JP2984749B2 - Algae cultivation method using silicon - Google Patents

Algae cultivation method using silicon

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Publication number
JP2984749B2
JP2984749B2 JP2047200A JP4720090A JP2984749B2 JP 2984749 B2 JP2984749 B2 JP 2984749B2 JP 2047200 A JP2047200 A JP 2047200A JP 4720090 A JP4720090 A JP 4720090A JP 2984749 B2 JP2984749 B2 JP 2984749B2
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JP
Japan
Prior art keywords
algae
culture
algal
concentration
silicon
Prior art date
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Expired - Fee Related
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JP2047200A
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Japanese (ja)
Other versions
JPH03251170A (en
Inventor
昭一 小林
光一 中島
武 生本
和也 藤沢
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Taito Co Ltd
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Taito Co Ltd
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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、シリコンを用いた藻類の培養方法に関し、
詳しくは通気性の優れたシリコン管を用いて連続的に藻
類を培養することを可能とする培養方法に関する。
The present invention relates to a method for culturing algae using silicon,
More specifically, the present invention relates to a culture method that enables continuous algae culture using a silicon tube having excellent air permeability.

[従来の技術及び発明が解決しようとする課題] 藻類には食品として有用な各種成分が含まれ、価格が
折り合えば広い用途が開拓できる。含有成分は藻の種
類、培養法などで異なるが、例えば、スピルリナ、クロ
レラでは各々蛋白質、脂肪、炭水化物、核酸含有量が4
8、6、11、4;55、18、15、4%であり、一般に蛋白質
含有量が高く、炭水化物を増加させたい場合は培地中の
窒素源濃度を下げて培養すればよい。
[Problems to be Solved by Conventional Techniques and Inventions] Algae contain various components useful as foods, and can be used for a wide variety of applications if the prices are reasonable. Although the components differ depending on the type of algae and the culture method, for example, spirulina and chlorella each have a protein, fat, carbohydrate, and nucleic acid content of 4
8, 6, 11, 4; 55, 18, 15, 4%. Generally, when the protein content is high and carbohydrates are to be increased, the culture may be carried out with the nitrogen source concentration in the medium lowered.

また、特殊成分として含まれる、ビタミン、脂肪、色
素、植物ホルモンなどの利用価値も高く、例えば、一例
では、Spirujina platensisにおいてビタミンA前駆
体、B1、B3、B6、B12、Eが、各々1,700、55、118、
3、1.6、190mg/kg乾物量含まれている。このようなこ
とから、藻体全体を健康食品、一般食品としての利用、
炭水化物として含まれる寒天、カラギーナン、アルギン
酸、フコイダンなどの多糖の食品物性改良剤としての利
用が可能である。
In addition, the useful value of vitamins, fats, pigments, plant hormones, and the like, which are contained as special components, is also high. For example, in one example, vitamin A precursors, B 1 , B 3 , B 6 , B 12 , and E are used in Spirujina platensis. , 1,700, 55, 118, respectively
It contains 3, 1.6 and 190 mg / kg dry matter. From such a thing, utilization of the whole algae body as health food, general food,
Polysaccharides such as agar, carrageenan, alginic acid, and fucoidan contained as carbohydrates can be used as food property improving agents.

しかし、藻の生産コストは現在のところ著しく高く、
屋内純粋培養試算では、160〜200米ドル/kg乾物量であ
り、コストに占める割合は、労働力50〜85、ポンプ4〜
24、培地4〜20、混合5〜8%と言われている。
However, the cost of producing algae is currently significantly higher,
Estimation of indoor pure culture is 160-200 USD / kg dry matter, and the ratio of cost is labor force 50-85, pump 4 ~
24, medium 4-20, mixed 5-8%.

したがって、これまでの藻類の培養法では、得られる
藻が高価となるので、藻の食品素材への応用は困難であ
り、僅かに高付加価値の健康食品に応用されているのが
現状である。
Therefore, in the conventional method of cultivating algae, the obtained algae is expensive, so it is difficult to apply the algae to food materials, and at present it is applied to health foods with a slightly high added value. .

[課題を解決するための手段] そこで本発明者らは藻製品の生産コストを培養の連続
化によって低減化することを試み、鋭意検討の結果、シ
リコン管を利用することにより効率的に藻類を連続生産
することを見い出し、そのシステムを組み立てたのであ
る。
[Means for Solving the Problems] Accordingly, the present inventors have attempted to reduce the production cost of algal products by continuation of culture, and as a result of intensive studies, as a result of efficiently using a silicon tube, algae have been efficiently removed. They found out that they would produce them serially, and assembled the system.

従来の藻類生産法では、特に、微細藻の場合、広い平
面の池に水を張り、緩やかに攪拌しながら培養し収穫す
る簡単なものから、ガラス管とポリエチレン管を交互に
繋いだ光合成リアクター(C.Guiden et al.:The World
biotech.Report 1984、Vol.1 Europe、pp541−59、Lond
on:Online Publications Ltd.)など各種の方法があ
る。
In the conventional algae production method, especially in the case of microalgae, water is poured into a large flat pond, cultivation and harvesting is performed with gentle stirring, and a photosynthetic reactor (glass tubes and polyethylene tubes connected alternately) C. Guiden et al .: The World
biotech.Report 1984, Vol.1 Europe, pp541-59, Lond
on: Online Publications Ltd.).

これまで最高であったポリエチレンでの酸素透過性は
30μmの厚さでも25℃で最大で6,000cc/m2・day・atmで
あり、炭酸ガス透過性は本値の3〜4倍である。しか
し、最近開発されたシリコンでの透過性は100μmの厚
さでも酸素で365,000cc/m2・day・atm、炭酸ガスで1,16
5,000cc/m2・day・atmにも達する。そこで本発明者らは
本素材での藻類培養について鋭意検討し、本素材を用い
れば、藻培養液が従来より高濃度であっても藻の生育速
度が低下せず、連続的に高濃度藻液を得られることを見
い出して、本発明を完成したのである。
The oxygen permeability of polyethylene, which was the highest so far,
Even at a thickness of 30 μm, the maximum is 6,000 cc / m 2 · day · atm at 25 ° C., and the carbon dioxide permeability is 3 to 4 times this value. However, recently developed silicon has a permeability of 365,000 cc / m 2 · day · atm for oxygen and 1,16 for carbon dioxide even at a thickness of 100 μm.
Also reached to 5,000cc / m 2 · day · atm . Therefore, the present inventors have studied diligently about algae culture with this material, and using this material, the growth rate of algae does not decrease even if the algal culture solution is higher in concentration than before, and the concentration of algae is continuously increased. The inventors have found that a liquid can be obtained and completed the present invention.

本発明を以下に示す。 The present invention is described below.

本発明はシリコンを用いた藻類の培養方法に関するも
のである。詳しくは、 (1)シリコン製の管状通気性膜もしくは基材の外表面
に固定してある該管状通気性膜に連続的に藻類接種培地
および/または新鮮な液体培地を供給して藻類を培養
し、培養済みの藻類液を順次系外に引き出すことを特徴
とする藻類の連続的培養方法。
The present invention relates to a method for culturing algae using silicon. More specifically, (1) cultivating algae by continuously supplying an algal inoculation medium and / or a fresh liquid medium to a tubular gas-permeable membrane made of silicon or a tubular gas-permeable membrane fixed to the outer surface of a substrate. And continuously drawing the cultured algal solution out of the system.

(2)藻類培養液を透析または濃縮して生育阻害物質を
除去しながら培養する上記の連続的培養方法。
(2) The continuous culture method described above, wherein the algal culture is dialyzed or concentrated to remove the growth-inhibiting substances and cultured.

シリコンは加工の仕方によって通気性を所望の程度に
変えることができ、また機械的強度が強いためにシステ
ムとして利用しやすい。また、シート状、管状、その他
各種の形状に加工でき、極めて有用な素材である。最
近、本素材を細管状に加工し、人工肺に用いた実用化例
はあるが、これは本素材の通気性を使用したものであ
る。本性質を藻類培養に利用したものが本発明の方法で
あり、これまで本素材を何人も藻類培養に利用した例は
なく、ましてや、培養に成功した例はない。また、本発
明の培養方法は素材としてシリコンに限らず、セルロー
ス、セラミックスなどの表面を防水加工したもの、その
他、通気性に優れた素材であれば利用できるが、現在の
ところ、シリコンが最適である。
Silicon can change the air permeability to a desired degree depending on the processing method, and is easily used as a system because of its high mechanical strength. Further, it is a very useful material that can be processed into a sheet shape, a tubular shape, and other various shapes. Recently, there is an example of practical use of this material processed into a thin tube and used for an artificial lung, but this uses the breathability of this material. The method of the present invention uses this property for algae culture. There has been no example of using this material for algae culture, and there is no example of successful culture. In addition, the culture method of the present invention is not limited to silicon as a material, and any material having excellent air permeability, such as cellulose, ceramics and the like whose surface is waterproofed, can be used. is there.

シリコン素材は疎水性表面をもつために藻類の通過が
容易であり、高濃度藻液でも通過でき、さらに通常は藻
濃度が500〜600mg/以上では生育は低下するが、本培
養方法では通気性が著しく優れていることから本値の2
倍以上でも生育速度は早い。
Silicone material has a hydrophobic surface so that it can easily pass through algae, and it can pass through even high-concentration algal fluids.Moreover, growth is usually reduced when the algal concentration is 500-600 mg / min. Is extremely excellent,
The growth rate is fast even if it is twice or more.

シリコンの形状は藻類の培養に適合するものであれ
ば、特に制限はないが、大型藻では平板、微細藻では管
状が便利である。管の大きさは管の厚さにより適当に選
択するが、例えば100μmの厚さでは管径3.0×3.2mm、2
00μmの厚さでは3.6×4.0mm程度が適当である。平膜の
場合は300×300mm角を用い、底をメッシュで補強する。
The shape of silicon is not particularly limited as long as it is suitable for algae culture, but a flat plate for large algae and a tube for microalgae are convenient. The size of the tube is appropriately selected depending on the thickness of the tube.
For a thickness of 00 μm, about 3.6 × 4.0 mm is appropriate. In the case of a flat membrane, use a 300 x 300 mm square and reinforce the bottom with a mesh.

200μmの管を用いた場合、図1のように平板上に渦
巻状にする、円筒に巻き付ける、水平および/または垂
直に置くなどする。平板上に管を並べた場合は、光の効
率を考慮し、少しずつスペースを設け、10段以上にも重
ねることができる。基本的には、このように設備した長
い管に培養液を循環または通過させるが、適当な箇所に
液面を一定に保てる貯液槽を付けると便利である。貯液
槽はシステム内の液量を一定に保ち、新しい培地を常に
補給できるようにセットしておくとよい。
When a 200 μm tube is used, it is spiraled on a flat plate as shown in FIG. 1, wrapped around a cylinder, or placed horizontally and / or vertically. When the tubes are arranged on a flat plate, spaces can be provided little by little in consideration of light efficiency, and the tubes can be stacked in ten or more stages. Basically, the culture solution is circulated or passed through a long tube equipped as described above, but it is convenient to provide a storage tank at an appropriate place to keep the liquid level constant. The storage tank is preferably set so that the amount of liquid in the system is kept constant and a fresh medium can always be supplied.

また、本発明に係るシステムを用いる培養方法では、
20m以上の長い管を用いたり、乾燥条件下では、培養液
が極端に濃縮され、通液が困難となったり、藻の生育速
度が低下することがあるので、この他、逆流止めを備え
た新鮮培地(培地濃度は任意に選択する)供給装置をつ
けるとよい。
In the culture method using the system according to the present invention,
If a long tube of 20 m or more is used, or the culture solution is extremely concentrated under dry conditions, it may be difficult to pass through the culture solution or the growth rate of algae may be reduced. A fresh medium (medium concentration may be selected arbitrarily) may be provided.

さらに、藻の種類、培養条件によっては培養時間の経
過とともに生育阻害物質が蓄積して生育速度が低下する
こともある。このような場合、システムの適当な箇所に
限外濾過膜または藻を通過させず、その他の成分を通過
させる通常の濾過素材、透析膜をセットし、生育阻害物
質を除去しながら連続培養する。この方式によれば、藻
が生産する各種物質を連続的に取り出すこともできる。
Furthermore, depending on the type of algae and the culture conditions, the growth inhibitory substance may accumulate with the elapse of the culture time, and the growth rate may decrease. In such a case, an ordinary filtration material and a dialysis membrane that allow other components to pass without passing through an ultrafiltration membrane or algae are set in an appropriate part of the system, and continuous culture is performed while removing growth inhibitors. According to this method, various substances produced by algae can be continuously taken out.

明、暗の長さを任意に変えることができるのも本シス
テムの特徴であり、管の長さ流量を調節して明部または
暗部にセットしさえすればよい。
It is also a feature of the present system that the length of light and darkness can be arbitrarily changed, and it is only necessary to adjust the length flow rate of the tube to set it in the light or dark portion.

初発藻液の濃度、培養済み藻液の引出しの量比は培養
速度、その他の条件により任意に選択すればよいが、可
及的高濃度藻培養液を出発液とし、例えば、2g/を出
発液とすれば、2日で2倍濃度となる。さらに、半量を
出発槽に戻して半量分の新鮮培地を追加し、培養を続行
すればよい。
The concentration of the initial algal solution and the ratio of the amount of the cultured algal solution to be withdrawn may be arbitrarily selected depending on the culture speed and other conditions, but the highest concentration algal culture solution is used as a starting solution, for example, starting at 2 g /. If the solution is used, the concentration becomes twice in two days. Further, half of the amount may be returned to the starting tank, half of the fresh medium may be added, and the culture may be continued.

管の末端で藻濃度が2倍になるように流速、管の長さ
を調節すれば、単に管を通過させるだけでよいが、管の
長さをこの半分にすれば2回循環させた後、半量を引き
出して、新鮮培地を追加し培養を続ける。藻濃度は分光
光度計680nmで測定し、初発濃度の2倍の吸光度に達っ
したら、自動的に半量を引出し、半量の新鮮培地を加え
るようにセットすればよい。
If the flow rate and the length of the tube are adjusted so that the algal concentration is doubled at the end of the tube, it is sufficient to simply pass through the tube. Draw out half, add fresh medium and continue culturing. The algae concentration is measured with a spectrophotometer 680 nm, and when the absorbance reaches twice the initial concentration, half of the algae can be automatically withdrawn and set so that half of the fresh medium is added.

藻の種類としては微細藻のChlorella(クロレラ)Sce
nedesmus(イカダモ)、Spirulina(スピルリナ)、Por
phyridium(チノリモ)、Nostoc(ネンジュモ)、Chlam
ydomonas(クラミドモナス)など多くの種類があるが管
の中を通過できるものであれば、いずれでも本発明のシ
ステムを用いた培養方法が適用できる。また、これらを
二種以上混合して培養することもできる。同様にして緑
藻、褐藻、紅藻などの大型藻でも管の径を大きくする
か、平板を用いるなど通過を可能にすれば本発明の方法
が適用できる。
The kind of algae is Chlorella (Chlorella) Sce
nedesmus, Spirulina, Por
phyridium, Nostoc, Chlam
Although there are many types such as ydomonas (Chlamydomonas), any culture method using the system of the present invention can be applied as long as it can pass through a tube. Further, two or more of these can be mixed and cultured. Similarly, the method of the present invention can be applied to large algae such as green algae, brown algae and red algae as long as the diameter of the tube is increased or the passage is enabled by using a flat plate.

また、変異させたクロレラなど従属栄養藻類も同様に
本発明のシステムを効果的に適用でき、炭素源を加えた
滅菌培地を用いて培養することにより、連続的に本藻類
を生産できる。
Heterotrophic algae such as mutated chlorella can also be effectively applied to the system of the present invention, and the algae can be continuously produced by culturing using a sterile medium containing a carbon source.

[実施例] 次に実施例を以て本発明をさらに詳細かつ具体的に説
明するが、これらに限定されるものではない。
EXAMPLES Next, the present invention will be described in more detail and specifically with reference to Examples, but it should not be construed that the invention is limited thereto.

実施例1 藻としてはspirulina platensis(環境科学研究協議
会、保存菌株No.39)、培地としてSOT培地を用い、2,50
0Luxの蛍光灯ランプ照射下、25℃、4m/minの流速で培
養した。システムは図1のような円形であり、厚さ200
μm、管径3.6×4.0mmのシリコン管10mをアルミ箔上に
セットし、培地供給装置を付けた200mの貯槽に液面を
1cm以下にしたものである。2mg/m濃度の藻液を(培地
供給装置を除く)システム全体に満たし、ペリスタリッ
クポンプを用いて循環培養した結果、表1のように、2
日で2倍の藻濃度になった。
Example 1 As algae, spirulina platensis (conservation strain No.39, Environmental Science Research Council) and SOT medium as medium, 2,50
The cells were cultured under a 0 Lux fluorescent lamp at 25 ° C. at a flow rate of 4 m / min. The system is circular as shown in FIG.
Set a 10-μm silicon tube with a diameter of 3.6 × 4.0 mm on an aluminum foil, and place the liquid level in a 200-m storage tank equipped with a medium supply device.
It is less than 1cm. As a result of filling the entire system with a 2 mg / m concentration algal solution (excluding the medium supply device) and circulating the culture using a peristaltic pump, as shown in Table 1,
The algal concentration doubled in a day.

実施例2 厚さ100μm、管径3.0×3.2mmのシリコン管10mをアル
ミ箔上にセット(0.04m2)、藻濃度を0.5mg/mにした
以外は、実施例1と同様にして培養したところ、1日で
3倍の藻濃度になった。
Example 2 Culture was carried out in the same manner as in Example 1 except that a silicon tube 10 m having a thickness of 100 μm and a diameter of 3.0 × 3.2 mm was set on an aluminum foil (0.04 m 2 ) and the algal concentration was set to 0.5 mg / m. However, the algal concentration tripled in one day.

実施例3 藻濃度を1mg/mにし、過度な乾燥を防止するために
水蒸気飽和チャンバー内で実施例1と同様に培養した結
果、3日で5倍の藻濃度になった。
Example 3 Algae concentration was set to 1 mg / m, and culturing was carried out in a water vapor saturation chamber in the same manner as in Example 1 in order to prevent excessive drying. As a result, the algal concentration was increased five times in 3 days.

実施例4 藻濃度を0.5mg/mにして、シリコン管の中間に1/2希
釈培地の補給装置を付けた以外は実施例1と同様にして
循環培養した結果、2日で5倍の藻濃度になった。
Example 4 Circular culture was performed in the same manner as in Example 1 except that the concentration of algae was 0.5 mg / m, and a supply device for a 1/2 dilution medium was provided in the middle of a silicon tube. Concentration.

実施例5 藻としてはSpirulina platensis(環境科学研究協議
会、保存菌株No.39)、藻濃度を0.5mg/mにし、厚さ20
0μm、管径3.6×4.0mmのシリコン管、230mをアクリル
板にセットし、スペース5〜10cmとって、5段にし、各
段毎に、通常の藻培養液に用いる1/2〜1/10の濃度のリ
ン酸カリウム、尿素を含む希薄培地供給装置を付け、流
速2m/minで培養した結果、2日培養後から5mg/mが2
m/minで得られた。また、この藻液を同じシリコン管
に35℃、乾燥状態で通過させると10mで1/4まで濃縮され
ミルク状藻液が得られた。
Example 5 As algae, Spirulina platensis (Environmental Research Council, stock strain No. 39), the algal concentration was 0.5 mg / m, and the thickness was 20
0 μm, a silicon tube with a pipe diameter of 3.6 × 4.0 mm, 230 m is set on an acrylic plate, and a space of 5 to 10 cm is taken to form 5 stages, and for each stage, 1/2 to 1/10 used for a normal algal culture solution The culture was performed at a flow rate of 2 m / min with a diluted medium supply device containing potassium phosphate and urea at a concentration of 5 mg / m.
m / min. When this algal solution was passed through the same silicon tube in a dry state at 35 ° C., it was concentrated to 1/4 at 10 m to obtain a milky algal solution.

実施例6 藻濃度1mg/mで実施例1と同様に培養後、排除限界
分子量20万の限外濾過膜で2倍に濃縮、新鮮培地を追加
して、さらに1日培養を続け、5倍濃度になった。
Example 6 After culturing at an algal concentration of 1 mg / m in the same manner as in Example 1, doubling the concentration with an ultrafiltration membrane having an exclusion limit molecular weight of 200,000, adding a fresh medium, and continuing culturing for another day, 5 fold Concentration.

実施例7 1mg/mのクロレラ(Chlorella regularis)を、炭素
源として酢酸、酢酸ナトリウム、窒素源として尿素を用
いた培地で実施例1と同様のシステムを用い、35℃で暗
所、貯槽から、酢酸、酢酸ナトリウムを添加しながら循
環培養した結果、24時間で10mg/mの藻液が得られた。
Example 7 1 mg / m of Chlorella regularis was prepared by using a system similar to that of Example 1 in a medium using acetic acid, sodium acetate, and urea as a nitrogen source at 35 ° C. As a result of circulating culture while adding acetic acid and sodium acetate, an algal solution of 10 mg / m was obtained in 24 hours.

[発明の効果] 本発明のシステムを用いた培養方法によれば、これま
で困難であった、高濃度藻培養液が効率的、連続的に生
産でき、本藻液は各種の方法により濃縮され、藻濃度1
〜2%でミルク状にして液状食品への応用、さらに濃縮
して、藻濃度10〜12%でクリーム状にすれば調理、味付
けし佃煮風食品とすることができる。また、サイクロデ
キストリンおよび/またはデキストリン、オリゴ糖など
と混合して噴霧乾燥し粉体とすることもできるし、シリ
コンなどの通気性膜上に薄く広げてシート状に乾燥して
ノリとすることもできるなど用途は広い。
[Effects of the Invention] According to the culture method using the system of the present invention, a high-concentration algal culture solution that has been difficult until now can be efficiently and continuously produced, and the algal solution is concentrated by various methods. , Algae concentration 1
It can be cooked and seasoned to make a tsukudani-style food by applying it to a liquid food by making it into a milky form at ~ 2% and further concentrating it into a creamy form with an algal concentration of 10 to 12%. It can also be mixed with cyclodextrin and / or dextrin, oligosaccharide, etc. and spray-dried into powder, or spread thinly on a gas-permeable membrane such as silicon and dried into a sheet to form glue. Applications are wide such as possible.

藻濃度15〜20%まで濃縮すれば、チーズ状になるの
で、このまま、または色素を除去して各種食品素材とし
て利用できる。
If concentrated to an algal concentration of 15 to 20%, it becomes cheese-like, and can be used as it is or after removing pigments as various food materials.

この他、培養藻は多糖、糖質、脂質、ビタミン、生理
活性物質などの抽出用原料ともなり、抽出物質は機能
性、健康食品、一般食品素材としてもりようできる。
In addition, the cultured algae can be used as a raw material for extracting polysaccharides, carbohydrates, lipids, vitamins, physiologically active substances, and the like, and the extracted substance can be used as a functional, health food, or general food material.

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

第1図はシリコン管を円形と角形に板状にセットしたシ
ステム全体を示したものである。本システムは培養管を
中心とし、貯槽(リザーブタンク)、培地または水供給
装置(補助培地タンク)、濃縮または透析装置(培地交
換、濃縮システム)、自動濃度センサーからなり、必要
に応じて組み合わせることができる。
FIG. 1 shows the entire system in which silicon tubes are set in a circular and square plate shape. This system mainly consists of a culture tube, a storage tank (reservoir tank), a medium or water supply device (auxiliary medium tank), a concentration or dialysis device (medium exchange, concentration system), and an automatic concentration sensor, which can be combined as necessary. Can be.

フロントページの続き (72)発明者 藤沢 和也 兵庫県神戸市中央区中山手通7丁目36番 5号 (56)参考文献 特開 昭51−110089(JP,A) 特開 昭56−61988(JP,A) (58)調査した分野(Int.Cl.6,DB名) C12N 1/00 - 7/08 C12M 1/00 - 3/10 Continuation of the front page (72) Inventor Kazuya Fujisawa 7-36-5 Nakayamate-dori, Chuo-ku, Kobe-shi, Hyogo (56) References JP-A-51-110089 (JP, A) JP-A-56-61988 ( JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) C12N 1/00-7/08 C12M 1/00-3/10

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】シリコン製の管状通気性膜もしくは基材の
外表面に固定してある該管状通気性膜に連続的に藻類接
種培地および/または新鮮な液体培地を供給して藻類を
培養し、培養済みの藻類液を順次系外に引き出すことを
特徴とする藻類の連続的培養方法。
An algal inoculation medium and / or a fresh liquid medium are continuously supplied to a tubular gas-permeable membrane made of silicon or a tubular gas-permeable membrane fixed on the outer surface of a substrate to culture algae. A method for continuously culturing algae, wherein the cultivated algal solution is sequentially drawn out of the system.
【請求項2】藻類培養液を透析または濃縮して生育阻害
物質を除去しながら培養する請求項1記載の培養方法。
2. The method according to claim 1, wherein the algal culture is dialyzed or concentrated to remove the growth-inhibiting substance and cultured.
JP2047200A 1990-03-01 1990-03-01 Algae cultivation method using silicon Expired - Fee Related JP2984749B2 (en)

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JP2984749B2 true JP2984749B2 (en) 1999-11-29

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102009028338A1 (en) 2009-08-07 2011-02-10 Wacker Chemie Ag Bioreactor with silicone coating
DE102009028339A1 (en) * 2009-08-07 2011-02-24 Wacker Chemie Ag Bioreactor made of silicone materials
JP2014060967A (en) * 2012-09-21 2014-04-10 Kobelco Eco-Solutions Co Ltd Fine algae culture method and fine algae culture facility
JP5899100B2 (en) * 2012-10-11 2016-04-06 株式会社神鋼環境ソリューション Microalgae culture apparatus and microalgae culture method
JP2016202033A (en) * 2015-04-17 2016-12-08 寿和 池田 Algae cultivation facility and algae cultivation method
US10584310B2 (en) * 2017-03-08 2020-03-10 Ivan Araujo Dayrell Integrated system to produce microalgae

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