JPH0549497A - Method for producing zeaxanthin - Google Patents

Method for producing zeaxanthin

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Publication number
JPH0549497A
JPH0549497A JP21245491A JP21245491A JPH0549497A JP H0549497 A JPH0549497 A JP H0549497A JP 21245491 A JP21245491 A JP 21245491A JP 21245491 A JP21245491 A JP 21245491A JP H0549497 A JPH0549497 A JP H0549497A
Authority
JP
Japan
Prior art keywords
culture
zeaxanthin
concentrated
alteromonas
extracted
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
JP21245491A
Other languages
Japanese (ja)
Other versions
JP3007453B2 (en
Inventor
Akihiro Yokoyama
昭裕 横山
Nobuko Otaki
伸子 大滝
Wataru Miki
渉 幹
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.)
KAIYO BIO TECH LAB
KAIYO BIO TECHNOL KENKYUSHO KK
Original Assignee
KAIYO BIO TECH LAB
KAIYO BIO TECHNOL KENKYUSHO KK
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Application filed by KAIYO BIO TECH LAB, KAIYO BIO TECHNOL KENKYUSHO KK filed Critical KAIYO BIO TECH LAB
Priority to JP21245491A priority Critical patent/JP3007453B2/en
Publication of JPH0549497A publication Critical patent/JPH0549497A/en
Application granted granted Critical
Publication of JP3007453B2 publication Critical patent/JP3007453B2/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)

Abstract

PURPOSE:To obtain the title compound useful for coloring cultured fishes, being readily purified, in high yield without admixture of chlorophyll by culturing a bacterium belonging to the genus Alteromonas, capable of producing zeaxanthin in a medium and collecting a product from the culture mixture. CONSTITUTION:A bacterium [e.g. Alteromonas sp. KK10,203C (FERM P-12,434)] belonging to the genus Alteromonas, capable of producing zeaxanthin is inoculated into a seed medium, subjected to shaking culture at 25 deg.C for 48 hours, the prepared seed culture solution is transferred to a culture tank in a ratio of 2%V/V, subjected to aerated spinner culture at 25 deg.C for 120 hours, the culture solution is filtered off to collect cells, which are ground, extracted with acetone, the extracted solution is concentrated, passed through a polystyrene-based adsorbent column, an adsorbed substance is eluted with methanol, concentrated, extracted with benzene and purified by silica gel chromatography and high- performance liquid chromatography to give zeaxanthin in high yield.

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、微生物が生産するゼア
キサンチンの製造法に関するものである。ゼアキサンチ
ンは、養殖魚の色揚げ、鶏卵の卵黄質改善等に有用であ
り、また抗酸化剤としても利用される。
TECHNICAL FIELD The present invention relates to a method for producing zeaxanthin produced by microorganisms. Zeaxanthin is useful for deep-fried farmed fish, improving yolk quality of chicken eggs, and is also used as an antioxidant.

【0002】[0002]

【従来の技術】従来より、ゼアキサンチンは、養殖アユ
の色揚げや鶏卵の卵黄質改善等の目的で広く用いられて
おり、そのほとんどが微細藻類のスピルリナの大量培養
によって調整されている。しかし、微細藻類の培養にお
いては、光合成に欠くことのできない光を供給しなけれ
ばならず、太陽光採取のため立地条件や人工光供給のた
めの培養装置等の設備が必要になる。また、微細藻類
は、一般に生育速度が遅く、十分な培養密度を得るため
に一週間から数週間を要し、生産性に問題がある。さら
に、微細藻類由来のゼアキサンチンの精製においてクロ
ロフィルとの分離が困難で精製工程が複雑である。これ
らの点を克服するために、陸上細菌 Erwiniauredovora
による発酵生産も研究されている (J.Bacteriol 172,6
704,1990)が、その収率極めて悪く実用上問題が残る。
以上のことよりゼアキサンチンの簡易な製造法の開発が
望まれている。
2. Description of the Related Art Conventionally, zeaxanthin has been widely used for the purpose of raising the color of cultured ayu and improving the yolk quality of chicken eggs, and most of them are prepared by mass-culturing microalga Spirulina. However, in culturing microalgae, light that is indispensable for photosynthesis must be supplied, and site conditions for collecting sunlight and equipment such as a culture device for supplying artificial light are required. In addition, microalgae generally have a slow growth rate, and it takes 1 to several weeks to obtain a sufficient culture density, which causes a problem in productivity. Furthermore, in the purification of zeaxanthin derived from microalgae, it is difficult to separate it from chlorophyll, and the purification process is complicated. To overcome these points, the land bacterium Erwiniauredovora
Fermentative production by lactic acid has also been studied (J.
704, 1990), but the yield is extremely poor, and a problem remains in practical use.
From the above, development of a simple method for producing zeaxanthin is desired.

【0003】[0003]

【発明が解決しようとする課題】従って、本発明は、従
来の微細藻類による製造法よりも簡便にゼアキサンチン
を提供することを目的とする。
SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide zeaxanthin more easily than the conventional production method using microalgae.

【0004】[0004]

【課題を解決するための手段】本発明はアルテロモナス
属に属しゼアキサンチンを生産する能力を有する微生物
を培地に培養し、培養物からゼアキサンチンを採取する
ことを特徴とするゼアキサンチンの製造法にある。以下
に本発明を詳細に説明する。
The present invention provides a method for producing zeaxanthin, which comprises culturing in a medium a microorganism belonging to the genus Alteromonas and having the ability to produce zeaxanthin, and collecting zeaxanthin from the culture. The present invention will be described in detail below.

【0005】ゼアキサンチン生産菌株としてはアルテロ
モナス属に属しゼアキサンチン生産能を有する菌株であ
ればいずれの菌株でも用いることができる。またこれら
の菌株の人工的変異方法、例えば紫外線照射、X線照
射、変異誘起剤処理などあるいは自然発生による変異
株、また遺伝子工学あるいは細胞融合による変異株でも
ゼアキサンチンを生産するものであれば本発明に用いる
ことができる。代表的菌株としてKK10203C株があげられ
る。
As the zeaxanthin-producing strain, any strain can be used as long as it belongs to the genus Alteromonas and has a zeaxanthin-producing ability. In addition, any artificial mutation method of these strains, for example, ultraviolet irradiation, X-ray irradiation, treatment with a mutagen or the like, or a naturally occurring mutant, or a mutant by genetic engineering or cell fusion, as long as it produces zeaxanthin, is used in the present invention. Can be used for. A representative strain is the KK10203C strain.

【0006】KK10203C株の菌学的性質について以下に述
べるが、該性質の決定は清水らの方法〔門田元、多賀信
夫編:海洋微生物研究法、学会出版センターpp.229(198
5)〕に従った。形態学的検討は、光学顕微鏡を用い、特
に胞子表面の形態については走査型電子顕微鏡によっ
た。KK10203C株の菌学的性質は以下の通りである。 (1) グラム染色 陰性 (2) 形態 菌の形・大きさ :棹状、2.2 μm×0.25μm 運動性 :あり 鞭毛・長さ :極単毛あり,2.0 μm (3) 菌体色素 :黄色 (4) 生理的性質 オキシダーゼ :陰性 グルコース分解性:陰性 ゼラチン分解性 :陽性 DNA分解性 :陰性 (5) OFテスト 陰性 以上の菌学的性質の知見からKK10203C株をアルテロモナ
ス(Alteromonas) 属に属する微生物と同定した。本属に
おける種の同定においてはエヌ・アール・クリーグ(N.
R.Krieg) 、ジェイ・ジイ・ホルト(J.G.Holt)編、バー
ジーズ・マニュアル・オブ・システマチック・バクテリ
オジー(Bergey's Manual of Systematic Bacteriology)
をもとに検索した。
The bacteriological properties of the KK10203C strain will be described below. The properties are determined by the method of Shimizu et al. [Gen Kadota, Nobuo Taga: Marine Microbial Research Method, Academic Publishing Center pp.229 (198).
5)] was followed. The morphological examination was performed by using an optical microscope, and particularly by using a scanning electron microscope for the morphology of the spore surface. The mycological properties of the KK10203C strain are as follows. (1) Gram stain Negative (2) Morphology Shape / size of bacterium: rod-like, 2.2 μm × 0.25 μm Motility: Yes Flagella / length: Extremely monochrysian, 2.0 μm (3) Bacterial pigment: Yellow ( 4) Physiological properties Oxidase: Negative Glucose degradability: Negative Gelatin degradability: Positive DNA degradability: Negative (5) OF test negative Based on the above findings of mycological properties, strain KK10203C was identified as a microorganism belonging to the genus Alteromonas. Identified. In identification of species in this genus, N. K. League (N.
R. Krieg), edited by JG Holt, Bergey's Manual of Systematic Bacteriology
It searched based on.

【0007】検索の結果、KK10203C株の性質と一致する
種を特定することは困難でありKK10203C株をアルテロモ
ナス・sp(Alteromonas sp.) とした。そしてこの菌株は
工業技術院微生物工業技術研究所に微工研菌寄第12434
号(FERM -12434)として寄託した。( 原寄託日:平成3
年8月19日)。上記微生物は一般に微生物の培養に用
いられる培地で培養され、生産されるゼアキサンチンは
常法により採取することができる。
[0007] As a result of the search, it was difficult to identify a species that matches the characteristics of the KK10203C strain, and the KK10203C strain was designated as Alteromonas sp. And this strain was sent to the Institute of Microbial Technology, Institute of Industrial Technology
No. (FERM -12434). (Date of original deposit: Heisei 3
August 19th). The above microorganisms are generally cultured in a medium used for culturing microorganisms, and the zeaxanthin produced can be collected by a conventional method.

【0008】培地としては資化可能な炭素源、窒素源、
無機物および必要な生育、生産促進物質を程よく含有す
る培地であれば合成培地、天然培地いずれでも使用可能
である。炭素源としてはグルコース、澱粉、デキストリ
ン、マンノース、フラクトース、シュクロース、ラクト
ース、キシロース、アラビノース、マンニトール、糖蜜
などを単独または組み合わせて用いられる。さらに、菌
の資化能によっては炭化水素、アルコール類、有機酸な
ども用いられる。窒素源としては塩化アンモニウム、硝
酸アンモニウム、硝酸ナトリウム、尿素、ペプトン、肉
エキス、酵母エキス、乾燥酵母、コーン・スチープ・リ
カー、大豆粉、カザミノ酸などが単独または組み合わせ
て用いられる。そのほか、食塩、塩化カリウム、硫酸マ
グネシウム、炭酸カルシウム、リン酸二水素カリウム、
リン酸水素二カリウム、硫酸第一鉄、塩化カルシウム、
硫酸マンガン、硫酸亜鉛、硫酸銅などの無機塩類や海水
を必要に応じて加える。さらに使用菌の生育やゼアキサ
ンチンの生産を促進する微量成分を適当に添加すること
ができる。
As the medium, assimilable carbon source, nitrogen source,
Either a synthetic medium or a natural medium can be used as long as it is a medium containing an inorganic substance and necessary growth and production promoting substances in an appropriate amount. As the carbon source, glucose, starch, dextrin, mannose, fructose, sucrose, lactose, xylose, arabinose, mannitol, molasses, etc. may be used alone or in combination. Further, depending on the assimilation ability of the bacterium, hydrocarbons, alcohols, organic acids, etc. are also used. As the nitrogen source, ammonium chloride, ammonium nitrate, sodium nitrate, urea, peptone, meat extract, yeast extract, dry yeast, corn steep liquor, soybean powder, casamino acid, etc. may be used alone or in combination. In addition, salt, potassium chloride, magnesium sulfate, calcium carbonate, potassium dihydrogen phosphate,
Dipotassium hydrogen phosphate, ferrous sulfate, calcium chloride,
Inorganic salts such as manganese sulfate, zinc sulfate, and copper sulfate and seawater are added as needed. Furthermore, a trace amount component that promotes the growth of the bacterium used and the production of zeaxanthin can be appropriately added.

【0009】培養法としては一般の培養法が用いられる
が、液体培養法、とくに深部攪拌培養法がもっとも適し
ている。培養温度は16〜37℃、特に22〜30℃が適当であ
り、培養中の培地のpHはアンモニア水や炭酸アンモニウ
ム溶液などを添加して、4 〜10、特に 6〜8に維持する
ことが望ましい。液体培養で通常 1〜7日培養をおこな
うと、目的物質のゼアキサンチンが菌体中に生成蓄積さ
れる。培養物中の生成量が最大に達したときに培養を停
止する。
As the culturing method, a general culturing method is used, but a liquid culturing method, particularly a deep agitation culturing method is most suitable. A suitable culture temperature is 16 to 37 ° C, especially 22 to 30 ° C. The pH of the culture medium during the culture may be maintained at 4 to 10, especially 6 to 8 by adding aqueous ammonia or ammonium carbonate solution. desirable. When liquid culture is generally performed for 1 to 7 days, the target substance zeaxanthin is produced and accumulated in the cells. The culture is stopped when the maximum amount of production in the culture is reached.

【0010】培養物からゼアキサンチンの単離精製は、
微生物代謝生産物をその培養物から単離精製するために
常用される方法に従っておこなわれる。例えば、菌体を
磨砕しヘキサン、ベンゼン、クロロホルム、アセトン、
エーテル、酢酸エチルなどで抽出する。次いでこの抽出
液を濃縮後、シリカゲルカラムクロマトグラフィー、ゲ
ルろ過(SephadexLH-20)等にかけてゼアキサンチンを分
離、精製する。なお、培養、精製操作中のゼアキサンチ
ンの動向は薄層クロマトグラフィーによるゼアキサンチ
ンの黄色を目安として追跡することができる。
Isolation and purification of zeaxanthin from the culture is
It is carried out according to a method commonly used for isolating and purifying a microbial metabolite from the culture. For example, microbial cells are ground and hexane, benzene, chloroform, acetone,
Extract with ether, ethyl acetate, etc. Then, the extract is concentrated and then subjected to silica gel column chromatography, gel filtration (Sephadex LH-20), etc. to separate and purify zeaxanthin. The trend of zeaxanthin during the culture and purification operations can be traced by using the yellow color of zeaxanthin by thin layer chromatography as a guide.

【0011】[0011]

【発明の効果】本発明によれば、従来微細藻類の培養物
により得られたゼアキサンチンを、極一般的な培養装置
により、高収率で容易に得ることができる。また、微細
藻類特有のクロロフィルの混入がなく、精製工程におい
て大幅に改善された。以下実施例により本発明を説明す
るが、本発明はこの実施例によりその技術的範囲が限定
されるものではない。
INDUSTRIAL APPLICABILITY According to the present invention, zeaxanthin conventionally obtained from a culture of microalgae can be easily obtained in a high yield by an extremely general culture device. In addition, there was no mixing of chlorophyll peculiar to microalgae, which was greatly improved in the purification process. The present invention will be described below with reference to examples, but the technical scope of the present invention is not limited by these examples.

【0012】[0012]

【実施例】種菌としてアルテロモナス・Sp.kk10203C 株
を用いる。ペプトン5g/L、酵母エキス1g/L、グ
ルコース2g/L、リン酸第二鉄0.04g/L、酢酸ナト
リウム0.01g/L、精製水250 ml、海水750 mlの組成を
有する種培地(殺菌前pH7.7)100 mlを200 ml容量の三角
フラスコに作製後該菌株を植菌し、25℃で48時間振とう
( 100rpm) 培養した。このようにして得られた種培養
液を10L容量の培養槽中の上記組成と同一の組成の培地
5Lに2%v/v の割合で移し、25℃で通気攪拌方式( 回
転数100rpm,/通気量1L/min)により培養をおこなっ
た。
[Example] An Alteromonas sp.kk10203C strain is used as an inoculum. Seed medium with the composition of peptone 5 g / L, yeast extract 1 g / L, glucose 2 g / L, ferric phosphate 0.04 g / L, sodium acetate 0.01 g / L, purified water 250 ml, seawater 750 ml (before sterilization (pH 7.7) 100 ml was made into a 200 ml Erlenmeyer flask, the strain was inoculated, and shaken at 25 ° C for 48 hours.
(100 rpm) Culture was performed. The seed culture thus obtained was transferred at a rate of 2% v / v to 5 L of a medium having the same composition as the above in a 10 L culture tank, and aerated and agitated at 25 ° C. (rotation speed 100 rpm, / The culture was performed at an aeration rate of 1 L / min).

【0013】培養中、培地のpHはとくに制御しないで、
120 時間培養した。培養液を瀘別し菌体を磨砕後アセト
ン2Lを添加し攪拌し、沈澱物を濾別し、抽出液7Lを
得た。抽出液を濃縮して3Lとしポリスチレン系吸着剤
ダイヤイオンpH20(1L)のカラムに通塔して活性物質
を吸着させた。脱イオン水および30%メタノールで不純
物を溶出後メタノールで活性物質を溶出した。活性画分
を濃縮し、ベンゼンで抽出した。抽出液を硫酸ナトリウ
ムで脱水した後、濃縮した。これをさらにシリカゲルカ
ラム(ナカライテスク社製シリカゲル60) を用い、ヘキ
サン: アセトン=8:2で展開した。溶出された画分A
を濃縮すると黄色の濃縮液2mlが得られた。画分Aは高
速液体クロマトグラフィー(ナカライテスク社製コスモ
シル5SL、内径8mm長さ250mm、ヘキサン:アセトン=
8:2、流速1.2ml/分)で精製した。溶出された画分B
は濃縮しゼアキサンチン8mgを得た。このようにして得
られたゼアキサンチンは、水素核NMR:可視光吸光分
析、質量分析において、公知のものと一致した。
During the culture, the pH of the medium is not particularly controlled,
Cultured for 120 hours. After the culture solution was filtered and the cells were ground, 2 L of acetone was added and stirred, and the precipitate was filtered off to obtain 7 L of extract. The extract was concentrated to 3 L and passed through a column of polystyrene adsorbent Diaion pH 20 (1 L) to adsorb the active substance. The active substance was eluted with methanol after eluting impurities with deionized water and 30% methanol. The active fraction was concentrated and extracted with benzene. The extract was dehydrated with sodium sulfate and then concentrated. This was further developed with hexane: acetone = 8: 2 using a silica gel column (silica gel 60 manufactured by Nacalai Tesque). Fraction A eluted
Was concentrated to give 2 ml of a yellow concentrate. Fraction A is high performance liquid chromatography (Nacalai Tesque Cosmosil 5SL, inner diameter 8 mm length 250 mm, hexane: acetone =
8: 2, flow rate 1.2 ml / min). Fraction B eluted
Was concentrated to obtain 8 mg of zeaxanthin. The zeaxanthin thus obtained was in agreement with a known one in hydrogen nucleus NMR: visible light absorption spectrometry, mass spectrometry.

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成3年9月24日[Submission date] September 24, 1991

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0013[Correction target item name] 0013

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0013】培養中、培地のpHはとくに制御しないで、
120 時間培養した。培養液を瀘別し菌体を磨砕後アセト
ン2Lを添加し攪拌し、沈澱物を濾別し、抽出液2Lを
得た。抽出液を濃縮して100 mlとしポリスチレン系吸着
剤ダイヤイオンpH20(1L)のカラムに通塔して活性物
質を吸着させた。脱イオン水および30%メタノールで不
純物を溶出後メタノールで活性物質を溶出した。活性画
分を濃縮し、ベンゼンで抽出した。抽出液を硫酸ナトリ
ウムで脱水した後、濃縮した。これをさらにシリカゲル
カラム(ナカライテスク社製シリカゲル60) を用い、ヘ
キサン: アセトン=8:2で展開した。溶出された画分
Aを濃縮すると黄色の濃縮液2mlが得られた。画分Aは
高速液体クロマトグラフィー(ナカライテスク社製コス
モシル5SL、内径8mm長さ250mm、ヘキサン:アセトン
=8:2、流速1.2 ml/分)で精製した。溶出された画
分Bは濃縮しゼアキサンチン8mgを得た。このようにし
て得られたゼアキサンチンは、水素核NMR:可視光吸
光分析、質量分析において、公知のものと一致した。
During the culture, the pH of the medium is not particularly controlled,
Cultured for 120 hours. After the culture solution was filtered and the bacterial cells were ground, 2 L of acetone was added and stirred, and the precipitate was filtered off to obtain 2 L of extract. The extract was concentrated to 100 ml and passed through a column of polystyrene adsorbent Diaion pH 20 (1 L) to adsorb the active substance. The active substance was eluted with methanol after eluting impurities with deionized water and 30% methanol. The active fraction was concentrated and extracted with benzene. The extract was dehydrated with sodium sulfate and then concentrated. This was further developed with hexane: acetone = 8: 2 using a silica gel column (silica gel 60 manufactured by Nacalai Tesque). The eluted fraction A was concentrated to obtain 2 ml of a yellow concentrated liquid. Fraction A was purified by high performance liquid chromatography (Cosmosil 5SL manufactured by Nacalai Tesque, Inc., inner diameter 8 mm, length 250 mm, hexane: acetone = 8: 2, flow rate 1.2 ml / min). The eluted fraction B was concentrated to obtain 8 mg of zeaxanthin. The zeaxanthin thus obtained was in agreement with a known one in hydrogen nucleus NMR: visible light absorption spectrometry, mass spectrometry.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 アルテロモナス属に属しゼアキサンチン
を生産する能力を有する微生物を培地に培養し、培養物
からゼアキサンチンを採取することを特徴とするゼアキ
サンチンの製造法。
1. A method for producing zeaxanthin, which comprises culturing in a medium a microorganism belonging to the genus Alteromonas and having the ability to produce zeaxanthin, and collecting zeaxanthin from the culture.
【請求項2】 アルテロモナス属に属する微生物がアル
テロモナス・sp微工研菌寄第12434号である請求項1記
載のゼアキサンチンの製造法。
2. The method for producing zeaxanthin according to claim 1, wherein the microorganism belonging to the genus Alteromonas is Alteromonas sp.
JP21245491A 1991-08-23 1991-08-23 Method for producing zeaxanthin Expired - Fee Related JP3007453B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21245491A JP3007453B2 (en) 1991-08-23 1991-08-23 Method for producing zeaxanthin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21245491A JP3007453B2 (en) 1991-08-23 1991-08-23 Method for producing zeaxanthin

Publications (2)

Publication Number Publication Date
JPH0549497A true JPH0549497A (en) 1993-03-02
JP3007453B2 JP3007453B2 (en) 2000-02-07

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ID=16622894

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21245491A Expired - Fee Related JP3007453B2 (en) 1991-08-23 1991-08-23 Method for producing zeaxanthin

Country Status (1)

Country Link
JP (1) JP3007453B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011122616A1 (en) 2010-03-30 2011-10-06 Jx日鉱日石エネルギー株式会社 Method of manufacturing zeaxanthin by fermentation
WO2012114998A1 (en) 2011-02-23 2012-08-30 Jx日鉱日石エネルギー株式会社 Zeaxanthin-enriched poultry egg

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011122616A1 (en) 2010-03-30 2011-10-06 Jx日鉱日石エネルギー株式会社 Method of manufacturing zeaxanthin by fermentation
WO2012114998A1 (en) 2011-02-23 2012-08-30 Jx日鉱日石エネルギー株式会社 Zeaxanthin-enriched poultry egg
KR20130124973A (en) 2011-02-23 2013-11-15 제이엑스 닛코닛세키 에네루기 가부시키가이샤 Zeaxanthin-enriched poultry egg
US9192588B2 (en) 2011-02-23 2015-11-24 Jx Nippon Oil & Energy Corporation Method for producing a zeaxanthin-enriched chicken egg

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