WO1992021764A1 - Procede pour produire de l'astaxanthine par fermentation - Google Patents
Procede pour produire de l'astaxanthine par fermentation Download PDFInfo
- Publication number
- WO1992021764A1 WO1992021764A1 PCT/JP1992/000722 JP9200722W WO9221764A1 WO 1992021764 A1 WO1992021764 A1 WO 1992021764A1 JP 9200722 W JP9200722 W JP 9200722W WO 9221764 A1 WO9221764 A1 WO 9221764A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- astaxanthin
- culture
- strain
- medium
- genus
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P23/00—Preparation of compounds containing a cyclohexene ring having an unsaturated side chain containing at least ten carbon atoms bound by conjugated double bonds, e.g. carotenes
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
- C12N1/14—Fungi; Culture media therefor
- C12N1/145—Fungal isolates
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
- C12R2001/00—Microorganisms ; Processes using microorganisms
- C12R2001/645—Fungi ; Processes using fungi
Definitions
- the present invention relates to a method for producing astaxanthin by a fermentation method.
- Asbestos xanthine is a type of natural carotenide and is useful as a color improver for cultured fish.
- a method for producing astaxanthin using a microorganism belonging to the genus Phafa includes, for example, a method using a microorganism belonging to the genus Phafa and having susceptibility to antimycin A [Applied and Environment].
- ronmen tal Mi crob iol ogy, 55, 116 (1989)] a method using microbes belonging to the genus Phafi, and having ionicon resistance [Journal,, 2944 (1990)].
- a method using Rhodochyma ATCC24202 Japanese Patent Publication No.
- 63-61907 is a method in which a microorganism belonging to the genus Fafa is treated with ethyl methansulfonate, UV irradiation or N-methyl-N'-nitro-N-2-nitrosogosa.
- Method using mutant strain treated with gin Japanese Patent Application Laid-open No.
- Hei 2-504101 (W088 / 08025) Method using a microorganism belonging to the genus Phaffa and having resistance to geraniol] Gazette (EP 427405)], belonging to the genus Quality (antimycin, tunicamycin, varnish), cytochrome B inhibitor (antimycin, 2-n-heptyl-4-hydroxy-quinolin-N-oxide) or terdinoid synthesis pathway
- a method using a microorganism having resistance to an inhibitor has been known (Japanese Patent Application Laid-Open No. 4-501053 (W090 / 01552)).
- a microorganism which belongs to the genus Paffa, is resistant to at least one of citronellol, primaquine and hydroxydiphenyl, and has an ability to produce astaxanthin is cultured in a medium. By collecting astaxanthin from It can be manufactured economically and efficiently.
- the present invention relates to a culture, cell or treated cell of a microorganism belonging to the genus Phaffa, which is resistant to at least one of citronellol, primaquine and hydroxydiphenyl, and has the ability to produce stastaxanthin. provide.
- Examples of the treated bacterial cells in the present invention include mechanically milled bacterial cells, ultrasonically treated substances, solvent-treated substances, enzyme-treated substances, surfactant-treated substances, and dried substances.
- resistance to citronellol, primaquine or hydroxydiphenyl means that it can grow on citronellol 220 i / m primaquine 3.9 g / l or hydroxydiphenyl.
- Microorganisms used in the present invention belong to the genus Puffa, and include at least citronellol, primaquine, and hydroxyphenyl.
- any type that is resistant to the species and has the ability to produce astaxanthin is used.
- These strains can be used to mutate asphaxanthin-producing bacteria of the genus Phaffa by conventional mutagenesis methods (eg, irradiation with ultraviolet light, treatment with a mutagenic agent (N-methyl-N'-two-row N-nitrosogazine), etc.). After allowing the cells to grow, they can be obtained as bacteria growing on a medium containing citronellol, primaquine or hydroxydifunil. Examples of such microorganisms include Phaf fia
- rhodozyma such as, for example, Huffy's mouth H-8264 (hereinafter referred to as strain H-8264), H-8434 (hereinafter referred to as strain H-8434), and H-8435 (hereinafter referred to as H -8435).
- the mutant strains (H-8264, H-8434 and H-8435 strains) and the parent strain (ATCC24202 strain) were spread on a minimal medium agar plate containing the additives shown in Tables 1 to 3 at 22 ° C. Cultured. The results are shown in Tables 1-3.
- the above three strains are based on the Butavest Treaty, the H-8264 strain is dated May 18, 1991, and the H-8434 and H-8435 strains are dated March 13, 1992. They have been deposited internationally with the Research Institute of Microbial Industry and Technology, and have been assigned FERM BP-3404, 3800 and 3801, respectively.
- the medium used in the present invention may be a synthetic medium or a natural medium as long as the medium contains a carbon source, a nitrogen source, an inorganic salt, a growth factor, and the like.
- a carbon source glucose, fructose, sucrose, molasses, and the like are used.
- nitrogen source ammonia, ammonium sulfate, peptone, yeast extract, corn stuplica and the like are used.
- the inorganic salt there are used mono-potassium phosphate, di-calcium phosphate, magnesium phosphate, magnesium sulfate, ferrous sulfate, manganese sulfate, calcium chloride and the like.
- growth factors vitamins, amino acids, nucleic acid-related substances and the like are used.
- the culture is performed by batch culture, continuous culture, etc., at a temperature of 15 to 35 ° C., preferably 20 to 25, at a pH of 3 to 8, preferably 4 to 6, and usually completed in 2 to 7 days.
- the pH of the medium is adjusted with calcium carbonate, inorganic or organic acids, alkaline solutions, ammonia, pH buffers (eg, lithium hydrogen phthalate), and the like.
- the cells are separated and This is dried and pulverized to obtain dried cells, or the cells are separated from the culture solution, crushed, and then astaxanthin is solvent-extracted from the crushed cells and processed by silica gel chromatography. .
- the staxanthin obtained by the present invention, the culture of the microorganism, the cells, the treated cells, and the like are used for fish and crustaceans.
- the H-8264 strain, the H-8434 strain, and the H-8435 strain were each inoculated into 8 ml of a seed medium having the following composition in a test tube, and then cultured at 22 ° C for 3 days.
- Seed medium composition glucose lOg / l, yeast extract 3g // l, butane 5g / 1, meat extract 3gZl (adjusted at pH 5.0, K0H, pressurized steam sterilization at 120 ° C for 20 minutes)
- 3 ml of the obtained three seed cultures were inoculated into 30 ml of a production medium having the following composition in a 250 ml Erlenmeyer flask and cultured at 22 ° C for 4 days.
- Production medium composition glucose 30 g / 1, sulfate Anmoniumu 2 GZL, yeast extract 2g / l, KH 2 P0 4 lg / and, gS0 4 - 7H 2 0 0.5 g / l, CaC • 2H 2 0 0.1 g / 1, Hydrogen phthalate power room 20.4g Zl (adjusted at pH5.0, K0H, steam sterilization at 120 ° C for 20 minutes)
- the amounts of xanthine produced in cultures of the strains H-8264, H-8434, and H-8435 were 5.8 mg / l, 5.5 ⁇ ⁇ , and TragZl, respectively.
- the H-8264 strain was inoculated into 300 ml of the seed medium described in Example 1 in a 2-liter Erlenmeyer flask, and then cultured at 22 ° C for 3 days. From the production medium described in Example 1 in a 5-liter After inoculating 3 liters of medium excluding the hydrogen-powered rim, the cells were cultured at 22 ° C for 48 hours (rotational speed 600 rpm, aeration 3 liters Zmin). The pH during the culture was adjusted to 5 with ammonia water. As a result, the amount of astaxanthin produced in the culture solution was 17. lmgZl.
- the H-8434 strain was inoculated into 300 ml of the seed medium described in Example 1 in a 2-liter Erlenmeyer flask and cultured at 22 ° C for 3 days. 80 ml of the resulting seed culture was inoculated into 720 ml of a culture medium obtained by removing hydrogen phthalate from the production medium described in Example 1 in a 2-liter culture tank, and cultured at 22 ° C for 48 hours (rotation). At several 900 rpm, the air flow rate was 0.8 liter / min). The pH during the culture was adjusted to 5 with aqueous ammonia. As a result, the amount of astaxanthin produced in the culture solution was 16.3 ⁇ 3 ⁇ 4.
- the cells were separated from this culture solution, the cells were dried with a spray dryer to obtain 37 g of dried cells containing 14 mg of astaxanthin.
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Health & Medical Sciences (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Microbiology (AREA)
- Medicinal Chemistry (AREA)
- Mycology (AREA)
- Tropical Medicine & Parasitology (AREA)
- Biomedical Technology (AREA)
- Virology (AREA)
- Botany (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP04511328A JP3117714B2 (ja) | 1991-06-06 | 1992-06-04 | 発酵法によるアスタキサンチンの製造法 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3/134750 | 1991-06-06 | ||
JP13475091 | 1991-06-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1992021764A1 true WO1992021764A1 (fr) | 1992-12-10 |
Family
ID=15135701
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP1992/000722 WO1992021764A1 (fr) | 1991-06-06 | 1992-06-04 | Procede pour produire de l'astaxanthine par fermentation |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0543023A4 (ja) |
JP (1) | JP3117714B2 (ja) |
CA (1) | CA2088667A1 (ja) |
WO (1) | WO1992021764A1 (ja) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005085465A1 (ja) * | 2004-03-04 | 2005-09-15 | Suntory Limited | アスタキサンチン含有脂質の製造方法 |
US7851199B2 (en) | 2005-03-18 | 2010-12-14 | Microbia, Inc. | Production of carotenoids in oleaginous yeast and fungi |
US8221997B2 (en) | 2005-10-28 | 2012-07-17 | Tosoh Corporation | Microorganism and method for producing carotenoid using the same |
US8691555B2 (en) | 2006-09-28 | 2014-04-08 | Dsm Ip Assests B.V. | Production of carotenoids in oleaginous yeast and fungi |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8097761B2 (en) | 2006-03-28 | 2012-01-17 | Jx Nippon Oil & Energy Corporation | Process for production of carotenoid |
JP4969370B2 (ja) | 2007-08-29 | 2012-07-04 | Jx日鉱日石エネルギー株式会社 | カロテノイドの製造方法 |
EP3065568B1 (en) | 2013-11-07 | 2019-12-25 | DSM IP Assets B.V. | Process for the purification of astaxanthin |
WO2015067709A1 (en) | 2013-11-07 | 2015-05-14 | Dsm Ip Assets B.V. | Process for the purification of astaxanthin |
CN105705040B (zh) | 2013-11-07 | 2018-12-11 | 帝斯曼知识产权资产管理有限公司 | 纯化虾青素的方法 |
WO2015067711A1 (en) | 2013-11-07 | 2015-05-14 | Dsm Ip Assets B.V. | Process for the purification of astaxanthin |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1988008025A1 (en) | 1987-04-15 | 1988-10-20 | Danisco Bioteknologi A/S | Astaxanthin-producing yeast cells, methods for their preparation and their use |
JPS6361907B2 (ja) | 1981-06-12 | 1988-11-30 | ||
WO1990001552A1 (en) | 1988-08-08 | 1990-02-22 | Igene Biotechnology, Inc. | Process for in vivo production of astaxanthin and phaffia rhodozyma yeast of enhanced astaxanthin content |
WO1991002060A1 (en) * | 1989-07-28 | 1991-02-21 | Igene Biotechnology, Inc. | Processes for in vivo production of astaxanthin and phaffia rhodozyma yeast of enhanced astaxanthin content |
EP0427405A1 (en) | 1989-10-27 | 1991-05-15 | Enzymatix Ltd. | Yeasts and their use in astaxanthin production |
-
1992
- 1992-06-04 WO PCT/JP1992/000722 patent/WO1992021764A1/ja not_active Application Discontinuation
- 1992-06-04 JP JP04511328A patent/JP3117714B2/ja not_active Expired - Fee Related
- 1992-06-04 EP EP19920911402 patent/EP0543023A4/en not_active Withdrawn
- 1992-06-04 CA CA002088667A patent/CA2088667A1/en not_active Abandoned
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6361907B2 (ja) | 1981-06-12 | 1988-11-30 | ||
WO1988008025A1 (en) | 1987-04-15 | 1988-10-20 | Danisco Bioteknologi A/S | Astaxanthin-producing yeast cells, methods for their preparation and their use |
JPH02504101A (ja) | 1987-04-15 | 1990-11-29 | ジスト―ブロカデス ナームロゼ フェンノートシャップ | アスタキサンチン生産性酵母細胞,その製造方法及びその使用 |
WO1990001552A1 (en) | 1988-08-08 | 1990-02-22 | Igene Biotechnology, Inc. | Process for in vivo production of astaxanthin and phaffia rhodozyma yeast of enhanced astaxanthin content |
JPH04501053A (ja) | 1988-08-08 | 1992-02-27 | アイジーン・バイオテクノロジイ・インコーポレイテッド | アスタキサンチンのイン・ビボ生産方法およびアスタキサンチン含量を増加させるファフィア・ロドジマ酵母 |
WO1991002060A1 (en) * | 1989-07-28 | 1991-02-21 | Igene Biotechnology, Inc. | Processes for in vivo production of astaxanthin and phaffia rhodozyma yeast of enhanced astaxanthin content |
EP0427405A1 (en) | 1989-10-27 | 1991-05-15 | Enzymatix Ltd. | Yeasts and their use in astaxanthin production |
JPH03206880A (ja) | 1989-10-27 | 1991-09-10 | Enzymatix Ltd | 酵母およびアスタキサンチン生産におけるその使用 |
Non-Patent Citations (2)
Title |
---|
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, vol. 55, 1989, pages 116 |
See also references of EP0543023A4 * |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005085465A1 (ja) * | 2004-03-04 | 2005-09-15 | Suntory Limited | アスタキサンチン含有脂質の製造方法 |
US7851199B2 (en) | 2005-03-18 | 2010-12-14 | Microbia, Inc. | Production of carotenoids in oleaginous yeast and fungi |
US9909130B2 (en) | 2005-03-18 | 2018-03-06 | Dsm Ip Assets B.V. | Production of carotenoids in oleaginous yeast and fungi |
US8221997B2 (en) | 2005-10-28 | 2012-07-17 | Tosoh Corporation | Microorganism and method for producing carotenoid using the same |
US8691555B2 (en) | 2006-09-28 | 2014-04-08 | Dsm Ip Assests B.V. | Production of carotenoids in oleaginous yeast and fungi |
US9297031B2 (en) | 2006-09-28 | 2016-03-29 | Dsm Ip Assets B.V. | Production of carotenoids in oleaginous yeast and fungi |
Also Published As
Publication number | Publication date |
---|---|
EP0543023A1 (en) | 1993-05-26 |
EP0543023A4 (en) | 1993-12-01 |
JP3117714B2 (ja) | 2000-12-18 |
CA2088667A1 (en) | 1992-12-07 |
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