JPH0521556B2 - - Google Patents

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Publication number
JPH0521556B2
JPH0521556B2 JP1096754A JP9675489A JPH0521556B2 JP H0521556 B2 JPH0521556 B2 JP H0521556B2 JP 1096754 A JP1096754 A JP 1096754A JP 9675489 A JP9675489 A JP 9675489A JP H0521556 B2 JPH0521556 B2 JP H0521556B2
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JP
Japan
Prior art keywords
strain
astaxanthin
culture
rhodozyma
carotenoid
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 - Lifetime
Application number
JP1096754A
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Japanese (ja)
Other versions
JPH02276584A (en
Inventor
Osamu Miura
Toshiko Yoshimi
Kunihiko Minato
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.)
OOSAKA KAGAKU GOKIN KK
Original Assignee
OOSAKA KAGAKU GOKIN KK
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Application filed by OOSAKA KAGAKU GOKIN KK filed Critical OOSAKA KAGAKU GOKIN KK
Priority to JP1096754A priority Critical patent/JPH02276584A/en
Publication of JPH02276584A publication Critical patent/JPH02276584A/en
Publication of JPH0521556B2 publication Critical patent/JPH0521556B2/ja
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Description

【発明の詳細な説明】[Detailed description of the invention] 【発明の目的】[Purpose of the invention]

[産業上の利用分野] 本発明は、魚介類養殖用餌料添加剤等として有
用なカロチノイド色素を新規な酵母菌株の培養に
より生産する方法に関する。 [従来の技術] (1) 背景 下式で示されるカロチノイド、アスタキサンチ
ン(Astaxanthin)は、甲殻類の殻や卵、サケの
肉、キンメダイの表皮など、動物界に極めて広く
分布しているソオカロチノイドの一種であつて、
β−カロチンが二分子縮合した化学構造を有す
る。 このものは、従来フアツフイア・ロドザイマの
ような、本カロチノイドを含む赤色酵母の菌体を
養殖マスの発色性餌料として、近年では養殖マダ
イの発色性餌料として、南極オキアミなどに代替
させる用途が検討されている(特公昭83−61907
号参照)。 (2) 従来技術の問題点 しかし、フアツフイア・ロドザイマのタイプ・
カルチユアであるATCC24202株は勿論、類似の
同種菌株、IFO10129及びATCC24230両株の色素
生産量は比較的低いから、オキアミなどの安価な
蛋白性天然資源と対抗できるだけの工業的基礎を
確立するには問題がある。 [発明が解決しようとする課題] そこで本発明が解決しようとする課題は、優れ
たアスタキサンチン産生性菌株を利用することに
よつて、オキアミと対抗可能な、アスタキサンチ
ンの経済的な発酵的生産法を開発することであ
る。
[Industrial Application Field] The present invention relates to a method for producing carotenoid pigments useful as feed additives for fish and shellfish culture by culturing a novel yeast strain. [Prior Art] (1) Background Astaxanthin, a carotenoid represented by the following formula, is a carotenoid that is extremely widely distributed in the animal kingdom, such as in crustacean shells and eggs, salmon meat, and the skin of goldenfin sea bream. It is a kind of
It has a chemical structure in which two molecules of β-carotene are condensed. This product has traditionally been used as a color-producing feed for farmed trout using the cells of red yeast containing this carotenoid, such as Huatuhuia rhodozyma, and in recent years, as a color-producing feed for farmed red sea bream, applications have been considered to replace Antarctic krill, etc. (Tokuko Showa 83-61907)
(see issue). (2) Problems with the conventional technology However, the type of Huathuia rhodozyma
Since the pigment production of the cultivar ATCC24202 strain as well as the similar homologous strains IFO10129 and ATCC24230 is relatively low, it is difficult to establish an industrial basis that can compete with cheap proteinaceous natural resources such as krill. There is. [Problem to be solved by the invention] Therefore, the problem to be solved by the present invention is to develop an economical fermentative production method for astaxanthin that can compete with krill by using an excellent astaxanthin-producing bacterial strain. It is to develop.

【発明の構成】[Structure of the invention]

[課題を解決するための手段] (1) 経過 本発明者らは、アスタキサンチン産生性の高い
菌株を取得する目的で、多数のブナ目(Order
Fa−gales)植物の樹液よりアスタキサンチン産
生菌株の検索を試みたところ、遂に既知のフアツ
フイア・ロドザイマ(Phaffia rhodozyma)に
属する諸菌株と、色素産生能、発育温度適性及び
耐浸透圧性の点で判然区別しうる一菌株OCMー
1株を分離、取得した。本発明は、この知見に基
づくものである。 (2) 概要 以上の知見に基づき、本発明は、赤色酵母フア
ツフイア・ロドザイマ(Phaffia rhodozyma)
OCM−1株を培養し、得られた菌体からアスタ
キサンチン又はそれを主とするカロチノイド色素
を採取することを特徴とするカロチノイド色素の
製造法を要旨とするものである。 以下、発明を構成する諸要素等につき項分けし
て説明する。 (3) 新菌株OCM−1株の菌学的記載 形態学的性質・培養的性質 YM液体培地培養(20℃、1週間培養後観
察): (a) 形態:楕円形、時に鎖状に数個連結。 (b) 大きさ:5.0〜7.5×5.0〜10μm。 YM寒天培地で20℃、3週間培養、生成した巨
大コロニーは、半径0.7〜0.9cmφ、オレンジに着
色、コロニーの隆起は扁平で、周縁は全縁〜波状
又はカール状で、輝光である。表面は平滑で、バ
ター質である。 (c) 増殖方式:多極出芽、YM液体培地の表面
に皮膜形成。 子嚢胞子形成(酢酸ソーダ培地、20℃、3週
間培養):認められず。但し、偽菌糸と厚膜胞
子は形成される。 射出胞子の形成(麦芽汁寒天培地及びYM寒
天培地で、20℃、3週間培養):認められず。 生理的性質 生育温度:0〜25℃ 耐浸透圧性:塩化ナトリウム 3%、グルコ
ース 40%。 硝酸塩同化能:(−)。 脂質の分解性:(−)。 尿素の分解性:(+)。 ゼラチン液化性:(+)。 カロチノイドの生成:(+)。 有機酸の生成:(+)。 澱粉様物質の生成:(+)。 ビタミン要求性:(+)(ビオチン及びパント
テン酸カルシウムを要求)。 糖の発酵性:グルコース(+)、ガラクトー
ス(−)、シユクロース(+)、マルトース
(+)、ラクトース(−)、ラフイノース(+)。 糖の資化性:マンニトール(+)、トレハロ
ース(+)、コハク酸塩(+)、グルコース
(+)、L−アラビノース(+)、L−タムノー
ス(−)、ガラクトース(−),エリスリトール
(−)、セロビオース(+)、クエン酸塩(−)、
シユクロース(+)、D−キシロース(+)、D
−リボース(−)、ラフイノース(+)、イノシ
トール(−)、可溶性澱粉(+)、マルトース
(+)、ラクトース(−)。 カロチノイド生産性 本寄託菌株は、糖質を基質として20℃程度の低
温で、多量のアスタキサンチンを主とするカロチ
ノイド色素(以下単に「カロチノイド色素と略
す)を生産する。 既知他菌株との対比 以上の性質を標準株ATCC24202及び
ATCC24230と対比した結果は下表−1の通りで
ある。
[Means for solving the problem] (1) Progress The present inventors have developed a large number of Fagales (Order
Attempting to search for astaxanthin-producing bacterial strains from the sap of Phaffia rhodozyma plants, we finally found that they were clearly distinguishable from known strains belonging to Phaffia rhodozyma in terms of pigment production ability, growth temperature suitability, and osmotic pressure resistance. A bacterial strain OCM-1 was isolated and obtained. The present invention is based on this knowledge. (2) Overview Based on the above knowledge, the present invention is directed to the use of the red yeast Phaffia rhodozyma.
The gist of this invention is a method for producing carotenoid pigments, which is characterized by culturing OCM-1 strain and collecting astaxanthin or carotenoid pigments mainly containing it from the resulting bacterial cells. Hereinafter, various elements constituting the invention will be explained in terms of sections. (3) Mycological description of the new strain OCM-1 Morphological properties/Cultural properties YM liquid medium culture (observation after 1 week of culture at 20°C): (a) Morphology: Oval, sometimes chain-like in number Individual concatenation. (b) Size: 5.0 to 7.5 x 5.0 to 10 μm. The giant colonies produced by culturing on YM agar medium at 20°C for 3 weeks have a radius of 0.7 to 0.9 cm, are colored orange, have flat ridges, and have an entire periphery to wavy or curled edges, and are bright. The surface is smooth and buttery. (c) Propagation method: multipolar budding, film formation on the surface of YM liquid medium. Ascospore formation (cultured in sodium acetate medium, 20°C, 3 weeks): Not observed. However, pseudohyphae and chlamydospores are formed. Formation of extruded spores (cultivated on wort agar medium and YM agar medium at 20°C for 3 weeks): Not observed. Physiological properties Growth temperature: 0-25°C Osmotic pressure resistance: Sodium chloride 3%, glucose 40%. Nitrate assimilation capacity: (-). Lipid degradability: (-). Degradability of urea: (+). Gelatin liquefaction: (+). Carotenoid production: (+). Generation of organic acids: (+). Formation of starch-like substances: (+). Vitamin requirement: (+) (requires biotin and calcium pantothenate). Sugar fermentability: glucose (+), galactose (-), sucrose (+), maltose (+), lactose (-), raffinose (+). Sugar assimilation: mannitol (+), trehalose (+), succinate (+), glucose (+), L-arabinose (+), L-thamnose (-), galactose (-), erythritol (-) ), cellobiose (+), citrate (-),
Sucrose (+), D-xylose (+), D
-ribose (-), raffinose (+), inositol (-), soluble starch (+), maltose (+), lactose (-). Carotenoid Productivity This deposited strain produces large amounts of carotenoid pigments, mainly astaxanthin (hereinafter simply referred to as "carotenoid pigments"), using carbohydrates as a substrate at a low temperature of around 20°C.Comparison with other known bacterial strains Characteristics of standard strain ATCC24202 and
The results compared with ATCC24230 are shown in Table 1 below.

【表】【table】

【表】 ** 発明者の菌学的研究による。
カロチノイド生産性 本願発明菌株は、フアツフイア・ロドザイマに
属する既知菌株と比べて、特段に高いカロチノイ
ド産生性を有する。下表−2は、グルコース−ペ
プトン−酵母エキス培地による各菌株のアスタキ
サンチン産生量を対比した結果である。
[Table] **Based on mycological research by the inventor.
Carotenoid Productivity The strain of the present invention has particularly high carotenoid productivity compared to known strains belonging to Futufia rhodozyma. Table 2 below shows the results of comparing the amount of astaxanthin produced by each strain in the glucose-peptone-yeast extract medium.

【表】 即ち、本発明菌株によれば、既知菌株中最良と
思われるATCC24230株に比較して5割以上の好
収率で、アスタキサンチンを生産させることがで
きる。 分類学上の位置 上表−1が示すごとく、本発明に係る新菌株
OCM−1株は、形態的にコロニーの大きさ、色
調及び表面状態等においてタイプカルチユア
ATCC24202及びATCC24230と多少の差異はある
が、全体として株の異同を論じる程の明確な差異
は認められない(既知の他の7菌株についても同
じ。)。 しかし本株は、全ての既知株に比べてカロチノ
イド生成能が格段に優れていると共に、耐浸透圧
性及び生育温度が顕著に低い点で、既知株の変異
株とはなし難いので、これをフアツフイア・ロド
ザイマ(Phaffia rhodozyma)に属する認め、
これにフアツフイア・ロドザイマ OCM−1な
る株名を付して工業技術院微生物工業研究所
(FERM)へFERM P−10653として寄託した。 (4) 色素の製造 本発明によりアスタキサンチン系色素を製造す
るには、従来の同系色素の発酵的生産法の場合と
同様に、フアツフイア・ロドザイマ OCM−1
株の純粋培養物(イノキユラム)を適当なC/N
比及びPHに調整された培地中に接種し、25℃以下
の低温下に好気的に発酵させ、ラグフエーズに到
達してとき菌体を採取し、これを低温で乾燥後、
必要に応じ破砕するか又は所望により更にクロロ
ホルム、ピリジン等の疎水性溶媒を用いて色素を
抽出する。この際、通常は、培養の規模に応じ、
小規模の培養から次第に大規模の培養に移行する
段階的な培養方法が採られる。 培地の炭素源としては、グルコース、シユクロ
ース、フルクトース、マルトース等の易資化性糖
類又は澱粉の酵素的又は化学的分解物等が適宜利
用されるが、工業的には廃糖蜜、澱粉滓分解物、
ダイズホエイなどの安価な炭素源の使用がより好
ましい。 窒素源としては、尿素、硫安、炭酸アンモニウ
ム等が好適に利用される。かつK,P及びMg源
として、燐酸カリウム、燐酸一水素カリウム、燐
酸二水素カリウム、硫酸カリウム、硫酸マグネシ
ウムなどの水溶性塩類の添加が望ましい。 更に微量栄養源として、ペプトン、味液R、コ
ーンステイープ、胚芽抽出液、麦芽エキス、酵母
エキスなどの添加が望ましい。これらの天然物
は、本菌株の生育に必要なビタミン類の他、核
酸、ホスフアチド、Fe、B、Cu、Mn、Cuなど
の微量栄養源を豊富に含有する。 [作用] 本発明に係る赤色酵母フアツフイア・ロドザイ
マ(Phaffia rhodozyma)OCM−1株は、既知
のロドザイマ種に属する諸株に比較して格段に優
れたアスタキサンチン産生能力を備えているの
で、本株の培養により、魚類の餌料添加剤として
有用な安全性の高いアスタキサンチンを、工業的
有利に、かつ安定して市場に供給することができ
る。 [実施例] 以下、実施例により発明実施の態様を説明する
が、例示は単に説明用のもので、発明思想の制限
又は限定を意味するものではない。 実施例 1 グルコース10g、ペプトン10g、酵母エキス5g、
燐酸二水素カリウム5g、硫酸マグネシウム七水
塩)2g及び水1からなる培地100mlを500ml容
のフラスコに分注し、121℃、15分間滅菌した。 以上の培地に別に培養したフアツフイア・ロド
ザイマ OCM−1株のシードを接種し、毎分200
振動の回転式振盪培養機で20℃で3日間培養し前
培養液を得た。 この前培養液0.5mmlを上と同組成の培地1に
接種し、同様に5日間本培養した。 終了後、3000r.p.m.で5分間遠心して菌体を分
離し、湿菌体1.01gを得た。 実施例 2 グルコース10g、ペプトン5g、酵母エキス3g、
麦芽エキス3g及び水1からなる培地100mlを
500ml容のフラスコに分注し、121℃、15分間滅菌
した。 その後、前例と同様に前培養、本培養及び菌体
分離を行い、湿潤菌体0.51gを得た。前例との対
比から、本菌はK、P及びMgを多量要求するこ
とが推定される。 実施例 3 上記実施例1で得た菌体に水を加えて菌体を懸
濁させ、液化CO2で冷却しながら径0.45m/mの
ガラスビーズを添加したガラスビーズセルホモジ
ナイザーで菌体を破砕後、20倍量のアセトンで抽
出した。 上の抽出液を減圧下に濃縮後、石油エーテルに
転溶させ、転溶液を無水硫酸ナトリウムを用いて
乾燥後、1cmのセルを用い、λ=474nmにおける
吸光度を求め、上掲の式により色素産生量
(A474)を産出した。含量0.678%。 実施例 4 上述実施例1及び実施例2で得たカロチノイド
の組成を高速液体クロマトグラフイー(HPLC、
機器:島津(株)製LC−6A、カラム:Lichrosorb
SI−100、移動相メタノール:イソプロピルエー
テル=1:9)で分析し、添付第1図に示すスペ
クトルを得た。 対照として、ATCC24230株を用いて実施例1
と同様に培養して得た菌体からの色素抽出物を同
様にHPLCで分析したところ、添付第2図に示す
結果が得られた。本例の場合、ピーク←(図中記
入)に相当するアスタキサンチンの比率は約75%
であつたが、対照株からの色素中のアスタキサン
チンの量比は約28%であつた。従つて、本発明に
係るフアツフイア・ロドザイマ(Phaffia
rhodozyma)OCM−1株は、アスタキサンチン
の工業的生産用菌株として、画然たる優位性を有
すべきことが窺知される。 実施例 5 サケ肉から抽出、精製したアスタキサンチンの
標品と、上記実施例3で得た色素の精製品の
HPLCで比較した。得られたスペクトラムを第3
図及び第4図に示す。両者ともに少量の不純物を
組むが、夫々のスペクトラムのパターン及びリテ
ンシヨンタイムは殆ど一致しており、このことか
ら本発明による色素がアスタキサンチンに相違な
いとが確認される。
[Table] That is, according to the strain of the present invention, astaxanthin can be produced at a yield higher than 50% compared to the ATCC24230 strain, which is considered to be the best among known strains. Taxonomic position As shown in Table 1 above, the new strain according to the present invention
The OCM-1 strain is morphologically distinct from the type culture in terms of colony size, color tone, and surface condition.
Although there are some differences from ATCC24202 and ATCC24230, there are no clear differences to the extent that the strains are different as a whole (the same is true for the other seven known strains). However, this strain has much superior carotenoid production ability compared to all known strains, and has significantly lower osmotic pressure resistance and growth temperature, making it difficult to treat it as a mutant of known strains. Recognized as belonging to Phaffia rhodozyma,
This strain was given the strain name Huatuphia rhodozyma OCM-1 and deposited as FERM P-10653 at the National Institute of Microbiology (FERM), Agency of Industrial Science and Technology. (4) Production of pigment In order to produce astaxanthin pigment according to the present invention, as in the case of the conventional fermentative production method of similar pigments, Fuatufia rhodozyma OCM-1
A pure culture of the strain (Inoculum) was grown at an appropriate C/N.
It is inoculated into a medium whose ratio and pH are adjusted, fermented aerobically at a low temperature of 25°C or less, and when it reaches lag phase, the bacterial cells are collected, and after drying at a low temperature,
If necessary, the mixture is crushed, or if desired, the pigment is further extracted using a hydrophobic solvent such as chloroform or pyridine. At this time, depending on the scale of culture, usually
A stepwise culture method is adopted in which small-scale culture gradually moves to large-scale culture. Easily assimilated sugars such as glucose, sucrose, fructose, and maltose or enzymatic or chemical decomposition products of starch are appropriately used as carbon sources for the culture medium, but industrially, blackstrap molasses and decomposition products of starch lees are used. ,
The use of inexpensive carbon sources such as soy whey is more preferred. As the nitrogen source, urea, ammonium sulfate, ammonium carbonate, etc. are suitably used. Additionally, as K, P, and Mg sources, it is desirable to add water-soluble salts such as potassium phosphate, potassium monohydrogen phosphate, potassium dihydrogen phosphate, potassium sulfate, and magnesium sulfate. Furthermore, it is desirable to add peptone, Ajizu R , corn staple, germ extract, malt extract, yeast extract, etc. as a trace nutrient source. These natural products contain abundant micronutrient sources such as nucleic acids, phosphatides, Fe, B, Cu, Mn, and Cu in addition to the vitamins necessary for the growth of this strain. [Effect] The red yeast Phaffia rhodozyma (Phaffia rhodozyma) OCM-1 strain according to the present invention has a significantly superior ability to produce astaxanthin compared to known strains belonging to Rhodozyma species. By culturing, highly safe astaxanthin useful as a fish feed additive can be stably supplied to the market with industrial advantages. [Examples] Hereinafter, embodiments of the invention will be explained using examples, but the examples are merely for explanation and do not mean any restriction or limitation on the idea of the invention. Example 1 Glucose 10g, peptone 10g, yeast extract 5g,
100 ml of a medium consisting of 5 g of potassium dihydrogen phosphate, 2 g of magnesium sulfate heptahydrate, and 1 portion of water was dispensed into a 500 ml flask and sterilized at 121° C. for 15 minutes. Seeds of Huatuphia rhodozyma OCM-1 strain cultured separately were inoculated into the above medium, and
A preculture solution was obtained by culturing at 20°C for 3 days in a rotating shaking culture machine. 0.5 m ml of this preculture solution was inoculated into medium 1 having the same composition as above, and the main culture was similarly carried out for 5 days. After completion, the cells were separated by centrifugation at 3000 rpm for 5 minutes to obtain 1.01 g of wet cells. Example 2 Glucose 10g, peptone 5g, yeast extract 3g,
100 ml of medium consisting of 3 g of malt extract and 1 portion of water.
The mixture was dispensed into 500 ml flasks and sterilized at 121°C for 15 minutes. Thereafter, preculture, main culture, and bacterial cell isolation were performed in the same manner as in the previous example to obtain 0.51 g of wet bacterial cells. From comparison with the previous example, it is estimated that this bacterium requires large amounts of K, P, and Mg. Example 3 Water was added to the bacterial cells obtained in Example 1 to suspend the bacterial cells, and while cooling with liquefied CO 2 , the bacterial cells were homogenized using a glass bead cell homogenizer to which glass beads with a diameter of 0.45 m/m were added. After crushing, it was extracted with 20 times the amount of acetone. After concentrating the above extract under reduced pressure, it was transferred to petroleum ether, and after drying the resulting solution using anhydrous sodium sulfate, the absorbance at λ = 474 nm was determined using a 1 cm cell, and the dye was determined using the above formula. The production amount (A 474 ) was produced. Content 0.678%. Example 4 The composition of the carotenoids obtained in Example 1 and Example 2 above was analyzed by high performance liquid chromatography (HPLC).
Equipment: Shimadzu Corporation LC-6A, Column: Lichrosorb
Analysis was performed using SI-100, mobile phase methanol:isopropyl ether=1:9), and the spectrum shown in the attached FIG. 1 was obtained. Example 1 using ATCC24230 strain as a control
When the pigment extract from the bacterial cells obtained by culturing in the same manner as above was similarly analyzed by HPLC, the results shown in the attached Figure 2 were obtained. In this example, the ratio of astaxanthin corresponding to the peak ← (indicated in the figure) is approximately 75%.
However, the amount ratio of astaxanthin in the pigment from the control strain was approximately 28%. Therefore, Phaffia rhodozyma according to the present invention
rhodozyma) OCM-1 strain is clearly superior as a strain for industrial production of astaxanthin. Example 5 A sample of astaxanthin extracted and purified from salmon meat and a purified product of the pigment obtained in Example 3 above.
Comparison was made by HPLC. The obtained spectrum is
It is shown in FIG. Although both contain a small amount of impurities, their spectral patterns and retention times are almost the same, which confirms that the dye according to the present invention is astaxanthin.

【発明の効果】【Effect of the invention】

以上説明した通り、本発明は、優れたアスタキ
サンチン産生性菌株を利用してオキアミと対抗可
能なアスタキサンチンの経済的な発酵的生産法を
開発し得たことにより、魚類養殖その他の産業に
寄与しうる。
As explained above, the present invention can contribute to fish farming and other industries by developing an economical fermentative production method for astaxanthin that can compete with krill using an excellent astaxanthin-producing bacterial strain. .

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明菌株が産生した色素中のアス
タキサンチンの生産比率を示すHPLCスペクトラ
ム、第2図は、公知のATCC24230株が産生した
色素中のアスタキサンチンの生産比率を示す
HPLCスペクトラム、第3図は、サケの肉から抽
出したアスタキサンチンのHPLCスペクトラム、
第4図は、本発明菌株が産生した精製色素の
HPLCスペクトラムである。
Figure 1 shows the HPLC spectrum showing the production ratio of astaxanthin in the pigment produced by the strain of the present invention, and Figure 2 shows the production ratio of astaxanthin in the pigment produced by the known ATCC24230 strain.
HPLC spectrum, Figure 3 is the HPLC spectrum of astaxanthin extracted from salmon meat.
Figure 4 shows the purified pigment produced by the strain of the present invention.
This is an HPLC spectrum.

Claims (1)

【特許請求の範囲】[Claims] 1 アスタキサンチン生産能を有する赤色酵母フ
アツフイア・ロドザイマ(Phaffia rhodo−
zyma)OCM−1株を培養し、得られた菌体から
アスタキサンチン又はそれを主とするカロチノイ
ド色素を採取することを特徴とするカロチノイド
色素の製造法。
1 Red yeast Phaffia rhodozyma that has astaxanthin-producing ability
zyma) OCM-1 strain is cultured, and astaxanthin or a carotenoid pigment mainly containing astaxanthin is collected from the obtained bacterial cells.
JP1096754A 1989-04-17 1989-04-17 Production of carotenoid dyestuff Granted JPH02276584A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1096754A JPH02276584A (en) 1989-04-17 1989-04-17 Production of carotenoid dyestuff

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1096754A JPH02276584A (en) 1989-04-17 1989-04-17 Production of carotenoid dyestuff

Publications (2)

Publication Number Publication Date
JPH02276584A JPH02276584A (en) 1990-11-13
JPH0521556B2 true JPH0521556B2 (en) 1993-03-24

Family

ID=14173451

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1096754A Granted JPH02276584A (en) 1989-04-17 1989-04-17 Production of carotenoid dyestuff

Country Status (1)

Country Link
JP (1) JPH02276584A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07242621A (en) * 1994-03-02 1995-09-19 Nippon Oil Co Ltd Method for extracting carotenoid compound

Also Published As

Publication number Publication date
JPH02276584A (en) 1990-11-13

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