JPH06277075A - Yield increase of phycocyanin - Google Patents

Yield increase of phycocyanin

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Publication number
JPH06277075A
JPH06277075A JP5066653A JP6665393A JPH06277075A JP H06277075 A JPH06277075 A JP H06277075A JP 5066653 A JP5066653 A JP 5066653A JP 6665393 A JP6665393 A JP 6665393A JP H06277075 A JPH06277075 A JP H06277075A
Authority
JP
Japan
Prior art keywords
phycocyanin
medium
culture
increasing
concentration
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.)
Pending
Application number
JP5066653A
Other languages
Japanese (ja)
Inventor
Takahisa Miyazaki
貴央 宮崎
Masanori Asada
雅宣 浅田
Takehisa Ohashi
武久 大橋
Tadashi Matsunaga
是 松永
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry Co Ltd
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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP5066653A priority Critical patent/JPH06277075A/en
Publication of JPH06277075A publication Critical patent/JPH06277075A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To increase the yield of phycocyanin by remarkably increasing the content of phycocyanin per unit algal cells. CONSTITUTION:In relation to a method for producing phycocyanin by culturing and growing a diatom in an aqueous medium and extracting phycocyanin from the resultant algal cells, this method for increasing the yield of phycocyanin involves one process among (1) a process for increasing the concentrations of the whole medium components, (2) a process for increasing the concentration of only a specified medium component, (3) a process for adding a culture medium increased in the concentrations of the whole components during culture and (4) a process for adding only a specified medium component during culture.

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、微細藻類を水性媒質中
で培養増殖させ、えられた藻体から色素タンパク質の1
つであるフィコシアニンを抽出、製造する方法におい
て、藻体中における目的物質の含量を高めることによ
り、目的物質の収量の増大を図ることを目的としたフィ
コシアニンの増収法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention cultivates and proliferates microalgae in an aqueous medium.
The present invention relates to a method for increasing the yield of a target substance by increasing the content of the target substance in the alga in a method for extracting and producing phycocyanin, which is one of the methods.

【0002】[0002]

【従来の技術および発明が解決しようとする課題】フィ
コシアニンは藍藻あるいはクリプト藻のフィコビリソー
ムを構成する色素タンパク質の1つであり、藍藻あるい
はクリプト藻の光合成において、光エネルギーを補足す
るという役割を果たしている。通常、615nm に吸収極大
波長があり、鮮やかな青色を呈することから、天然色素
として利用されている(特公昭55-47866 号公報および
特公昭56-5143 号公報参照)。また、生理活性作用も注
目されているために、藍藻を増殖することによってフィ
コシアニンを製造する技術開発が進められているが、よ
り一層の収量増加が望まれている。
2. Description of the Related Art Phycocyanin is one of pigment proteins constituting phycobilisomes of cyanobacteria or cryptoalga and plays a role of supplementing light energy in photosynthesis of cyanobacteria or cryptoalga. . Usually, since it has an absorption maximum wavelength at 615 nm and exhibits a bright blue color, it is used as a natural dye (see Japanese Patent Publication Nos. 55-47866 and 56-5143). Further, since a physiologically active action is also drawing attention, technological development for producing phycocyanin by growing cyanobacteria is under way, but further increase in yield is desired.

【0003】従来藍藻によるフィコシアニン生産の検討
においては、1週間から2週間といった一定期間での培
養が検討されているだけで、培養期間中の藻体当たりの
フィコシアニン含量の変化を経時的に詳細に検討した例
はなく、培養期間を通して藻体当たりのフィコシアニン
含量は一定であると思われていた。
Conventionally, in the study of phycocyanin production by cyanobacteria, only the culture for a fixed period such as 1 to 2 weeks has been studied, and the change in the phycocyanin content per alga body during the culture period can be detailed over time. There was no study, and it was thought that the phycocyanin content per alga was constant throughout the culture period.

【0004】本発明者らは、藍藻の培養期間を通して経
時的に詳細にフィコシアニン含量を検討することによっ
て、培養初期の2〜4日目にフィコシアニン含量が極大
となり、その後藍藻の増殖にともない、藻体当たりのフ
ィコシアニン含量が下がっていくことを見いだした(図
1参照)。すなわち従来は、約1週間から2週間の培養
期間内のフィコシアニン含量が下がってきた時点で培養
を止め、藍藻を集めフィコシアニンを抽出していたこと
になる。しかるに、本発明者らは、藍藻を増殖させなが
らフィコシアニンを高含量のまま維持させるためには、
培養の途中に窒素源を含む栄養物質または培地成分を添
加すればよいことを見いだし、本発明を完成させるに至
った。
The present inventors investigated the phycocyanin content in detail over time through the culture period of cyanobacteria, and the phycocyanin content reached a maximum on the 2nd to 4th days in the early stage of the culture, and thereafter, as the cyanobacteria grew, the algae increased. It was found that the phycocyanin content per body decreased (see Fig. 1). That is, conventionally, the culture was stopped when the phycocyanin content decreased within the culture period of about 1 to 2 weeks, and the cyanobacteria were collected to extract the phycocyanin. However, in order to maintain a high content of phycocyanin while growing cyanobacteria, the present inventors have
It has been found that a nutrient substance containing a nitrogen source or a medium component may be added during the culture, and the present invention has been completed.

【0005】[0005]

【課題を解決するための手段】本発明は、微細藻類を水
性媒質中で培養増殖させ、えられた藻体からフィコシア
ニンを抽出してフィコシアニンを製造する際において、
つぎのいずれかの工程、(1)培地成分全体の濃度を上
げる工程、(2)培地中の特定成分のみ濃度を上げる工
程、(3)培養の途中に成分全体の濃度を上げた培地を
添加する工程または(4)培養の途中に培地中の特定成
分のみを添加する工程を含むことを特徴とするフィコシ
アニンの増収法に関する。
Means for Solving the Problems The present invention comprises culturing and proliferating microalgae in an aqueous medium and extracting phycocyanin from the obtained algal cells to produce phycocyanin.
Any of the following steps, (1) increasing the concentration of all the medium components, (2) increasing the concentration of only specific components in the medium, (3) adding a medium in which the concentration of all the components is increased during the culture Or (4) a step of adding only a specific component in the medium during the culture, to a method for increasing the yield of phycocyanin.

【0006】[0006]

【実施例】本発明は、微細藻類を増殖させ、かつ藻体当
たりのフィコシアニン含量を高く維持することによって
フィコシアニンの生産性を著しく高めるというフィコシ
アニンの増収法を提供するものである。
EXAMPLES The present invention provides a method for increasing the yield of phycocyanin in which the productivity of phycocyanin is markedly increased by growing microalgae and maintaining a high phycocyanin content per alga body.

【0007】本発明において利用できる微細藻類は、フ
ィコシアニンを産生する藻類であればいずれのものでも
よいが、藍藻類が好ましく、国際寄託機関である、アメ
リカン タイプ カルチャー コレクション(American
Type Culture Collection 、以下ATCCと称す)に寄
託されている公知の藍藻またはその変種や変異株に限る
ことなく、天然から分離した海洋性、淡水性の藍藻も使
用できる。また、これらの藻体を1種または2種以上併
用してもよい。たとえば、シネココッカス( Synechococ
cus ) 属、シネコシスティス( Synechocystis ) 属、ス
ピルリナ( Spirulina ) 属、ノストック( Nostoc )属、
フィシェレラ( Fischerell )属、ホルミディウム( Phor
midium )属、グレオカプサ( Gloeocapsa )属、カロスリ
ック( Calothrix ) 属、プレクトネマ( Plectonema )
属、オスシラトリア( Oscillatoria )属などに属する藍
藻があげられる。かかる藻類の具体例としては、シネコ
コッカス属 ( Synechococcus sp.)に属するATCC 2
7144、ATCC 27192、ATCC 27180、ATCC 294
04またはATCC 29534、シネコシスティス属( Synec
hocystis sp.)に属するATCC 27150またはATCC
27266、スピルリナ属( Spirulina sp.)に属するAT
CC 29541またはATCC 29542、ノストック属( Nost
oc sp.)に属するATCC 27904、フィシェレラ属( Fi
schirella sp.)に属するATCC 27929またはATC
C 29161、ホルミディウム属 (Phormidium sp.)に属す
るATCC 29409、グレオカプサ属( Gloeocapsa sp.)
に属するATCC 27269、カロスリック属 ( Calothrix
sp.)に属するATCC 27901、プレクトネマ属 (Plecto
nema sp.)に属するATCC 18200、オスシラトリア属
(Oscillatoria sp.)に属するATCC 27906などがあ
げられる。
The microalgae that can be used in the present invention may be any algae that produce phycocyanin, but cyanobacteria are preferable, and the American type culture collection (American) which is an international depository institution.
The well-known cyanobacteria deposited in the Type Culture Collection (hereinafter referred to as ATCC) or its variants or mutants are not limited, and marine and freshwater cyanobacteria isolated from nature can also be used. Moreover, you may use these algal bodies together by 1 type (s) or 2 or more types. For example, Synechococ
cus) genus, Synechocystis (Synechocystis) genus Spirulina (Spirulina) genus, Nostoc (Nostoc) genus,
The genus Fischerell , Phordium
midium) genus, Gureokapusa (Gloeocapsa) genus, Karosurikku (Calothrix) genus, Purekutonema (Plectonema)
Examples include cyanobacteria belonging to the genus Oscillatoria . Specific examples of such algae include ATCC 2 belonging to the genus Synechococcus sp .
7144, ATCC 27192, ATCC 27180, ATCC 294
04 or ATCC 29534, Synec
ATCC 27150 or ATCC belonging to hocystis sp .
27266, AT belonging to the genus Spirulina sp .
CC 29541 or ATCC 29542, Nostoc
oc sp .) ATCC 27904, genus Fischerella ( Fi
schirella sp .) belonging to ATCC 27929 or ATC
C 29161, ATCC 29409 belonging to the genus Phormidium sp ., And genus Gloeocapsa sp .
Belongs to ATCC 27269, Calothrix
AT CC 27901 belonging to sp .), Plecto nema ( Plecto
nema sp.) belonging to ATCC 18200, Osushiratoria the genus
ATCC 27906 and the like belonging to ( Oscillatoria sp .).

【0008】本発明において用いられる藍藻を維持生育
させる培地成分としては、通常の藍藻の培養に用いられ
ている公知の藍藻用培地であれば良く、たとえば表1、
2に示したBG−11培地または国立環境研究所のC培
地などを用いることができる。また、海水性または好塩
性の藍藻のばあいには、NaClを0.1 〜5%適宜添加
すればよいし、ビタミンB12要求性の藻のばあいには、
1〜50μg/lのビタミンB12を添加すればよい。
The medium component for maintaining and growing cyanobacteria used in the present invention may be any known medium for cyanobacteria that is commonly used for culturing cyanobacteria, for example, Table 1
BG-11 medium shown in 2 or C medium of National Institute for Environmental Studies can be used. Further, in the case of seawater or halophilic cyanobacteria, 0.1 to 5% of NaCl may be appropriately added, and in the case of algae requiring vitamin B 12 ,
Vitamin B 12 of 1 to 50 μg / l may be added.

【0009】[0009]

【表1】 [Table 1]

【0010】[0010]

【表2】 [Table 2]

【0011】本発明は、藍藻の培養において培地中のN
源物質もしくはそれらを含む培地の濃度を上げて培養す
るか、または培養の途中に数回、培地中のN源物質もし
くはそれらを含む培地を添加することによってフィコシ
アニン含量を高く維持し、フィコシアニンの増収をはか
るものである。
The present invention relates to N in a medium for culturing cyanobacteria.
The phycocyanin content is maintained high by increasing the concentration of the source material or the medium containing them, or by adding the N source material in the medium or the medium containing them several times during the culture to increase the phycocyanin yield. Is to measure.

【0012】N源物質とは、藍藻の同化作用においてに
藍藻中に窒素を供給する物質であればいずれのものでも
よく、かかるN源物質の具体例としては、NaNO3
NH4 NO3 またはKNO3 などがあげられる。
The N-source substance may be any substance as long as it supplies nitrogen into cyanobacteria in the assimilation action of cyanobacteria. Specific examples of such an N-source substance include NaNO 3 and
Examples thereof include NH 4 NO 3 and KNO 3 .

【0013】培地中のN源物質もしくはそれらを含む培
地の濃度を上げて培養するばあいには、N源物質の濃度
が窒素元素として、0.5 〜12.5g/l、好ましくは0.5
〜2.5 g/lとなるように調製した培地を用いて培養す
ればよい。たとえば、BG−11培地を用いるばあいに
は、標準培地濃度に対して2〜10倍、好ましくは2〜
5倍の濃度で培養すればよい。
When the concentration of the N source substance in the medium or the medium containing them is increased and the culture is carried out, the concentration of the N source substance is 0.5 to 12.5 g / l, preferably 0.5
Culture may be performed using a medium prepared to have a concentration of 2.5 g / l. For example, when BG-11 medium is used, it is 2 to 10 times, preferably 2 to 10 times the standard medium concentration.
Culture may be performed at a 5-fold concentration.

【0014】培養の途中に数回、N源物質もしくはそれ
らを含む培地を添加して培養するばあいには、培養開始
後2〜7日ごとに、N源物質の最終的な添加総量が窒素
元素として、0.5 〜12.5g/lとなるように数回、好ま
しくは2〜5回添加すればよい。
When the N-source substance or the medium containing them is added several times during the culture, the final total amount of the N-source substance added is nitrogen every 2 to 7 days after the start of the culture. As an element, it may be added several times, preferably 2 to 5 times, so as to have an amount of 0.5 to 12.5 g / l.

【0015】ただし、海水性の培地では食塩濃度は1〜
2倍までとするのが好ましい。
However, the salt concentration in the seawater medium is 1 to
It is preferably doubled.

【0016】藍藻の培養は、通常の方法で行なえばよ
い。培養時には光照射が必要であるが、太陽光、ハロゲ
ン灯、蛍光灯、白熱電灯などが用いられる。藍藻培養時
の光は4〜200 μEinstein/m2 /sec の強度であれば
良く、好ましくは5〜60μEinstein/m2 /sec である
が、培養初期には弱くしておき、藍藻の生育に応じて強
くしてもよい。また適宜培養液中に炭酸ガスを吹き込
み、溶液中の炭酸イオンの量を増加させることによって
増殖速度をたかめることもできる。
Cyanobacteria may be cultured by a usual method. Although light irradiation is required during culture, sunlight, halogen lamps, fluorescent lamps, incandescent lamps, etc. are used. Light during cyanobacterium culture may have an intensity of 4 to 200 μEinstein / m 2 / sec, preferably 5 to 60 μEinstein / m 2 / sec, but it should be weakened at the beginning of the culture and adjusted according to the growth of cyanobacteria. You may strengthen it. The growth rate can also be increased by appropriately blowing carbon dioxide into the culture solution to increase the amount of carbonate ions in the solution.

【0017】高密度で培養するには、半透性の半透膜も
しくは透析膜などを用いるか、または遠心分離機を用い
て藻体を回収し、培地の一部を除いてから、N源溶液ま
たは培地を加えるのが好ましい。
For high-density culture, a semipermeable semipermeable membrane or dialysis membrane or the like is used, or a centrifuge is used to collect algal cells, and a part of the medium is removed, followed by N source. It is preferred to add a solution or medium.

【0018】培養した藻体は、ろ過によるか、または遠
心分離機を用いて、通常の方法、たとえば3000rpm 、15
分程度遠心分離を行うとよい。
The cultured algal cells may be filtered or by using a centrifuge in a conventional manner, for example, 3000 rpm, 15 rpm.
Centrifuge for about a minute.

【0019】フィコシアニンは、培養した藻体中に産生
され、フィコシアニンの抽出および含量の測定は以下の
ようにして行なう。
Phycocyanin is produced in the cultured alga body, and the extraction and content of phycocyanin are measured as follows.

【0020】経時的にサンプリングした藻体懸濁液を30
00rpm 、4℃で15分間遠心分離操作を行い、上澄液を捨
て藻体懸濁液をえる。えられる藻体懸濁液と等量の水で
藻体懸濁液を洗浄したのち、凍結乾燥する。凍結乾燥藻
体10mgを1mg/mlのリゾチーム溶液(0.1Mリン酸緩衝
液、pH6.5)10mlに懸濁し、暗所で30℃、3〜6時間振
盪し、溶菌する。これを3000rpm 、4℃で15分間遠心分
離操作を行い、えられた上清の抽出液について615nm と
652nm における吸光度を測定することにより、乾燥藻体
当たりのフィコシアニン含量を求める。
30 algae suspensions sampled over time
Centrifuge at 00 rpm and 4 ° C for 15 minutes to discard the supernatant and obtain an algal suspension. The algal suspension is washed with the same amount of water as the obtained algal suspension, and then freeze-dried. Lyophilized algal cells (10 mg) are suspended in 1 mg / ml lysozyme solution (0.1 M phosphate buffer, pH 6.5) and shaken at 30 ° C. for 3 to 6 hours in the dark to lyse the cells. This was centrifuged at 3000 rpm for 15 minutes at 4 ° C, and the resulting supernatant extract was adjusted to 615 nm.
The phycocyanin content per dry alga is determined by measuring the absorbance at 652 nm.

【0021】つぎに実施例により本発明の方法を具体的
に述べるが、以下の例に限定されるものではない。
Next, the method of the present invention will be specifically described by way of examples, but the invention is not limited to the following examples.

【0022】比較例1 シネココッカス属 ( Synechococcus sp.)に属するAT
CC 27144をBG−11培地を用いて25℃、蛍光灯下40μ
Einstein/m2 /sec で培養した。培養開始後、経時的
に培養液の一部を抜き取り、3000rpm 、4℃、15分間遠
心分離操作を行い、藻体を回収し、水で洗浄したのち凍
結乾燥した。この乾燥重量により藻体増殖を評価した。
さらにこの凍結乾燥藻体10mgを0.1 %リゾチーム溶液10
ml(0.1MNa−EDTAを含む0.1 Mリン酸緩衝液、p
H6.5 )に懸濁し、暗所、30℃で4時間振盪し、溶菌し
た。これを前記同様に遠心分離操作を行い、沈殿と抽出
液とに分け、えられた抽出液の615nm と652nm における
吸光度を測定することにより、フィコシアニン含量を求
めた。結果を図1に示した。培養開始後3日目に単位乾
燥藻体重量当たりのフィコシアニン含量が最大になって
おり、その後藻の増殖にともない、単位乾燥藻体重量当
たりのフィコシアニン含量は低下していった。
Comparative Example 1 AT belonging to the genus Synechococcus sp .
CC27144 in BG-11 medium at 25 ° C under fluorescent light 40μ
The cells were cultured at Einstein / m 2 / sec. After the start of the culture, a part of the culture solution was withdrawn with time, centrifuged at 3000 rpm, 4 ° C. for 15 minutes to collect algal cells, washed with water and freeze-dried. The algal growth was evaluated by this dry weight.
Furthermore, 10 mg of this freeze-dried algal cells was added to 10% of 0.1% lysozyme solution.
ml (0.1 M phosphate buffer containing 0.1 M Na-EDTA, p
The cells were suspended in H6.5), shaken at 30 ° C. for 4 hours in the dark, and lysed. The phycocyanin content was determined by centrifuging this in the same manner as above, separating it into a precipitate and an extract, and measuring the absorbance of the obtained extract at 615 nm and 652 nm. The results are shown in Fig. 1. The phycocyanin content per unit dry algal weight reached a maximum on the third day after the start of the culture, and thereafter, the phycocyanin content per unit dry algal weight decreased with the growth of algae.

【0023】培養3週間で乾燥藻体濃度は2.0 g/l、
フィコシアニン含量は7.1 %で、産生されたフィコシア
ニンは142mg /lであった。
After 3 weeks of culturing, the concentration of dried algal cells was 2.0 g / l,
The phycocyanin content was 7.1% and the phycocyanin produced was 142 mg / l.

【0024】実施例1 シネココッカス属 ( Synechococcus sp.)に属するAT
CC 27144を用いて比較例1と同様に培養を開始した
後、4、7、11、16日目に培養液をそれぞれ1/4、1
/3、1/2、1/2ずつ分取し、藻体を遠心分離によ
って回収し、藻体をまた培養器に戻し、BG−11培地を
2倍濃度とした培地を分取した培養液と等量加えた。21
日目に培養を止め、培養液を比較例1と同様に処理し、
乾燥藻体量とフィコシアニン含量を測定し、フィコシア
ニン産生量を求めた。乾燥藻体濃度は2.1 g/l、フィ
コシアニン含量は18.8%で、産生されたフィコシアニン
は395mg /lとなり、比較例1の結果と比べて本発明の
方法により産生量は2.8 倍と著しく向上した。
Example 1 AT belonging to the genus Synechococcus sp .
After culturing was started in the same manner as in Comparative Example 1 using CC 27144, the culture solution was diluted to 1/4, 1 and 4 days 4, 7, 11 and 16, respectively.
/ 3, 1/2, 1/2 each, collected alga bodies by centrifugation, returned the alga bodies to the incubator again, and collected the medium containing BG-11 medium at double concentration And added the same amount. twenty one
The culture was stopped on the day, and the culture solution was treated in the same manner as in Comparative Example 1,
The amount of dried algal cells and the content of phycocyanin were measured to determine the amount of phycocyanin produced. The concentration of dry algal cells was 2.1 g / l, the phycocyanin content was 18.8%, and the phycocyanin produced was 395 mg / l. Compared with the results of Comparative Example 1, the production amount of the method of the present invention was remarkably improved by 2.8 times.

【0025】また、比較例1と同様に培養開始後、経時
的に培養液の一部を抜き取り、乾燥藻体あたりのフィコ
シアニン含量(%)を求めた。結果を図1に示した。
After culturing was started in the same manner as in Comparative Example 1, a part of the culture solution was withdrawn over time to determine the phycocyanin content (%) per dried alga. The results are shown in Fig. 1.

【0026】実施例2〜9 実施例1において、シネココッカス属 ( Synechococcus
sp.)に属するATCC 27144の代わりに、表3の藍藻
を用いたほかは全て実施例1と同様に行い、表3の結果
をえた。
Examples 2-9 In Example 1, the genus Synechococcus
sp .) was replaced with ATCC 27144 belonging to Table 3 and the same procedure as in Example 1 was carried out except that the cyanobacteria in Table 3 was used, and the results in Table 3 were obtained.

【0027】[0027]

【表3】 [Table 3]

【0028】実施例10 比較例1と同様に培養開始後、4、7、11、16日目にB
G−11培地を2倍濃度とした培地を培養液の1/4量ず
つ添加し、21日目に培養を止め、培養液を比較例1と同
様に処理し、乾燥藻体量とフィコシアニン含量を求め
た。培養液は約2.4 倍に増えており、乾燥藻体濃度は、
0.91g/l、フィコシアニン含量は15.5%でフィコシア
ニン産生量は141mg /lであった。
Example 10 As in Comparative Example 1, B was measured 4, 7, 11, 16 days after the start of culture.
A medium containing G-11 medium at a double concentration was added by 1/4 volume of the culture solution, the culture was stopped on the 21st day, the culture solution was treated in the same manner as in Comparative Example 1, and the amount of dried algal cells and phycocyanin content were changed. I asked. The culture solution has increased about 2.4 times, and the concentration of dried algal cells is
The phycocyanin content was 0.91 g / l, the phycocyanin content was 15.5%, and the phycocyanin production was 141 mg / l.

【0029】実施例11 実施例1において、BG−11培地を2倍濃度とした培地
を添加する代わりに、BG−11培地のNaNO3 のみ
2倍濃度とした培地を添加したほかは実施例1と同様に
行った。21日目に培養を止め、乾燥藻体濃度2.0 g/
l、フィコシアニン含量12.8%、フィコシアニン産生量
256mg /lをえた。
Example 11 Example 1 was repeated except that the medium of BG-11 medium containing only NaNO 3 in double concentration was added instead of the medium containing BG-11 medium of double concentration. I went the same way. The culture was stopped on the 21st day and the concentration of dried algal cells was 2.0 g /
1, phycocyanin content 12.8%, phycocyanin production
256 mg / l was obtained.

【0030】実施例12および比較例2 シネコシスティス属 ( Synechocystis sp.)ATCC 2
7266を用いて、BG−11培地を3倍濃度とし、該培地に
2%(w/v)のNaCl、10μg/lのビタミンB12
を添加したほかは比較例1と同様に培養を行った。比較
例2として、シネコシスティス属 ( Synechocystis s
p.)ATCC 27266を用いて、BG−11培地に2%(w
/v)のNaCl、10μg/lのビタミンB12を添加し
たほかは比較例1と同様に培養を行った。結果を表4に
示した。
Example 12 and Comparative Example 2 Synechocystis sp . ATCC 2
7266 was used to make the BG-11 medium a 3-fold concentration, and 2% (w / v) NaCl and 10 μg / l vitamin B 12 were added to the medium.
Culture was performed in the same manner as in Comparative Example 1 except that was added. As Comparative Example 2, Synechocystis s
p .) ATCC 27266 in BG-11 medium at 2% (w
/ V) NaCl and 10 μg / l vitamin B 12 were added, and the same culture as in Comparative Example 1 was performed. The results are shown in Table 4.

【0031】[0031]

【表4】 [Table 4]

【0032】実施例13 シネコシスティス属 ( Synechocystis sp.)ATCC 2
7266を用いて、BG−11培地のNaNO3 のみ3倍濃度
とした以外は実施例12と同様に培養を行った。21日目に
培養を止め、乾燥藻体濃度1.8 g/l、フィコシアニン
含量11.5%フィコシアニン産生量 207mg/lをえた。
Example 13 Synechocystis sp . ATCC 2
Using 7266, culturing was performed in the same manner as in Example 12 except that NaNO 3 in the BG-11 medium was used at a 3-fold concentration. Cultivation was stopped on the 21st day, and a dry algal cell concentration of 1.8 g / l and a phycocyanin content of 11.5% phycocyanin production amount of 207 mg / l were obtained.

【0033】[0033]

【発明の効果】本発明の方法により、藻体当たりのフィ
コシアニン含量を著しく高め、フィコシアニンの増収を
もたらすことができ、よってフィコシアニンの生産コス
トを著しく下げることができる。
INDUSTRIAL APPLICABILITY According to the method of the present invention, the phycocyanin content per alga body can be remarkably increased, and the phycocyanin yield can be increased, so that the phycocyanin production cost can be remarkably reduced.

【図面の簡単な説明】[Brief description of drawings]

【図1】比較例1および実施例1において記したシネコ
コッカス属( Synechococcus sp.)ATCC 27144の培養
中の乾燥藻体重量当たりのフィコシアニン含量の変化を
培養経時的に示した図である。
FIG. 1 is a diagram showing changes in phycocyanin content per weight of dry algal cells in culture of Synechococcus sp . ATCC 27144 described in Comparative Example 1 and Example 1 over time in culture.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 微細藻類を水性媒質中で培養増殖させ、
えられた藻体からフィコシアニンを抽出してフィコシア
ニンを製造する際において、つぎのいずれかの工程を含
むことを特徴とするフィコシアニンの増収法。 (1)培地成分全体の濃度を上げる工程、(2)培地中
の特定成分のみ濃度を上げる工程、(3)培養の途中に
成分全体の濃度を上げた培地を添加する工程または
(4)培養の途中に培地中の特定成分のみを添加する工
程。
1. A microalgae is cultured and grown in an aqueous medium,
A method for increasing the yield of phycocyanin, which comprises the step of any one of the following in producing phycocyanin by extracting phycocyanin from the obtained algal cells. (1) A step of increasing the concentration of all medium components, (2) A step of increasing the concentration of only specific components in the medium, (3) A step of adding a medium in which the concentration of all the components is increased during the culture, or (4) Culture A step of adding only specific components in the medium in the middle of.
【請求項2】 前記微細藻類が藍藻である請求項1記載
のフィコシアニンの増収法。
2. The method for increasing the yield of phycocyanin according to claim 1, wherein the microalgae are cyanobacteria.
【請求項3】 前記特定成分がN元素を含む物質または
培地である請求項1記載のフィコシアニンの増収法。
3. The method for increasing the yield of phycocyanin according to claim 1, wherein the specific component is a substance containing N element or a medium.
JP5066653A 1993-03-25 1993-03-25 Yield increase of phycocyanin Pending JPH06277075A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5066653A JPH06277075A (en) 1993-03-25 1993-03-25 Yield increase of phycocyanin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5066653A JPH06277075A (en) 1993-03-25 1993-03-25 Yield increase of phycocyanin

Publications (1)

Publication Number Publication Date
JPH06277075A true JPH06277075A (en) 1994-10-04

Family

ID=13322078

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5066653A Pending JPH06277075A (en) 1993-03-25 1993-03-25 Yield increase of phycocyanin

Country Status (1)

Country Link
JP (1) JPH06277075A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2013105430A1 (en) * 2012-01-12 2015-05-11 江崎グリコ株式会社 Method for preparing phycocyanin

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2013105430A1 (en) * 2012-01-12 2015-05-11 江崎グリコ株式会社 Method for preparing phycocyanin
US10214568B2 (en) 2012-01-12 2019-02-26 Ezaki Glico Co., Ltd. Method for preparing phycocyanin

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