JP2615393B2 - Closed algae culture system - Google Patents

Closed algae culture system

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Publication number
JP2615393B2
JP2615393B2 JP12146488A JP12146488A JP2615393B2 JP 2615393 B2 JP2615393 B2 JP 2615393B2 JP 12146488 A JP12146488 A JP 12146488A JP 12146488 A JP12146488 A JP 12146488A JP 2615393 B2 JP2615393 B2 JP 2615393B2
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JP
Japan
Prior art keywords
culture system
measuring
carbon dioxide
closed
algal
Prior art date
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Expired - Lifetime
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JP12146488A
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Japanese (ja)
Other versions
JPH01291783A (en
Inventor
敦弘 嶋田
茂夫 藤井
喬 小谷野
美津夫 小口
孔治 大坪
慶治 新田
Original Assignee
科学技術庁航空宇宙技術研究所長
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/02Photobioreactors
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M31/00Means for providing, directing, scattering or concentrating light
    • C12M31/08Means for providing, directing, scattering or concentrating light by conducting or reflecting elements located inside the reactor or in its structure
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/30Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration
    • C12M41/34Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration of gas

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  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Zoology (AREA)
  • Genetics & Genomics (AREA)
  • Biotechnology (AREA)
  • Microbiology (AREA)
  • Sustainable Development (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • Molecular Biology (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] この発明は、閉鎖系内で藻類を連続的に培養するため
の装置に関する。
Description: TECHNICAL FIELD The present invention relates to an apparatus for continuously culturing algae in a closed system.

[従来の技術] スペースシャトル等を用いた宇宙開発が行なわれてい
るが、この場合、乗員のための食料及び酸素の確保が問
題となる。もし、例えばスピルリナのような食用に供す
ることができる藻類をスペースシャトルや宇宙ステーシ
ョン内で培養することができれば食料と酸素を同時に得
ることができるので非常に好都合である。
[Prior Art] Space development using a space shuttle or the like is performed, but in this case, securing food and oxygen for occupants becomes a problem. If edible algae such as spirulina can be cultured in a space shuttle or space station, it would be very convenient to obtain food and oxygen simultaneously.

宇宙において藻類を培養する場合、無重力下で培養す
ることになるので、閉鎖系で培養することが必要にな
る。また、長期間にわたって連続的に培養することがで
きるものが好ましい。藻類を閉鎖系において長期間にわ
たって連続的に培養する場合、藻体濃度の調節、藻体の
回収及び培地の添加、培養液のpHの調節及び二酸化炭素
の培養液中への添加、発生する酸素の回収ならびに圧力
調節等、開放系のバッチ式装置では問題とはならない種
々の問題がある。
When cultivating algae in space, the cultivation is performed under zero gravity, so it is necessary to culture in a closed system. Further, those capable of continuously culturing for a long period of time are preferable. When algae are continuously cultured in a closed system for a long period of time, the concentration of alga bodies is adjusted, the alga bodies are collected and a medium is added, the pH of the culture medium is adjusted and carbon dioxide is added to the culture medium, and the oxygen generated There are various problems, such as recovery and pressure control, which are not problems in an open batch type apparatus.

従来、クロレラ等の微細藻類の培養装置としてはバッ
チ式のものは数多くあり、その中では光供給方法や二酸
化炭素供給方法に特徴を持たせたものがある。また、そ
れらをコンピューターによってコントロールさせるもの
も考案されている。しかしながら、長期連続培養を目的
として、藻体回収、倍地添加装置を持ち、酸素を分離で
きる閉鎖系の培養装置はない。
2. Description of the Related Art Conventionally, there are many batch-type microalgae culturing apparatuses such as chlorella, and among them, there are apparatuses having characteristics in a light supply method and a carbon dioxide supply method. Computers that control them by computer have also been devised. However, for the purpose of long-term continuous cultivation, there is no closed-system cultivation apparatus that has an alga recovery and medium addition device and can separate oxygen.

[発明が解決しようとする問題点] 従って、この発明の目的は、藻類を閉鎖系にて長期に
わたって連続培養し、藻体及び酸素を連続的に回収する
ことができる、閉鎖系藻類培養装置を提供することであ
る。
[Problems to be Solved by the Invention] Accordingly, an object of the present invention is to provide a closed algae culture apparatus capable of continuously culturing algae in a closed system for a long period of time and continuously collecting algal cells and oxygen. To provide.

[問題点を解決するための手段] この発明は、培養槽と該培養槽を介して閉じた管路と
から成る閉鎖培養系と、該閉鎖培養系内に培養物を循環
させる手段と、該閉鎖培養系内の圧力を測定する手段
と、前記閉鎖培養系内の二酸化炭素の量を測定する手段
と、前記閉鎖培養系内で培養される藻体の密度を測定す
る手段と、前記閉鎖培養系から藻体を回収する手段と、
前記閉鎖培養系に培地を供給する手段と、前記閉鎖培養
系に二酸化炭素を供給する手段と、前記閉鎖培養系から
酸素を回収する手段とを含む閉鎖系藻類培養装置を提供
する。
[Means for Solving the Problems] The present invention provides a closed culture system comprising a culture tank and a pipe line closed through the culture tank, means for circulating the culture in the closed culture system, Means for measuring the pressure in the closed culture system, means for measuring the amount of carbon dioxide in the closed culture system, means for measuring the density of algal cells cultured in the closed culture system, and the closed culture Means for recovering algae from the system;
Provided is a closed algal culture apparatus comprising: means for supplying a medium to the closed culture system; means for supplying carbon dioxide to the closed culture system; and means for recovering oxygen from the closed culture system.

[発明の効果] この発明により、藻類を閉鎖系にて長期にわたって連
続培養し、藻体及び酸素を連続的に回収することができ
る、閉鎖系藻類培養装置が提供された。この発明の装置
を用いると、どのような外部環境下においても藻体と酸
素とを同時に連続的に得ることができる。従って、この
発明の装置を用いてスペースシャトルや宇宙ステーショ
ン等において食用に供することができる藻類を培養する
と、乗員の食料となる藻体と酸素とを同時に連続的に得
ることができ、極めて有利である。
[Effects of the Invention] According to the present invention, there is provided a closed algae culture apparatus capable of continuously culturing algae in a closed system for a long period of time and continuously collecting algal bodies and oxygen. By using the device of the present invention, algal cells and oxygen can be simultaneously and continuously obtained under any external environment. Therefore, when cultivating edible algae in a space shuttle, a space station, or the like using the device of the present invention, algal bodies and oxygen serving as food for the occupant can be simultaneously and continuously obtained, which is extremely advantageous. is there.

[発明の具体的説明] この発明の培養装置は、培養槽と、該培養槽を介して
閉じた管路とから成る閉鎖培養系を含む。培養槽の寸
法、形状、構造等は何ら制限されるものではなく、培養
規模や外部環境その他の条件により適宜選択することが
できる。培養槽を透明の材質で形成し、太陽光を利用し
て藻類を培養することもできるが、どのような条件下で
も培養することができることを確保するために、培養槽
には光源を設けることが好ましい。光源はどのようなも
のであってもよいが、光ファイバーの束を培養槽の中に
挿入し、培養槽外にある光源からの光を光ファイバーに
導いて藻類に光を与える構成のものが培養槽に不要の熱
を与えず、また、フィルターを用いて容易に紫外線をカ
ットできるので好ましい。また、培養槽は、槽内の培養
物を撹拌するための手段を有していることが好ましい。
撹拌手段は撹拌板のようなものでも良いが、光の供給の
観点から培養層内には何もないことが好ましいので、培
養槽に入る管路を複数個に分岐させ、管路から培養槽内
に流入する培養物自身の流れによって培養槽内の培養物
を撹拌する構成のものが好ましい。
[Specific description of the invention] The culture apparatus of the present invention includes a closed culture system including a culture tank and a pipeline closed through the culture tank. The size, shape, structure, and the like of the culture tank are not limited at all, and can be appropriately selected depending on the culture scale, external environment, and other conditions. The culture tank is made of a transparent material, and the algae can be cultured using sunlight.However, in order to ensure that the culture can be performed under any conditions, the culture tank should be provided with a light source. Is preferred. The light source may be of any type, but the one that inserts a bundle of optical fibers into the culture tank and guides light from the light source outside the culture tank to the optical fiber to give light to algae is a culture tank. This is preferable because unnecessary heat is not applied to the filter and ultraviolet rays can be easily cut off using a filter. The culture tank preferably has a means for stirring the culture in the tank.
The stirring means may be a stirring plate, but it is preferable that there is nothing in the culture layer from the viewpoint of light supply. It is preferable that the culture in the culture tank is stirred by the flow of the culture itself flowing into the inside.

上記培養槽と管路とから成る閉鎖培養系には、該閉鎖
培養系内に培養物を循環させる手段が設けられている。
培養物を循環させる手段は、例えば管路に直列に挿入さ
れたポンプであってよい。
The closed culture system including the culture tank and the pipe is provided with a means for circulating the culture in the closed culture system.
The means for circulating the culture may be, for example, a pump inserted in series in the pipeline.

上記閉鎖培養系には、系内の圧力を測定する手段が設
けられている。このような手段の例として、例えば培養
層に設置された圧力計を挙げることができる。
The closed culture system is provided with a means for measuring the pressure in the system. As an example of such means, for example, a pressure gauge installed in a culture layer can be mentioned.

上記閉鎖培養系にはさらに、閉鎖培養系内で培養され
る藻体の密度を測定する手段が設けられている。藻体の
密度に測定するための手段としては例えば管路に直列に
挿入された濁度計を挙げることができる。
The closed culture system is further provided with a means for measuring the density of algal cells cultured in the closed culture system. As a means for measuring the algal density, for example, a turbidity meter inserted in series in a pipe can be mentioned.

上記閉鎖培養系にはまた、培養系から藻体を回収する
手段が設けられている。藻体を回収する手段としては、
上記管路から分岐した分岐管を設け、この分岐管に例え
ば円筒上のフィルターとポンプを直列に設けたものを挙
げることができる。
The closed culture system is also provided with a means for collecting algal cells from the culture system. As means for collecting algal bodies,
A branch pipe branched from the above-mentioned conduit is provided, and for example, a pipe provided with a filter and a pump on a cylinder in series is provided in this branch pipe.

上記閉鎖培養系にはさらに、該培養系に培地を供給す
る手段が設けられている。培地を供給する手段として
は、上記管路から分岐した分岐管を設け、この分岐管に
培地タンクとポンプとを直列に設けたものを挙げること
ができる。
The closed culture system is further provided with a means for supplying a medium to the culture system. As a means for supplying the culture medium, there may be mentioned a means in which a branch pipe branched from the above-mentioned conduit is provided, and a medium tank and a pump are provided in series in the branch pipe.

さらに、上記閉鎖培養系には、該閉鎖培養系に二酸化
炭素を与えるための手段が設けられている。二酸化炭素
を与える手段としては、例えば、気体を通すが液体は通
さない大きさの孔を多数有するファイバーの束(以下、
ホローファイバーという)を管路に直列に挿入し、か
つ、該ホローファイバーに二酸化炭素を与えるために弁
及び流量計を介して二酸化炭素ボンベを連結したものを
挙げることができる。なお、ここで用いるホローファイ
バーは市販のものを用いることができる。
Further, the closed culture system is provided with a means for supplying carbon dioxide to the closed culture system. As a means for giving carbon dioxide, for example, a bundle of fibers having a large number of holes that allow gas to pass but not liquid (hereinafter, referred to as a fiber bundle)
Hollow fiber) is inserted in series in a pipe, and a carbon dioxide cylinder is connected to the hollow fiber via a valve and a flow meter in order to supply carbon dioxide to the hollow fiber. The hollow fiber used here can be a commercially available one.

さらに、上記閉鎖培養系には、該培養系から酸素を回
収するための手段が設けられている。酸素を回収するた
めの手段としては、上記管路に直列にホローファイバー
を挿入し、該ホローファイバーに気体ポンプと酸素蓄積
ボンベを直列に連結したものを挙げることができる。こ
の場合、酸素流量計、二酸化炭素流量計及び気体流量を
直列に挿入しておくと、回収された酸素の量及びその二
酸化炭素含量を知ることができるので好ましい。
Further, the closed culture system is provided with means for recovering oxygen from the culture system. As a means for recovering oxygen, a hollow fiber may be inserted in series in the above-mentioned conduit, and a gas pump and an oxygen storage cylinder may be connected in series to the hollow fiber. In this case, it is preferable to insert an oxygen flow meter, a carbon dioxide flow meter, and a gas flow in series, since the amount of recovered oxygen and its carbon dioxide content can be known.

さらに、上記閉鎖培養系には、その温度を調節する温
度調節器を設けておくことが好ましい。
Further, the closed culture system is preferably provided with a temperature controller for controlling the temperature.

次に上記装置の操作方法を説明する。通常の培養時に
は、培養槽に光を当てながら、上記閉鎖培養系内に培養
物を循環させる手段、例えはポンプを作動させて閉鎖培
養系内に培地及び藻体を含む培養物を循環させる。この
際、閉鎖培養系内の藻体の密度、圧力及び二酸化炭素量
は常時モニターする。また、酸素回収手段は常時作動さ
せて培養系内で生じた酸素を常時回収する。すなわち、
酸素回収手段が上記管路に直列にホローファイバーを挿
入し、該ホローファイバーに気体ポンプと酸素蓄積ボン
ベを直列に連結したものである場合には、気体ポンプを
常時引いてホローファイバーにより気液分離を行なう。
藻体は、培養槽内で光合成を行ない増殖する。
Next, a method of operating the above-described device will be described. During normal culture, a means for circulating the culture in the closed culture system, for example, operating a pump, circulates the culture containing the medium and algal cells in the closed culture system while irradiating the culture tank with light. At this time, the density, pressure and carbon dioxide amount of the algal cells in the closed culture system are constantly monitored. Further, the oxygen recovery means is constantly operated to constantly recover oxygen generated in the culture system. That is,
When the oxygen recovery means is a hollow fiber inserted in series in the above-mentioned conduit, and a gas pump and an oxygen storage cylinder are connected in series to the hollow fiber, the gas pump is constantly pulled to separate the gas and liquid by the hollow fiber. Perform
Algae undergo photosynthesis in the culture tank and proliferate.

藻体が増殖した結果、藻体の密度が一定値以上、例え
ば培養初期の30%増になったことが濁度計等の藻体密度
測定手段により示された場合には、藻体を回収すると共
に培地を添加する。すなわち、藻体回収手段が管路から
分岐した分岐管を設け、この分岐管に例えば円筒上のフ
ィルターとポンプとを直列に設けたものであり、上記培
地供給手段が上記管路から分岐した分岐管を設け、この
分岐管に培地タンクとポンプとを直列に設けたものであ
る場合には、藻体回収手段のポンプを作動させて上記フ
ィルターで培養物を濾し取ると同時に、培地供給手段の
ポンプを作動させて培地タンクから閉鎖培養系に培地の
供給を行なう。フィルターによって藻体から分離された
使用済みの培地はタンクに蓄えて廃棄することもできる
し、所望により閉鎖培養系内に再循環させることもでき
る。
As a result of the algal body multiplying, if the algal body density measurement means such as a turbidity meter indicates that the algal body density has increased by a certain value or more, for example, 30% in the initial stage of the culture, the algal body is collected. And add medium. That is, the algal body collecting means is provided with a branch pipe branched from the pipe, and the branch pipe is provided with, for example, a filter and a pump on a cylinder in series, and the medium supply means is branched from the pipe. In the case where a pipe is provided, and a medium tank and a pump are provided in series in this branch pipe, the pump of the alga body recovery means is operated to filter the culture with the filter, and at the same time, the medium supply means is provided. The pump is operated to supply the medium from the medium tank to the closed culture system. The used medium separated from the algal cells by the filter can be stored in a tank and discarded, or can be recirculated into a closed culture system if desired.

閉鎖培養系内の圧力を測定する手段により、培養系内
の圧力が一定値以上になったことが示された場合には、
上記藻体回収手段を作動させて藻体のみを回収する。ま
た、培養系内の圧力が一定値以下になったことが示され
た場合には、上記培地供給手段を作動させて培地のみを
培養系に供給する。
When the means for measuring the pressure in the closed culture system indicates that the pressure in the culture system has exceeded a certain value,
The algal body collecting means is operated to collect only the algal bodies. Further, when it is indicated that the pressure in the culture system has become equal to or less than a certain value, the medium supply means is operated to supply only the medium to the culture system.

また、上記二酸化炭素測定手段、例えばpHメーターに
より培養系内の二酸化炭素濃度が不足したこと(pHが一
定値以上に高くなったこと)が示された時には上記二酸
化炭素供給手段から二酸化炭素が供給される。
When the carbon dioxide measuring means, for example, a pH meter indicates that the concentration of carbon dioxide in the culture system is insufficient (the pH has become higher than a certain value), carbon dioxide is supplied from the carbon dioxide supplying means. Is done.

このようにして、培養系から酸素が回収され、藻体の
密度が一定値以上になったときには藻体が回収されて培
地が供給され、一定圧力以上になった時には藻体のみが
回収され、一定圧力以下になった場合には培地のみが供
給され、閉鎖培養系内は常に一定範囲の条件下に保た
れ、藻体の培養並びに酸素及び藻体の回収が連続的に行
なわれる。
In this way, oxygen is recovered from the culture system, and when the density of the algal body is higher than a certain value, the algal body is recovered and the medium is supplied, and when the pressure is higher than a certain pressure, only the alga body is recovered, When the pressure falls below a certain pressure, only the medium is supplied, the inside of the closed culture system is always kept under a certain range of conditions, and the cultivation of algal cells and the recovery of oxygen and algal cells are performed continuously.

上記操作は手動的に行なうこともできるが、労力を少
なくするためにコンピューターを用いて自動制御により
行なうことが好ましい。すなわち、各測定手段(圧力、
藻体密度及び二酸化炭素濃度並びに所望により酸素濃
度、酸素流量、二酸化炭素流量及び濃度)からの計測値
全てをコンピューターにオンラインで入力し、現在のラ
ンの状態をCRT画面に表示させると共に、経時的変化を
折れ線グラフで表わし、さらに、二酸化炭素測定手段と
二酸化炭素供給手段、藻体密度測定手段と藻体回収手段
及び培地供給手段、圧力測定手段と藻体回収手段及び培
地供給手段を連動させてコンピューターにより自動制御
を行なうことが好ましい。このようにして、藻体の培養
並びに藻体の回収及び酸素の回収、培地の供給、二酸化
炭素の供給を全自動で連続的に行なうことができる。
The above operation can be performed manually, but is preferably performed by automatic control using a computer in order to reduce labor. That is, each measuring means (pressure,
All measured values from algal density and carbon dioxide concentration and, if desired, oxygen concentration, oxygen flow rate, carbon dioxide flow rate and concentration) are input to the computer online, and the current run status is displayed on the CRT screen, The change is represented by a line graph, and further, the carbon dioxide measuring means and the carbon dioxide supplying means, the algal body density measuring means and the algal body collecting means and the medium supplying means, the pressure measuring means and the algal body collecting means and the medium supplying means are linked to each other. It is preferable to perform automatic control by a computer. In this manner, the cultivation of the algal cells, the recovery of the algal cells and the recovery of oxygen, the supply of the culture medium, and the supply of carbon dioxide can be continuously performed automatically.

この発明の装置により培養される藻類は、特に限定さ
れるものではなく、いずれの藻類をも培養することがで
きる。また、培地の組成や培養温度は培養する藻類に応
じて適宜決定される。
The algae cultured by the apparatus of the present invention are not particularly limited, and any algae can be cultured. Further, the composition of the medium and the culture temperature are appropriately determined according to the algae to be cultured.

[実施例] 以下、この発明を実施例に基づいてより具体的に説明
する。この発明の装置は以下に記載する実施例の他にも
種々の態様が可能であることは明らかであり、以下の実
施例に限定されるものではない。
EXAMPLES Hereinafter, the present invention will be described more specifically based on examples. It is clear that the device of the present invention can be variously modified in addition to the embodiments described below, and is not limited to the following embodiments.

添付の図面はこの発明の装置の好ましい1実施例を示
す。図示の装置は培養槽10及び培養槽10を介して閉じた
管路12から成る閉鎖培養を含む。管路12にはポンプ14が
挿入され、培養槽10及び管路12内の培養物は矢印aの方
向に循環する。培養槽には圧力計16が設置されている。
培養槽に入る管路12の部分は3つに分岐しており、流入
する培養物自身の流れによって培養槽内の培養が撹拌さ
れる。培養槽10には光源18から延びた光ファイバーの束
20が挿入されており、光源18からの光が光ファイバーの
束20を通して培養槽10内に与えられる。
The accompanying drawings show a preferred embodiment of the device of the present invention. The illustrated apparatus includes a closed culture consisting of a culture vessel 10 and a conduit 12 closed through the culture vessel 10. A pump 14 is inserted into the pipe 12, and the culture in the culture tank 10 and the pipe 12 circulates in the direction of arrow a. A pressure gauge 16 is provided in the culture tank.
The portion of the conduit 12 entering the culture tank is branched into three, and the culture in the culture tank is agitated by the flow of the inflow culture itself. The culture tank 10 has a bundle of optical fibers extending from a light source 18.
20 is inserted, and light from the light source 18 is supplied into the culture tank 10 through a bundle 20 of optical fibers.

管路12には、pHメーター22、ホローファイバーから成
る酸素分離器24、ホローファイバーから成る二酸化炭素
供給器26、濁度計28及び温度調節器30がそれぞれ直列に
挿入されている。酸素分離器24には気体ポンプ32、酸素
流量計34、二酸化炭素流量計36、気体流量計38及び酸素
貯蔵ボンベ40が直列に配置されている。二酸化炭素供給
器26には、二酸化炭素ボンベ42、弁44及び気体流量計46
が直列に接続されている。
A pH meter 22, an oxygen separator 24 composed of hollow fibers, a carbon dioxide feeder 26 composed of hollow fibers, a turbidity meter 28, and a temperature controller 30 are inserted in series in the pipe 12, respectively. In the oxygen separator 24, a gas pump 32, an oxygen flow meter 34, a carbon dioxide flow meter 36, a gas flow meter 38, and an oxygen storage cylinder 40 are arranged in series. The carbon dioxide supply device 26 includes a carbon dioxide cylinder 42, a valve 44, and a gas flow meter 46.
Are connected in series.

管路12からは第1の分岐管48が分岐し、この分岐管48
には電磁弁50を介してポンプ52及び藻体回収器54が直列
に配置されている。電磁弁50は図示のA→C又はB→C
いずれか一方に通路を開くものである。電磁弁50のBに
は空気貯蔵器51が連結されている。藻体回収器54は円筒
上のフィルター56を含む。藻体回収器54で回収された藻
体は藻体貯蔵容器58内に貯蔵される。藻体回収器54の出
口側にはポンプ60及び廃棄物タンク62が直列に連結さ
れ、また藻体回収器54の入り口側には水タンク64、ポン
プ66及び弁68が直列に接続されている。
A first branch pipe 48 branches from the pipe 12, and this branch pipe 48
, A pump 52 and an algal body collector 54 are arranged in series via an electromagnetic valve 50. Solenoid valve 50 is A → C or B → C shown
A passage is opened in either one. An air reservoir 51 is connected to B of the solenoid valve 50. Algae collector 54 includes a filter 56 on a cylinder. The algal bodies collected by the algal body collecting device 54 are stored in the algal body storage container 58. A pump 60 and a waste tank 62 are connected in series on the outlet side of the algal body recovering unit 54, and a water tank 64, a pump 66 and a valve 68 are connected in series on the inlet side of the algal body collecting unit 54. .

また、管路12からは第2の分岐管70が分岐し、分岐管
70には電磁弁72が接続されている。電磁弁72はA→B又
はA→Cいずれか一方に通路を開くものである。電磁弁
72のAには管路70aが接続され、管路70aは上記ポンプ52
及び培地タク74を介して電磁弁72のBに接続している。
Also, a second branch pipe 70 branches from the pipe 12 and
An electromagnetic valve 72 is connected to 70. The solenoid valve 72 opens a passage in either A → B or A → C. solenoid valve
A pipe 70a is connected to A of 72, and the pipe 70a is connected to the pump 52.
And the medium valve 74 is connected to B of the solenoid valve 72.

圧力計16、pHメーター22、濁度計28、酸素流量計34、
二酸化炭素流量計36及び気体流量計38からの計測値は全
てコンピューターにオンラインで入力され、CRT画面に
表示される。また、各計測値の変化も、折れ線グラフと
してCRT画面上に表示される。
Pressure gauge 16, pH meter 22, turbidity meter 28, oxygen flow meter 34,
All the measured values from the carbon dioxide flow meter 36 and the gas flow meter 38 are input online to the computer and displayed on the CRT screen. Also, the change of each measurement value is displayed on the CRT screen as a line graph.

さらに、濁度計28とポンプ52、60及び電磁弁50及び7
2;pHメーター22と弁44;圧力計16とポンプ52、60及び電
磁弁50、72がそれぞれコンピューターを介して電気的に
持続されている。
Further, the turbidity meter 28, the pumps 52 and 60 and the solenoid valves 50 and 7
2; the pH meter 22 and the valve 44; the pressure gauge 16, the pumps 52 and 60, and the solenoid valves 50 and 72 are electrically maintained via a computer, respectively.

次に上記装置の操作方法を説明する。通常の培養時に
は、光源18からの光を光ファイバーの束20を介して培養
槽10に与えながらポンプ14を作動させて培養槽10及び管
路12内に藻体及び培地を含む培養物を矢印aの方向に循
環させる。この時、電磁弁50はB→C、電磁弁72はA→
Bに開いており、ポンプ52及び60は停止しているので分
岐管48及び70内には培養物は流通しない。培養時には圧
力計16、pHメーター22及び濁度計28は常時作動してお
り、その計測値は上述のようにオンラインでコンピュー
ターに入力される。培養系の温度は温度調節器30によっ
て所望の温度に維持される。また、気体ポンプ32は作動
しており、酸素分離器24によって酸素が分離され、酸素
貯蔵ボンベ40に蓄積される。
Next, a method of operating the above-described device will be described. During normal culture, the pump 14 is operated while supplying light from the light source 18 to the culture tank 10 through the bundle of optical fibers 20, and the culture containing the alga bodies and the medium in the culture tank 10 and the conduit 12 is indicated by an arrow a. Circulate in the direction of. At this time, the solenoid valve 50 is B → C, the solenoid valve 72 is A →
Since the pump is open to B and the pumps 52 and 60 are stopped, the culture does not flow through the branch pipes 48 and 70. During the culture, the pressure gauge 16, the pH meter 22, and the turbidity meter 28 are constantly operating, and the measured values are input to the computer online as described above. The temperature of the culture system is maintained at a desired temperature by the temperature controller 30. Further, the gas pump 32 is operating, and oxygen is separated by the oxygen separator 24 and stored in the oxygen storage cylinder 40.

培養の結果、藻体が増殖して藻体の密度が一定値、例
えば初期密度の30%増になったことが濁度計28により示
されると、コンピューターを介して濁度計と電気的に接
続されている電磁弁50及び72がそれぞれA→C、A→C
に自動的に開き、かつポンプ52及び60が自動的に作動す
る。その結果、ポンプ52及び60に引かれて培養物が分岐
管48を矢印bの方向に流通し、電磁弁50及びポンプ52を
介して藻体回収器54に至り、円筒上フィルター56で藻体
が濾し取られて藻体貯蔵容器58内に蓄積され、円筒状フ
ィルター56によって藻体と分離された使用済の培地はポ
ンプ60を介して廃棄物タンク62内に廃棄される。円筒状
フィルター56が目詰まりした場合には、弁68を開き、ポ
ンプ66を作動させて水タンク64から水を引き出し、これ
を培養物を濾すのと反対方向に流してフィルターの目詰
まりを取り除く。一方、ポンプ52の働きにより、培地タ
ンク74から培地が引き出され、分岐管70a内を矢印cの
方向に流通して電磁弁72をA→Cに流れて分岐管70を介
して管路12に流入する。このようにして藻体の回収と培
養系への培地の供給が同時に行なわれる。
As a result of the culture, when the turbidimeter 28 indicates that the alga bodies multiplied and the density of the alga bodies increased to a certain value, for example, 30% of the initial density, the turbidity meter electrically connected to the computer. The connected solenoid valves 50 and 72 are A → C and A → C respectively.
Automatically open and the pumps 52 and 60 operate automatically. As a result, the culture is drawn by the pumps 52 and 60, flows through the branch pipe 48 in the direction of arrow b, reaches the alga body collector 54 via the solenoid valve 50 and the pump 52, and is filtered by the cylindrical filter 56. Is collected in the algal cell storage container 58, and the used medium separated from the algal cells by the cylindrical filter 56 is discarded into the waste tank 62 via the pump 60. If the cylindrical filter 56 is clogged, open the valve 68 and operate the pump 66 to draw water from the water tank 64 and drain it in the opposite direction to filter the culture to remove the filter clogging . On the other hand, by the function of the pump 52, the medium is drawn from the medium tank 74, flows through the branch pipe 70a in the direction of arrow c, flows through the solenoid valve 72 from A to C, and flows into the pipe 12 through the branch pipe 70. Inflow. In this way, the recovery of the algal cells and the supply of the culture medium to the culture system are performed simultaneously.

圧力計16の値が一定値以上、例えば0.06kg/cm2以上に
なったことが圧力計16によって示された場合には、圧力
計16とコンピューターを介して電気的に接続されている
電磁弁50及び72がそれぞれA→C、A→Bに自動的に開
き、かつ、ポンプ52及び60が自動的に作動する。その結
果、上記と同様に分岐管48内を矢印bの方向に培養物が
流通し、藻体回収器54によって藻体が回収される。一
方、ポンプ52の働きで分岐管70a内を培地タンク74から
の培地が矢印cの方向に流通すが、電磁弁7はA→Bに
開いているので、培地は管路12には流入しない。このよ
うにして、培養系の圧力が一定値以上に高くなった場合
には培地を供給することなく藻体のみが回収され、培養
系内の圧力が低下する。
If the pressure gauge 16 indicates that the value of the pressure gauge 16 has reached a certain value or more, for example, 0.06 kg / cm 2 or more, a solenoid valve electrically connected to the pressure gauge 16 via a computer 50 and 72 open automatically from A to C and A to B, respectively, and pumps 52 and 60 operate automatically. As a result, the culture flows in the branch pipe 48 in the direction of the arrow b in the same manner as described above, and the algal cells are collected by the algal cell collecting device 54. On the other hand, the culture medium from the culture tank 74 flows in the direction of arrow c in the branch pipe 70a by the function of the pump 52, but the culture medium does not flow into the pipeline 12 because the solenoid valve 7 is opened from A to B. . In this way, when the pressure of the culture system becomes higher than a certain value, only the algal cells are collected without supplying the medium, and the pressure in the culture system is reduced.

逆に、圧力計16によって系内の圧力が一定値、例えば
0.01kg/cm2以下になったことが示された場合には、電磁
弁50及び72がそれぞれB→C、A→Cに自動的に開き、
ポンプ52及び60が自動的に作動する。電磁弁50はB→C
に開いているので藻体回収器54には空気貯蔵器51からの
空気が流入するのみで培養物は流入しない。一方、ポン
プ52の働きにより、培地タンク74からの培地が上記と同
様に分岐管70a内を流通し、電磁弁72をA→Cに流通し
て分岐管70を介して管路12に流入する。このようにし
て、藻体は回収されずに培地のみが供給され、培養系内
の圧力は高くなる。
Conversely, the pressure in the system is kept constant by the pressure gauge 16, for example,
When it is shown that the pressure becomes 0.01 kg / cm 2 or less, the solenoid valves 50 and 72 are automatically opened from B → C and A → C, respectively,
Pumps 52 and 60 operate automatically. Solenoid valve 50 is B → C
Therefore, only the air from the air reservoir 51 flows into the algal cell recovery device 54, and the culture does not flow into the alga body recovery device 54. On the other hand, by the action of the pump 52, the culture medium from the culture tank 74 flows through the branch pipe 70a in the same manner as described above, flows through the electromagnetic valve 72 from A to C, and flows into the pipe 12 via the branch pipe 70. . Thus, only the medium is supplied without collecting the algal cells, and the pressure in the culture system increases.

一方、pHメーター22により、培養系内のpHが一定値、
例えば10以上になったことが示された場合には、pHメー
ター22とコンピューターを介して電気的に接続された弁
44が自動的に開き、二酸化炭素ボンベ42から二酸化炭素
が二酸化炭素供給器26を介して管路12内の培養物に供給
される。このようにして、培養系内の二酸化炭素が不足
してpHが高くなった場合には二酸化炭素が供給され、そ
の結果pHは低くなる。
On the other hand, the pH in the culture system is kept constant by the pH meter 22,
For example, if it is indicated that the value has reached 10 or more, a valve electrically connected to the pH meter 22 via a computer
44 is automatically opened, and carbon dioxide is supplied from the carbon dioxide cylinder 42 to the culture in the conduit 12 via the carbon dioxide supply device 26. In this way, when the pH rises due to a shortage of carbon dioxide in the culture system, carbon dioxide is supplied, resulting in a lower pH.

上述の実施例の装置によると、手動的な操作を必要と
することなく、藻類を一定範囲の条件下で長期間にわた
って連続的に培養し、藻体と酸素を連続的に回収するこ
とができる。
According to the apparatus of the above-described embodiment, algae can be continuously cultured for a long period of time under a certain range of conditions without requiring manual operation, and alga bodies and oxygen can be continuously collected. .

図に示した装置を試作した。培養槽の直径は17cm、円
筒状部分の高さが25cmで内容量は6であった。また、
管路12は内径1cmのシリコーンゴムから成り、その全長
は2mであった。
The device shown in the figure was prototyped. The diameter of the culture tank was 17 cm, the height of the cylindrical portion was 25 cm, and the content was 6. Also,
The conduit 12 was made of silicone rubber having an inner diameter of 1 cm, and its total length was 2 m.

この装置を用いてスピルリナ・マキシマを20日間連続
培養した。ポンプ14によって培養物は2/分で循環さ
せた。その結果、乾燥重量で1g以上の藻体が回収され、
酸素濃度が40%以上の気体を毎分50〜150mlの割合で得
ることができた。
Spirulina maxima was continuously cultured for 20 days using this apparatus. The culture was circulated at 2 / min by pump 14. As a result, alga bodies of 1 g or more in dry weight are collected,
A gas having an oxygen concentration of 40% or more was obtained at a rate of 50 to 150 ml per minute.

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

図面はこの発明の閉鎖系藻類培養装置の1実施例を模式
的に示す図である。 10……培養槽、12……管路、14……ポンプ、16……圧力
計、18……光源、20……光ファイバー束、22……pHメー
ター、24……酸素分離器、26……二酸化炭素供給器、28
……濁度計、30……温度調節器、32……気体ポンプ、40
……酸素貯蔵ボンベ、42……二酸化炭素ボンベ、48、70
……分岐管、50、72……電磁弁、54……藻体回収器、5
2、60……ポンプ、74……培地タンク
The drawing is a view schematically showing one embodiment of the closed algae culture apparatus of the present invention. 10: Culture tank, 12: Pipe line, 14: Pump, 16: Pressure gauge, 18: Light source, 20: Optical fiber bundle, 22: pH meter, 24: Oxygen separator, 26 ... Carbon dioxide supply, 28
… Turbidity meter, 30… temperature controller, 32… gas pump, 40
…… Oxygen storage cylinder, 42 …… Carbon dioxide cylinder, 48, 70
… Branch pipe, 50, 72… Solenoid valve, 54… Algae recovery device, 5
2, 60 pump, 74 medium tank

フロントページの続き (72)発明者 大坪 孔治 東京都多摩市豊ケ丘5丁目1番7号201 号 (72)発明者 新田 慶治 東京都東久留米市大門町2丁目4番 東 久留米第二住宅5号棟502号Continuation of the front page (72) Inventor Koharu Otsubo 5-7-1, Toyooka, Tama-shi, Tokyo No. 201 201 (72) Inventor Keiji Nitta 2-4-2, Omon-cho, Higashi-Kurume-shi, Tokyo Higashi-Kurume Second Housing 5 Building No.502

Claims (10)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】培養槽と該培養槽を介して閉じた管路とか
ら成る閉鎖培養系と、該閉鎖培養系内に培養物を循環さ
せる手段と、該閉鎖培養系内の圧力を測定する手段と、
前記閉鎖培養系内の二酸化炭素の量を測定する手段と、
前記閉鎖培養系内で培養される藻体の密度を測定する手
段と、前記閉鎖培養系から藻体を回収する手段と、前記
閉鎖培養系に培地を供給する手段と、前記閉鎖培養系に
二酸化炭素を供給する手段と、前記閉鎖培養系から酸素
を回収する手段とを含む閉鎖系藻類培養装置。
1. A closed culture system comprising a culture tank and a pipe line closed through the culture tank, means for circulating the culture in the closed culture system, and measuring the pressure in the closed culture system. Means,
Means for measuring the amount of carbon dioxide in the closed culture system,
Means for measuring the density of algal cells cultured in the closed culture system, means for collecting algal cells from the closed culture system, means for supplying a medium to the closed culture system, A closed algal culture apparatus comprising: means for supplying carbon; and means for recovering oxygen from the closed culture system.
【請求項2】前記二酸化炭素の量を測定する手段はpH測
定装置であり、前記藻体の密度を測定する手段は濁度計
である請求項1記載の装置。
2. The apparatus according to claim 1, wherein the means for measuring the amount of carbon dioxide is a pH measuring device, and the means for measuring the density of the algal cells is a turbidimeter.
【請求項3】前記二酸化炭素を供給する手段及び前記酸
素を回収する手段はそれぞれ、前記管路に挿入され、気
体は透過するが液体は透過しない大きさの孔を有する中
空ファイバーを含む請求項又1は2記載の装置。
3. The means for supplying carbon dioxide and the means for recovering oxygen each include a hollow fiber having a hole sized to be permeable to gas but impermeable to liquid, inserted into the conduit. 1 is the device according to 2.
【請求項4】前記圧力を測定するための手段と前記藻体
を回収するための手段及び前記培地を供給するための手
段とは接続されており、閉鎖培養系内の圧力が一定値以
上になった場合に前記藻体を回収するための手段が自動
的に藻体を回収し、閉鎖培養系内の圧力が一定値以下に
なった場合に前記培地を供給するための手段が自動的に
培地を供給する請求項1ないし3のいずれか1項に記載
の装置。
4. The means for measuring the pressure, the means for recovering the algal cells, and the means for supplying the medium are connected to each other, so that the pressure in the closed culture system is equal to or higher than a predetermined value. The means for recovering the alga bodies automatically recovers the alga bodies when the condition has been reached, and the means for supplying the medium automatically when the pressure in the closed culture system becomes a certain value or less. The device according to any one of claims 1 to 3, which supplies a medium.
【請求項5】前記二酸化炭素の量を測定する手段と前記
二酸化炭素を供給する手段とは接続され、閉鎖培養系内
の二酸化炭素濃度が一定値以下になった場合に前記二酸
化炭素を供給する手段が自動的に二酸化炭素を供給する
請求項1ないし4のいずれか1項に記載の装置。
5. The means for measuring the amount of carbon dioxide and the means for supplying carbon dioxide are connected, and supply the carbon dioxide when the concentration of carbon dioxide in the closed culture system falls below a certain value. Apparatus according to any of the preceding claims, wherein the means automatically supplies carbon dioxide.
【請求項6】前記藻体の密度を測定する手段と前記藻体
を回収する手段及び前記培地を供給する手段とは接続さ
れ、閉鎖培養系内の藻体密度が一定値以上になった場合
に前記藻体を回収する手段が自動的に藻体を回収し、か
つ、前記培地を供給する手段が自動的に前記閉鎖培養系
内に培地を供給する請求項1ないし6のいずれか1項に
記載の装置。
6. The means for measuring the density of the algal bodies, the means for collecting the algal bodies, and the means for supplying the medium, wherein the algal body density in the closed culture system is equal to or higher than a certain value. 7. The method according to claim 1, wherein the means for automatically collecting the algal cells automatically collects the algal cells, and the means for supplying the medium automatically supplies the medium into the closed culture system. An apparatus according to claim 1.
【請求項7】培養槽に光を照射する手段をさらに含む請
求項1ないし6のいずれか1項に記載の装置。
7. The apparatus according to claim 1, further comprising means for irradiating the culture tank with light.
【請求項8】前記自動的操作はコンピューターによって
自動制御される請求項4ないし6のいずれか1項に記載
の装置。
8. The apparatus according to claim 4, wherein said automatic operation is automatically controlled by a computer.
【請求項9】前記閉鎖培養系内の圧力を測定する手段、
前記閉鎖培養系内の二酸化炭素の量を測定する手段及び
前記閉鎖培養系内で培養される藻体の密度を測定する手
段からの計測値はオンラインでコンピューターに入力さ
れ、かつ、前記圧力を測定するための手段と前記藻体を
回収するための手段及び前記培地を供給するための手
段、前記二酸化炭素の量を測定する手段と前記二酸化炭
素を供給する手段、並びに前記藻体の密度を測定する手
段と前記藻体を回収する手段及び前記培地を供給する手
段とはそれぞれ上記コンピューターを介して接続される
請求項8記載の装置。
9. A means for measuring a pressure in the closed culture system,
Measured values from the means for measuring the amount of carbon dioxide in the closed culture system and the means for measuring the density of the algal cells cultured in the closed culture system are input to a computer online, and the pressure is measured. Means for recovering the algal bodies and means for supplying the medium, means for measuring the amount of carbon dioxide and means for supplying the carbon dioxide, and measuring the density of the algal bodies 9. The apparatus according to claim 8, wherein the means for performing the operation, the means for collecting the algal cells, and the means for supplying the medium are connected via the computer.
【請求項10】前記閉鎖培養系内の圧力を測定する手
段、前記閉鎖培養系内の二酸化炭素の量を測定する手段
及び前記閉鎖培養系内で培養される藻体の密度を測定す
る手段からの計測値はオンラインでコンピューターに入
力され、かつコンピューターのCRT画面上に表示される
請求項9記載の装置。
10. A means for measuring the pressure in the closed culture system, a means for measuring the amount of carbon dioxide in the closed culture system, and a means for measuring the density of algal cells cultured in the closed culture system. 10. The apparatus according to claim 9, wherein the measured values are input online to a computer and displayed on a CRT screen of the computer.
JP12146488A 1988-05-18 1988-05-18 Closed algae culture system Expired - Lifetime JP2615393B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12146488A JP2615393B2 (en) 1988-05-18 1988-05-18 Closed algae culture system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12146488A JP2615393B2 (en) 1988-05-18 1988-05-18 Closed algae culture system

Publications (2)

Publication Number Publication Date
JPH01291783A JPH01291783A (en) 1989-11-24
JP2615393B2 true JP2615393B2 (en) 1997-05-28

Family

ID=14811787

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2615393B2 (en)

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US5151347A (en) * 1989-11-27 1992-09-29 Martek Corporation Closed photobioreactor and method of use
KR100434755B1 (en) * 2000-08-25 2004-06-07 재단법인 포항산업과학연구원 Incubation apparatus for photosynthesis measurement of phytoplankton
DE102006014648B3 (en) * 2006-03-28 2007-12-27 Sartorius Biotech Gmbh Reactor plant and process for cultivating phototrophic microorganisms
JP2009195163A (en) * 2008-02-21 2009-09-03 Ccs Inc Culture apparatus for algae
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JP7216239B1 (en) * 2022-06-30 2023-01-31 三菱化工機株式会社 Algae culture device

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101235378B1 (en) * 2010-11-15 2013-02-20 전라남도 Device for cultivating micro algae

Also Published As

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