JP2526360B2 - Method for culturing filamentous algae - Google Patents

Method for culturing filamentous algae

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Publication number
JP2526360B2
JP2526360B2 JP5223598A JP22359893A JP2526360B2 JP 2526360 B2 JP2526360 B2 JP 2526360B2 JP 5223598 A JP5223598 A JP 5223598A JP 22359893 A JP22359893 A JP 22359893A JP 2526360 B2 JP2526360 B2 JP 2526360B2
Authority
JP
Japan
Prior art keywords
culture
culture solution
algae
culturing
carrier
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
JP5223598A
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Japanese (ja)
Other versions
JPH0775555A (en
Inventor
真希子 氷見
一紀 藤田
繁也 米谷
和樹 小林
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.)
Research Institute of Innovative Technology for Earth
Hitachi Ltd
Original Assignee
Research Institute of Innovative Technology for Earth
Hitachi Ltd
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Priority to JP5223598A priority Critical patent/JP2526360B2/en
Publication of JPH0775555A publication Critical patent/JPH0775555A/en
Application granted granted Critical
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Expired - Fee Related legal-status Critical Current

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Description

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

【0001】[0001]

【産業上の利用分野】本発明は糸状体藻類の培養方法に
係り、特に糸状体藻類を培養した後の培養液からこれら
の藻体を回収するのが容易である糸状体藻類の培養方法
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for culturing filamentous algae, and more particularly to a method for culturing filamentous algae, which facilitates the recovery of these algae from the culture solution after culturing the filamentous algae. .

【0002】[0002]

【従来の技術】近年、藻類の大量培養によるCO2 固定
や良質のタンパク質の生産等が注目されている。藻類の
培養によって藻体中の有用物質等を生産する際には、培
養後の藻体を培養液から回収する固液分離の工程が必要
となるが、藻類を大量生産する場合にはこの固液分離工
程が大きな問題となっている。すなわち、実験室等で小
規模で行う培養では、吸引ろ過等による培養液の除去や
遠心分離による藻体の沈降によって藻体のみを回収する
ことが可能である。しかし、大規模の培養には大きな培
養面積と大量の培養液が必要であり、培養後の藻体の回
収をろ過法や遠心分離法で行うと、高エネルギー、高費
用を要することとなり、非実用的であった。
2. Description of the Related Art In recent years, attention has been paid to CO 2 fixation by high-volume culture of algae and production of high-quality proteins. When a useful substance in an alga is produced by culturing algae, a solid-liquid separation step of recovering the alga after culturing from the culture solution is required. The liquid separation process has become a big problem. That is, in a small-scale culture in a laboratory or the like, it is possible to collect only the algal cells by removing the culture solution by suction filtration or by sedimenting the algal cells by centrifugation. However, large-scale culture requires a large culture area and a large amount of culture solution, and if the alga bodies are recovered by a filtration method or a centrifugation method after the culture, high energy and high cost are required. It was practical.

【0003】また、藻類の大量培養における藻体回収の
方法として、藻体が自然に培養液中で浮上する性質を利
用し、浮上した藻体の濃縮液を回収し、そのまま乾燥す
る方法( Algae Biowass: ‘Ruoaloriented fresh wate
r culitivation and production of algae in India'
I. V. Venkataiaman, B. P. Nigam and P. K. Ramanath
an )、硫酸アルミニウムや塩化カルシウムなどの凝集剤
を培養液に添加して藻体を凝集させ、固液分離する方法
( Advances in Biotechnological Process 6,pages 7
3−110 )などが提案されている。
Further, as a method for recovering algal bodies in a large-scale culture of algae, a method of utilizing the property that algal bodies naturally float in the culture solution, collecting a concentrated liquid of the floating algal bodies, and drying it directly (Algae Biowass: 'Ruoaloriented fresh wate
r culitivation and production of algae in India '
IV Venkataiaman, BP Nigam and PK Ramanath
an), a flocculant such as aluminum sulfate or calcium chloride is added to the culture solution to flocculate the alga cells and perform solid-liquid separation (Advances in Biotechnological Process 6, pages 7
3-110) and the like have been proposed.

【0004】しかしながら、前者の方法では、浮上した
藻体の濃縮液は凝集体と異なりすくい取ることができな
いため、濃縮液を直接乾燥しなければならず、藻体の回
収に長時間を要するという欠点があり、また後者の方法
では、凝集剤の使用により培養物が汚染され、藻体やそ
の抽出物を食品や薬品として用いる場合に特に凝集剤の
混入が問題となる場合がある。
However, in the former method, the concentrated liquid of the algal cells that has floated up cannot be scooped out unlike the aggregates, so the concentrated liquid must be dried directly, and it takes a long time to recover the algal cells. In the latter method, the culture is contaminated by the use of the aggregating agent, and when the alga body or its extract is used as a food or a drug, the incorporation of the aggregating agent may be a problem.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、前記
従来技術の問題を解決し、培養後の糸状体藻類を効率よ
く、かつ汚染することなく培養液から回収することがで
きる糸状体藻類の培養方法を提供することにある。
The object of the present invention is to solve the above-mentioned problems of the prior art and to collect filamentous algae after culturing efficiently and without contamination from the culture broth. The purpose of the present invention is to provide a method for culturing.

【0006】[0006]

【課題を解決するための手段】上記目的は、藻類培養液
多孔性担体または繊維状担体を加え、一定速度の旋回
流を起こし、藻体に凝集物を形成させるとともに、この
凝集物を担体に蓄積させることにより達成される。すな
わち、本願で特許請求される発明は以下の通りである。 (1)糸状体藻類を培養液中で培養するに当たり、培養
液に多孔性担体または繊維状担体を加え、かつ該培養液
を流速13〜32cm/secで旋回することを特徴と
する糸状体藻類の培養方法。
The above object is to add a porous carrier or a fibrous carrier to an algae culture solution, to cause a swirling flow at a constant speed to form an agglomerate in an algal body, and the agglomerate to be a carrier. It is achieved by accumulating in. That is, the invention claimed in the present application is as follows. (1) When culturing filamentous algae in a culture solution, a porous carrier or a fibrous carrier is added to the culture solution, and the culture solution is swirled at a flow rate of 13 to 32 cm / sec. Culture method.

【0007】[0007]

【作用】培養液の旋回によって培養された藻体が旋回中
心部または培養容器底部にひき込れ、これらの場所で凝
集して凝集物を形成する。この凝集物は培養液内で沈澱
するため回収が容易となる。特に糸状体の藻体はたがい
にからみあい、より高高度に凝集するため、回収効率が
向上する。また培養液に担体を加えて旋回することによ
り、旋回中心部に集まった藻体が中心部に流れてきた担
体と接触し、担体の孔内に蓄積または担体の繊維にから
みつくことができるため、藻体の凝集が容易となり、培
養液からの藻体の回収がさらに容易となる。
The algal cells cultured by the swirling of the culture solution are drawn into the center of swirling or the bottom of the culture vessel and aggregate at these places to form aggregates. Since this aggregate precipitates in the culture medium, it can be easily collected. In particular, filamentous algae are entangled with each other and aggregate at a higher level, which improves the recovery efficiency. Further, by adding a carrier to the culture solution and swirling, the alga bodies gathered in the swirling center contact the carrier flowing into the center, and can accumulate in the pores of the carrier or become entangled in the fibers of the carrier, Aggregation of alga bodies is facilitated, and recovery of alga bodies from the culture solution is further facilitated.

【0008】本発明の培養方法に用いられる藻類は糸状
体藻類であり、例えば、スピルリナ属(Spirulina s
p.)、アナベナ属(Anabaena sp.)等が挙げられる。藻類
は、公知の培地、例えば、K2 HPO4 、NaNO3
FeSO4 、MgSO4 、K2 SO4 、NaCl、Ca
Cl、H3 BO3 、MnCl2 、ZnSO 4 、CuSO
4 、Na2 MoO4 、NH4 VO3 、Co(NO3)2
NiSO4等の無機塩類を5.0〜2,500 ppmおよ
びビタミンアミノ酸などの有機栄養素を0.1〜50 p
pm含む任意の液体培地(培養液)を用いて培養すること
ができる。基本培地の代表的なものとしてザルーク(Za
rrouk )培地などが挙げられる。
The algae used in the culture method of the present invention are filamentous
Body algae, for example, Spirulina s
p.) and the genus Anabaena (Anabaena sp.) and the like. Algae
Is a known medium such as K2HPOFour, NaNO3,
FeSOFour, MgSOFour, K2SOFour, NaCl, Ca
Cl, H3BO3, MnCl2, ZnSO Four, CuSO
Four, Na2MoOFour, NHFourVO3, Co (NO3)2,
NiSOFourInorganic salts such as 5.0 to 2,500 ppm and
And organic nutrients such as vitamins and amino acids 0.1 to 50 p
Culture using any liquid medium (culture medium) containing PM
Can be. As a typical basal medium, Zaluk (Za
rrouk) medium and the like.

【0009】培地には、光合成に必要なCO2 源として
CO2 ガスやNaHCO3 が添加される。通常は0.0
1〜30%、好ましくは1〜20%のCO2 ガスまたは
0.1〜10%、好ましくは0.5〜5%のNaHCO
3 が添加される。培養温度は5〜60℃が好ましく、特
に20〜40℃が好ましい。培養時の光の照度は通常1
00〜100,000ルクスに保たれるが、特に500
〜30,000ルクスが望ましい。光源には蛍光灯、X
eランプ等が用いられるが、フィルター等を用いて藻体
に到達する光の波長を限定したものでもよい。
CO 2 gas or NaHCO 3 is added to the medium as a CO 2 source necessary for photosynthesis. Usually 0.0
1-30%, preferably 1-20% CO 2 gas or 0.1-10%, preferably 0.5-5% NaHCO 3.
3 is added. The culture temperature is preferably 5 to 60 ° C, particularly preferably 20 to 40 ° C. The illuminance of light during culture is usually 1
Maintained at 00-100,000 lux, but especially 500
~ 30,000 lux is desirable. Fluorescent lamp, X
Although an e-lamp or the like is used, a filter or the like may be used to limit the wavelength of light reaching the alga.

【0010】本発明においては培養液に旋回流を起こし
て培養を行う。該旋回流を生じさせる方法には特に制限
はなく、ロータリーシェイカー等を用いて培養器自体を
旋回させる方法や培養液のみを旋回させる方法が採用さ
れる。後者の方法には、培養容器から排出された培養液
を再度旋回流で流入させる循環系を利用する方法、培養
容器中の老廃物を含む培養液を排出し、新鮮培養液を補
充する系を利用する方法等が挙げられ、具体的には、液
体サイクロンの原理を用いた培養槽で培養を行う方法が
挙げられる。また培養容器中に直接CO2 ガスを吹き込
む際にはこの通気系を利用して旋回流を起こすこともで
きる。
In the present invention, the culture is cultivated by causing a swirling flow. The method of generating the swirling flow is not particularly limited, and a method of swirling the incubator itself using a rotary shaker or the like and a method of swirling only the culture solution are adopted. The latter method uses a circulation system in which the culture solution discharged from the culture vessel is again swirled, and a system in which the culture solution containing waste products in the culture vessel is discharged and a fresh culture solution is replenished. Examples thereof include a method of utilizing, and specifically, a method of culturing in a culture tank using the principle of hydrocyclone. Further, when blowing CO 2 gas directly into the culture vessel, a swirling flow can be generated by utilizing this aeration system.

【0011】培養液の旋回速度は、13〜32cm/s
ecである。旋回速度がこの範囲以外では培養時に糸状
体藻類の凝集物を形成することができない。例えば、振
とう幅2.5〜5.0cmの振とう機で、底面径8.5
cmのフラスコを振とうさせるときには20rpm〜8
0rpm、特に30rpm〜70rpmの範囲で回転さ
せるのが好ましい。旋回流は連続流でも間欠流でもよ
い。
The rotation speed of the culture solution is 13 to 32 cm / s.
ec. When the swirling speed is outside this range, aggregates of filamentous algae cannot be formed during culture. For example, a shaker with a shaking width of 2.5 to 5.0 cm and a bottom diameter of 8.5
20 rpm to 8 cm when shaking a cm flask
It is preferable to rotate at 0 rpm, particularly 30 rpm to 70 rpm. The swirling flow may be a continuous flow or an intermittent flow.

【0012】また本発明においては、旋回する培養液に
担体を入れて藻体の凝集を促進する。この担体には、ポ
リウレタンフォーム、スポンジ、シリコンなど多孔性の
もの、フェルト、ヘチマ(植物性繊維)、ガラスファイ
バー等繊維状のものが適しており、糸状体藻類には特に
孔径100〜2000μmのスポンジが適している。担
体の形状には特に制限はないが、径0.5〜10cmの
球体または多面体に細刻または切り込みを入れて表面積
を大きくしたものが好ましい。担体の使用量は、培養液
容積の0.5〜50%程度、特に1〜10%が好まし
い。また担体は、培養開始時に培養液に加えて培養を行
っても、培養後期に加えて、藻体の回収を行ってもよ
い。凝集した藻体は、担体孔内に蓄積し、凝集物として
培養液内に沈殿するため、容易に回収することができ
る。
[0012] In yet present invention, promote aggregation of putting a carrier algal culture solution to pivot. Suitable carriers include porous materials such as polyurethane foam, sponge, and silicone, and fibrous materials such as felt, loofah (vegetable fiber), and glass fiber. Sponge with a pore diameter of 100 to 2000 μm is particularly suitable for filamentous algae. Is suitable. The shape of the carrier is not particularly limited, but a sphere or a polyhedron having a diameter of 0.5 to 10 cm, which is finely chopped or cut to have a large surface area, is preferable. The amount of the carrier used is preferably about 0.5 to 50%, and particularly preferably 1 to 10% of the culture solution volume. In addition, the carrier may be added to the culture solution at the start of the culture for culturing, or may be added at the latter stage of the culturing for collecting the alga. The aggregated alga bodies accumulate in the carrier pores and precipitate in the culture solution as aggregates, so they can be easily collected.

【0013】[0013]

【実施例】以下、本発明を実施例により詳しく説明する
が、本発明はこれらの例に限定されるものではない。 実施例1 Zarrouk培地にCO2 源としてNaHCO3
6.8g/lを添加した液体培地に、糸状体藻類のSp
irulina SP.を0.15g(乾燥重量)/l
および1cm角に切ったスポンジ(孔径500μm)を
入れて培養を行った。培養器には底面径8.5cmのフ
ラスコを用い、これをロータリーシェイカーにより60
rpm(旋回速度13cm/sec)の旋回流を起こし
て液体培地に空気を通気した。培養温度は23℃、照度
13,000ルクスに維持した。培養開始直後は旋回
の中心部に藻体底濃度域ができ、約2時間後には凝集藻
体がスポンジの孔内に蓄積し始め、約6日後にはスポン
ジの表面全体が藻体で覆われた。図1には培養開始6日
後の培養状態を示した。
EXAMPLES The present invention will now be described in detail with reference to examples, but the present invention is not limited to these examples. Example 1 NaHCO 3 1 as a CO 2 source in Zarrow medium
The liquid medium containing 6.8 g / l was added to the filamentous alga Sp
irulina SP. 0.15 g (dry weight) / l
Then, a sponge (pore size: 500 μm) cut into 1 cm squares was put into the cells to culture. A flask with a bottom diameter of 8.5 cm was used as the incubator, and this was shaken by a rotary shaker to 60
A swirling flow of rpm (swirl speed 13 cm / sec) was generated to aerate the liquid medium with air. The culture temperature was maintained at 23 ° C and the illuminance was maintained at 13,000 lux . Turn immediately after the start of culture
There is a bottom concentration area of algal cells in the center of the
The body begins to accumulate in the pores of the sponge, and after about 6 days the sponge
The entire surface of Ji was covered with algal bodies. 6 days from the start of culture
The subsequent culture state is shown.

【0014】[0014]

【0015】[0015]

【0016】[0016]

【0017】[0017]

【0018】[0018]

【0019】[0019]

【0020】[0020]

【0021】[0021]

【0022】比較例1 実施例1において、 藻体として桿状藻体であるSyne
chococcusSP.(0.1g/l、乾燥重量
を用いた以外は実施例1と同様にして培養を行った。し
かし、培養6日を経過しても、藻体はスポンジ孔内に蓄
積されなかった。図2には培養開始6日後の培養状態を
示した。
Comparative Example 1 In Example 1, Syne which is a rod-shaped alga as the alga
chococcus SP. (0.1 g / l , dry weight )
Culture was performed in the same manner as in Example 1 except that However, algal cells were not accumulated in the sponge pores even after 6 days of culture. FIG. 2 shows the culture state 6 days after the start of culture.

【0023】[0023]

【発明の効果】本発明によれば、培養液を特定速度を旋
回し、かつ培養液に多孔性担体または繊維状担体を加え
て旋回をすることにより、培養時に藻体を凝集させつ
つ、これを担体に蓄積することができるため、培養後の
藻体の固液分離を効率よく行うことができ、また藻体回
収に凝集剤等の薬剤を使用しないため、藻体およびその
抽出物の安全性が確保され、大規模な培養を経済的に行
うことが可能である。
According to the present invention, the culture solution is swirled at a specific speed, and a porous carrier or a fibrous carrier is added to the culture solution for swirling, thereby aggregating algal cells during culturing. Since it can be accumulated in the carrier, solid-liquid separation of algal cells after culturing can be efficiently performed, and since no agent such as a flocculant is used for collecting algal cells, the safety of algal cells and their extracts is safe. Therefore, it is possible to economically perform large-scale culture.

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

【図1】実施例1における培養開始後6日目の培養状態
を示す図。
FIG. 1 is a diagram showing a culture state on day 6 after the start of culture in Example 1.

【図2】比較例1における培養開始後6日目の培養状態
を示す図。
FIG. 2 shows the culture state on day 6 after the start of culture in Comparative Example 1 .
FIG.

【符号の説明】[Explanation of symbols]

1…液体培地(培養液)、3…藻体の凝集物、4…分散
した藻体、5…スポンジ、10…フラスコ(培養容
器)。
DESCRIPTION OF SYMBOLS 1 ... Liquid culture medium (culture liquid) , 3 ... Aggregate of alga bodies, 4 ... Dispersed alga bodies, 5 ... Sponge, 10 ... Flask (culture container).

───────────────────────────────────────────────────── フロントページの続き (72)発明者 米谷 繁也 東京都港区西新橋2−8−11 第7東洋 海事ビル8F (72)発明者 小林 和樹 東京都港区西新橋2−8−11 第7東洋 海事ビル8F (56)参考文献 特開 平2−18000(JP,A) 特公 昭46−21782(JP,B1) ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Shigeya Yoneya 2-8-11 Nishi-Shimbashi, Minato-ku, Tokyo 7th Toyo Kaiji Building 8F (72) Inventor Kazuki Kobayashi 2-8-11 Nishi-shinbashi, Minato-ku, Tokyo 7th Toyo Kaiji Building 8F (56) Reference JP-A-2-18000 (JP, A) JP-B-46-21782 (JP, B1)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 糸状体藻類を培養液中で培養するに当た
り、培養液に多孔性担体または繊維状担体を加え、かつ
該培養液を流速13〜32cm/secで旋回すること
を特徴とする糸状体藻類の培養方法。
1. When culturing filamentous algae in a culture solution, a porous carrier or a fibrous carrier is added to the culture solution, and the culture solution is swirled at a flow rate of 13 to 32 cm / sec. Method for culturing body algae.
JP5223598A 1993-09-08 1993-09-08 Method for culturing filamentous algae Expired - Fee Related JP2526360B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5223598A JP2526360B2 (en) 1993-09-08 1993-09-08 Method for culturing filamentous algae

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5223598A JP2526360B2 (en) 1993-09-08 1993-09-08 Method for culturing filamentous algae

Publications (2)

Publication Number Publication Date
JPH0775555A JPH0775555A (en) 1995-03-20
JP2526360B2 true JP2526360B2 (en) 1996-08-21

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WO2010054325A2 (en) * 2008-11-07 2010-05-14 Kuehnle Agrosystems, Inc. Preservation and composition of bioprocess algae for production of lipids, seedstock, and feed

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JPH0218000A (en) * 1988-07-07 1990-01-22 Mitsubishi Heavy Ind Ltd Propagating method of microorganism for decomposing humic acid

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