DeterminativeBacteriology 第9版によ
り検索した結果、Pseudomonassolanacearum種に属す
る菌であることが確認された。
Based on the above mycological properties,
As a result of searching by y's Mannual of Determinative Bacteriology 9th edition, it was confirmed to be a bacterium belonging to the genus Pseudomonas solanacearum .

【0009】本発明方法を実施する際、アデニン添加完
全培地のpHを7.5〜10.5、好ましくは8.5〜9.5に調整し
て用いると、ヒポキサンチンの生産速度が著しく向上す
る。pHがこれ以上では、培地中のアデニンが析出するよ
うになる。アデニン添加完全培地のpHの調整は、水酸化
ナトリウム水溶液によって行なわれる。
When carrying out the method of the present invention, adjusting the pH of the adenine-added complete medium to 7.5 to 10.5, preferably 8.5 to 9.5, the hypoxanthine production rate is significantly improved. If the pH is higher than this, adenine in the medium will precipitate. The pH of the complete medium containing adenine is adjusted with an aqueous sodium hydroxide solution.

【0010】[0010]

【実施例】【Example】

実施例1P. solanacearum No.206-04 (FERM P-15545)を、50mlの
L-broth 液体培地中で一晩振とう培養することにより前
培養を行った後、L-broth 液体培地に0.05%のアデニン
を添加した培養培地500ml中で、邪魔板付き回転培養槽
を用いて、攪拌回転数4000rpm、40℃の条件下でで72時
間培養することにより本培養を行った。
Example 1 P. solanacearum No. 206-04 (FERM P-15545) was added in an amount of 50 ml.
After preculturing by shaking culture in L-broth liquid medium overnight, in a culture medium 500 ml containing 0.05% adenine in L-broth liquid medium, using a rotary culture tank with a baffle plate. The main culture was carried out by culturing for 72 hours under the conditions of stirring rpm of 4000 rpm and 40 ° C.

【0011】これら一連の操作を行った後、培養液から
遠心機を用いて菌株を抽出し、HPLCによって、ヒポキサ
ンチン生産量の定量が行われた。カラムとしてはODS-80
TMを、また展開溶媒としては0.5M蟻酸アンモニウムを用
い、カラム温度35℃で展開した。そして、検出波長254n
mでヒポキサンチン生産量の定量を行ったところ、L-bro
th 液体培地に0.05%のアデニンを加えた培養液1ml当り
約800〜900μgの生産量でヒポキサンチンが生産される
ことが確認された。
After carrying out these series of operations, the strain was extracted from the culture medium using a centrifuge, and the amount of hypoxanthine produced was quantified by HPLC. ODS-80 as a column
TM was used and 0.5M ammonium formate was used as a developing solvent, and the column was developed at a column temperature of 35 ° C. And the detection wavelength 254n
Hypoxanthine production was quantified using m-
It was confirmed that hypoxanthine was produced at a production amount of about 800 to 900 μg per 1 ml of a culture medium containing 0.05% adenine in th liquid medium.

【0012】なお、アデニンの添加されない完全培地を
用いた場合には、ヒポキサンチンの生産がみられない。
When a complete medium containing no adenine was used, hypoxanthine was not produced.

【0013】実施例2 L-broth 液体培地(pH7.0)に0.05%のアデニンを添加し
た培養培地3mlを試験管に入れ、その培地にP. solanac
earum No.206-04 (FERM P-15545)を加え、37℃の条件下
でで24時間振とう培養を行なって前培養液を得た、その
後、水酸化ナトリウム水溶液によりアデニン添加完全培
地のpHを7.5〜10.0の範囲内で調整し、この培地8.5mlに
前培養液1.5mlを加え、培養温度37℃で再度振とう培養
を100時間行なった。
Example 2 3 ml of a culture medium prepared by adding 0.05% adenine to L-broth liquid medium (pH 7.0) was placed in a test tube, and P. solanac was added to the medium .
earum No.206-04 the (FERM P-15545) was added, to obtain a pre-culture broth is performed for 24 hours with shaking cultured under conditions of 37 ° C., then, pH of adenine added complete medium with sodium hydroxide solution Was adjusted within the range of 7.5 to 10.0, 1.5 ml of the preculture liquid was added to 8.5 ml of this medium, and shaking culture was again carried out at a culture temperature of 37 ° C. for 100 hours.

【0014】アデニン添加完全培地のpHとヒポキサンチ
ンの生産速度との関係は、下記表に示される。この場合
のアデニンの資化速度は0.75〜1.66μg/ml・hrとなり、p
H7.0のときの0.65μg/ml・hrよりは高い値を示した。pH ヒポキサンチンの生産速度(μg/ml・hr) 7.0 0.65 7.5 0.75 8.0 0.91 8.5 1.31 9.0 1.66 9.5 1.54 10.0 1.16
The relationship between the pH of the complete medium containing adenine and the production rate of hypoxanthine is shown in the following table. The adenine assimilation rate in this case is 0.75 to 1.66 μg / ml ・ hr, and p
The value was higher than 0.65 μg / ml · hr at H7.0. pH Hypoxanthine production rate (μg / ml ・ hr) 7.0 0.65 7.5 0.75 8.0 0.91 8.5 1.31 9.0 1.66 9.5 1.54 10.0 1.16

【0015】[0015]

【発明の効果】ヒポキサンチンを生成せしめる能力を有
するシュードモナス属に属する微生物により、旨味成分
として用いられているイノシン、イノシン酸の前駆物質
であるヒポキサンチンを効率よくかつ廉価に製造するこ
とができる。
INDUSTRIAL APPLICABILITY A microorganism belonging to the genus Pseudomonas having the ability to produce hypoxanthine can efficiently and inexpensively produce hypoxanthine, which is a precursor of inosine and inosine acid used as umami components.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C12P 17/00 - 17/18 C07D 473/30 CA/REGISTRY(STN) JSTPlus(JOIS) BIOSIS/WPI(DIALOG) PubMed─────────────────────────────────────────────────── ─── Continuation of front page (58) Fields surveyed (Int.Cl. 7 , DB name) C12P 17/00-17/18 C07D 473/30 CA / REGISTRY (STN) JSTPlus (JOIS) BIOSIS / WPI (DIALOG) ) PubMed

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ヒポキサンチンを生成せしめる能力を有
するシュードモナス属に属する微生物を、アデニン添加
完全培地において培養することによりヒポキサンチンを
生成蓄積せしめ、これを採取することを特徴とするヒポ
キサンチンの製造方法。
1. A method for producing hypoxanthine, characterized in that a microorganism belonging to the genus Pseudomonas having the ability to produce hypoxanthine is cultured in a complete medium containing adenine to produce and accumulate hypoxanthine, which is then collected. .
【請求項2】 pHを7.5〜10.5に調整したアデニン添加
完全培地が用いられる請求項1記載のヒポキサンチンの
製造方法。
2. The method for producing hypoxanthine according to claim 1, wherein an adenine-added complete medium having a pH adjusted to 7.5 to 10.5 is used.
JP9523497A 1996-04-03 1997-03-28 Method for producing hypoxanthine Expired - Fee Related JP3484917B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9523497A JP3484917B2 (en) 1996-04-03 1997-03-28 Method for producing hypoxanthine

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP8-106343 1996-04-03
JP10634396 1996-04-03
JP9523497A JP3484917B2 (en) 1996-04-03 1997-03-28 Method for producing hypoxanthine

Publications (2)

Publication Number Publication Date
JPH1028593A JPH1028593A (en) 1998-02-03
JP3484917B2 true JP3484917B2 (en) 2004-01-06

Family

ID=26436506

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9523497A Expired - Fee Related JP3484917B2 (en) 1996-04-03 1997-03-28 Method for producing hypoxanthine

Country Status (1)

Country Link
JP (1) JP3484917B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001302427A (en) * 2000-04-25 2001-10-31 Nok Corp Plant growth accelerator and method for accelerating growth of plant by using the accelerator
KR20000072445A (en) * 2000-09-04 2000-12-05 쓰루 슈수케 Manufacture method of Hypoxanthine.
CN109298086A (en) * 2018-09-18 2019-02-01 江西省农业科学院农产品质量安全与标准研究所(江西省农业科学院农产品加工研究所) It is a kind of while measuring the efficient liquid-phase chromatography method of a variety of flavour nucleotides and application in fresh meat
CN114703065B (en) * 2022-04-11 2024-06-14 安琪酵母(济宁)有限公司 Yeast extract rich in bases and base derivatives and preparation method thereof

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001224393A (en) 2000-02-16 2001-08-21 Nok Corp Method of preparing hypoxanthine

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001224393A (en) 2000-02-16 2001-08-21 Nok Corp Method of preparing hypoxanthine

Also Published As

Publication number Publication date
JPH1028593A (en) 1998-02-03

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