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JP4079877B2 - Microalgae culture apparatus and microalgae culture method - Google Patents
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JP4079877B2 - Microalgae culture apparatus and microalgae culture method - Google Patents

Microalgae culture apparatus and microalgae culture method Download PDF

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JP4079877B2
JP4079877B2 JP2003502141A JP2003502141A JP4079877B2 JP 4079877 B2 JP4079877 B2 JP 4079877B2 JP 2003502141 A JP2003502141 A JP 2003502141A JP 2003502141 A JP2003502141 A JP 2003502141A JP 4079877 B2 JP4079877 B2 JP 4079877B2
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徹 佐藤
好寛 土屋
真介 臼井
征四郎 平林
裕 近藤
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Description

<技術分野>
本発明は、光合成生物である微細藻類を培養するためのクローズド型の微細藻類培養装置、及び、微細藻類培養方法に関する。
<背景技術>
光合成生物である微細藻類は、二酸化炭素を吸収して光合成作用によってビタミン類、アミノ酸、色素類、タンパク質、多糖類、脂肪酸等の有用成分を製造するため、養殖の飼料用等として培養されている。又、この種の微細藻類は、地球温暖化の原因の1つとされる二酸化炭素を処理する手段としても利用され、近年、これを大量に培養する培養装置が研究されている。
ところで、培養装置は、培養液中で微細藻類を培養するものであって、光合成に必要な光は主に太陽光線を利用し、二酸化炭素は空気又は二酸化炭素と空気との混合気体を培養液に吹き込むことによって供給する。
而して、培養装置において太陽エネルギーを効率良く利用して微細藻類を効率良く培養するためには、
(1)受光量が多いこと
(2)培養液を十分撹拌し、微細藻類に効率良く光を当て、栄養分と二酸化炭素を均一に供給するとともに、微細藻類から排出される酸素を除去すること
(3)培養液の滞留のない撹拌を実現し、微細藻類の壁面付着による光透過の低下やコロニーの形成による沈殿防止を図ること
が必要となる。
従来、微細藻類の培養法として、培養池やレースウェイ型培養池等を利用したオープン型培養方式が実施されているが、この方式では培養液の十分な撹拌ができないために光が表層にしか到達せず、培養濃度が低く、埃やゴミ或は空気中の浮遊微生物等の混入を防ぐことができないために高pH、高塩分濃度等の特殊な条件下での培養が可能な微細藻類しか培養できず、更には培養液の温度調整が困難である等の問題がある。
そこで、培養容器の中に培養液を入れ、該培養液中に二酸化炭素を含むガスを吹き込みつつ、可視光線を入射させることによって培養容器内で微細藻類を培養するクローズド型の培養装置が種々提案されている。
ところで、クローズド型の培養装置の設置面積当たりの容量はオープン型培養方式のそれに比して小さく、高い生産性を上げるには高濃度培養が必要となる。
しかしながら、クローズド型の培養装置においては、光は受光壁面側から内部に至るに連れて減衰するため、光に当たる藻類と当たらない藻類ができてしまい、従って、装置内での培養液の十分な撹拌がなければ全ての藻類に公平に受光させることができず、高生産性を達成することができないという問題がある。
又、クローズド型の培養装置においては、培養容器の内壁に微細藻類が付着したり、培養容器内で微細藻類がコロニーを形成して沈殿するため、光の透過が遮られて培養効率が著しく低下するという問題がある。更に、培養容器内で微細藻類が沈殿するとバクテリアの温床となり、培養液が腐敗する原因にもなる。
本発明は上記問題に鑑みてなされたもので、その目的とする処は、培養液の十分な撹拌を実現して高い生産性を得ることができるとともに、微細藻類の培養容器壁面への付着や培養容器底面への沈殿を防いで長期に亘って高い培養効率を維持することができる微細藻類培養装置、及び、微細藻類培養方法を提供することにある。
<発明の開示>
上記目的を達成するため、請求の範囲第1項に記載の発明は、頂部に開口部を有する培養容器の中に培養液を入れ、該培養液中に二酸化炭素を含むガスを吹き込みつつ、可視光線を入射させることによって前記培養容器内で微細藻類を培養する微細藻類培養装置において、前記培養容器を横置きされた内筒と外筒から成る二重円筒状に成形するとともに、少なくとも外筒を可視光線を透過する透明材料で構成し、前記培養容器内に前記培養液の旋回流を形成するためのガスを吹き込むガス吹込口を培養容器内下部に開口せしめたことを特徴とする。
請求の範囲第2項に記載の発明は、請求の範囲第1項に記載の発明において、前記内筒と外筒を円筒、楕円筒又は長円筒で構成するとともに、これらの内筒と外筒を同心又は偏心させて配置したことを特徴とする。
請求の範囲第3項に記載の発明は、頂部に開口部を有する培養容器の中に培養液を入れ、該培養液中に二酸化炭素を含むガスを吹き込みつつ、可視光線を入射させることによって前記培養容器内で微細藻類を培養する微細藻類培養方法において、同心に横置された内筒と外筒とで二重円筒状に成形され、少なくとも外筒を可視光線を透過する透明材料で構成して成る培養容器の下部に開口するガス吹込口を、内筒と外筒の中心軸を通る鉛直面の左右何れか一方に配置し、該ガス吹込口から前記ガスを吹き込むことによって培養容器内に前記培養液の旋回流を形成することを特徴とする。
請求の範囲第4項に記載の発明は、頂部に開口部を有する培養容器の中に培養液を入れ、該培養液中に二酸化炭素を含むガスを吹き込みつつ、可視光線を入射させることによって前記培養容器内で微細藻類を培養する微細藻類培養方法において、偏心して横置きされた内筒と外筒とで二重円筒状に成形され、少なくとも外筒を可視光線を透過する透明材料で構成して成る培養容器の下部に開口するガス吹込口を、内筒の中心軸を通る鉛直面の左右何れか一方に配置し、該ガス吹込口から前記ガスを吹き込むことによって培養容器内に前記培養液の旋回流を形成することを特徴とする。
請求の範囲第5項に記載の発明は、請求の範囲第3項又は第4項に記載の発明において、前記培養容器の内筒の中心軸を通る鉛直面の左右に前記ガス吹込口を配置し、両ガス吹込口を所定時間毎に交互に切り替えることによって培養容器内の培養液の旋回方向を交互に切り替えることを特徴とする。
請求の範囲第6項に記載の発明は、請求の範囲第3項又は第4項に記載の発明において、前記培養容器の長手方向に複数のガス吹込口を配置し、培養容器の一端側のガス吹込口からガスを所定の時間差をもって順次吹き込むことによって培養容器内に培養液の前記培養容器の長手方向に沿って変化する旋回流を形成することを特徴とする。
請求の範囲第7項に記載の発明は、請求の範囲第3項又は第4項に記載の発明において、前記培養容器の長手方向に沿って複数のガス吹込口を内筒の中心軸を通る鉛直面の左右に交互に配置し、各ガス吹込口からガスを吹き込むことによって培養容器内に方向が長手方向に交互に異なる培養液の旋回流を形成することを特徴とする。
請求の範囲第8項に記載の発明は、請求の範囲第3項〜第7項の何れかに記載の発明において、前記培養容器の外筒外面への温調水の散水、外筒の外側に形成された水通路への温調水の通水又は内筒内への温調水の通水によって前記培養液の温度をコントロールすることを特徴とする。
従って、請求の範囲第1項に記載の発明によれば、前記培養容器内に前記培養液の旋回流を形成するためのガスを吹き込むガス吹込口を培養容器内下部に開口せしめるようしたため、ガスの吹き込みによって培養容器内に培養液の旋回流を形成して、培養液の十分な撹拌がなされて全ての微細藻類が公平に受光することができ、これによって高生産性を達成することができる。又、培養溶液内での気泡通過時の混相乱流と壁面における乱流境界層及び二重円筒状を成す培養容器の曲面壁に沿って培養液が流れることによるゲルトラー渦によって、外筒の曲面壁から内筒の曲面壁及び内筒の曲面壁から外筒の曲面壁に向かう渦が発生し、この渦によって培養液が滞留することなく十分撹拌されるため、微細藻類が培養容器の壁面に付着したりコロニーを形成して沈殿することがなくなり、微細藻類によって光の透過が遮られることがなく、微細藻類は効率良く且つ均一に受光するために微細藻類を効率良く培養することができ、長期に亘って高い培養効率を維持することができる。更に、培養容器を耐圧強度の高い内筒と外筒で構成したため、その板厚を小さく抑えて装置の軽量化及びコストダウンを図ることができる。
請求の範囲第2項に記載の発明によれば、円筒、楕円筒又は長円筒から成る内筒と外筒を同心又は偏心させて配置することによって培養容器を容易に構成することができる。
請求の範囲第3項によれば、同心に横置された内筒と外筒とで二重円筒状に成形され、少なくとも外筒を可視光線を透過する透明材料で構成して成る培養容器の下部に開口するガス吹込口を、内筒と外筒の中心軸を通る鉛直面の左右何れか一方に配置し、また、該ガス吹込口から前記ガスを吹き込むことによって培養容器内に前記培養液の旋回流を形成するため、培養液の十分な撹拌が容易になされて全ての微細藻類が公平に受光することができ、これによって高生産性を達成することができる。又、培養溶液内での気泡通過時の混相乱流と壁面における乱流境界層及び二重円筒状を成す培養容器の曲面壁に沿って培養液が流れることによるゲルトラー渦を容易に発生させることによって、外筒の曲面壁から内筒の曲面壁及び内筒の曲面壁から外筒の曲面壁に向かう渦を容易に発生させ、この渦によって培養液が滞留することなく十分撹拌されるため、微細藻類が培養容器の壁面に付着したりコロニーを形成して沈殿することがなくなり、微細藻類によって光の透過が遮られることがなく、微細藻類は効率良く且つ均一に受光するために微細藻類を効率良く培養することができ、長期に亘って高い培養効率を維持することができる。
請求の範囲第4項によれば、偏心して横置きされた内筒と外筒とで二重円筒状に成形され、少なくとも外筒を可視光線を透過する透明材料で構成して成る培養容器の下部に開口するガス吹込口を、内筒の中心軸を通る鉛直面の左右何れか一方に配置し、該ガス吹込口から前記ガスを吹き込むことによって培養容器内に前記培養液の旋回流を形成するため、培養液の十分な撹拌が容易になされて全ての微細藻類が公平に受光することができ、これによって高生産性を達成することができる。又、培養溶液内での気泡通過時の混相乱流と壁面における乱流境界層及び二重円筒状を成す培養容器の曲面壁に沿って培養液が流れることによるゲルトラー渦を容易に発生させることによって、外筒の曲面壁から内筒の曲面壁及び内筒の曲面壁から外筒の曲面壁に向かう渦を容易に発生させ、この渦によって培養液が滞留することなく十分撹拌されるため、微細藻類が培養容器の壁面に付着したりコロニーを形成して沈殿することがなくなり、微細藻類によって光の透過が遮られることがなく、微細藻類は効率良く且つ均一に受光するために微細藻類を効率良く培養することができ、長期に亘って高い培養効率を維持することができる。
請求の範囲第5項に記載の発明によれば、前記培養容器の内筒の中心軸を通る鉛直面の左右に前記ガス吹込口を配置し、両ガス吹込口を所定時間毎に交互に切り替えることによって培養容器内の培養液の旋回方向を交互に切り替えることによって、培養液を更に効率良く撹拌することができる。
請求の範囲第6項に記載の発明、すなわち、前記培養容器の長手方向に複数のガス吹込口を配置し、培養容器の一端側のガス吹込口からガスを所定の時間差をもって順次吹き込むことによって培養容器内に培養液の前記培養容器の長手方向に沿って変化する旋回流を形成することによっても、培養液の十分な撹拌を実現して高い生産性を得ることができるとともに、微細藻類の培養容器壁面への付着や培養容器底面への沈殿を防いで長期に亘って高い培養効率を維持することができる。
請求の範囲第7項に記載の発明、すなわち、前記培養容器の長手方向に沿って複数のガス吹込口を内筒の中心軸を通る鉛直面の左右に交互に配置し、各ガス吹込口からガスを吹き込むことによって培養容器内に方向が長手方向に交互に異なる培養液の旋回流を形成することによっても、培養液の十分な撹拌を実現して高い生産性を得ることができるとともに、微細藻類の培養容器壁面への付着や培養容器底面への沈殿を防いで長期に亘って高い培養効率を維持することができる。
請求の範囲第8項に記載の発明によれば、培養容器への温調水の散水又は通水によって培養液の温度をコントロールすることができるため、培養液を季節によらず一年中適温に保つことができ、特に夏期における培養液の過昇温による藻類成長への悪影響を効果的に解消することができる。
<発明を実施するための最良の形態>
以下に本発明の実施の形態を添付図面に基づいて説明する。
図1は本発明に係る微細藻類培養装置の斜視図、図2は同微細藻類培養装置の破断正面図(図1の矢視A方向の破断面図)、図3は同微細藻類培養装置の側断面図、図4は図3のB−B線断面図である。
本発明に係る微細藻類培養装置1は、外形がドラム状を成す培養容器2を支持台3上に横置きに設置して構成されている。
上記培養容器2は、図2〜図3に示すように、二重円筒状を成して同心的に横置きされた内筒4と外筒5の左右両端をリング状の側壁6,7によって閉塞して構成されている。即ち、同心的に横置きされた内筒4と外筒5の左右両端部に側壁6,7がそれぞれ組み込まれ、両側壁6,7の外周縁に穿設された複数(図示例では各6つ)の円孔(不図示)に長尺のボルト8を水平に通し(図1参照)、各ボルト8の端部に螺合するナット9を締め付けることによって外形がドラム状を成す培養容器2が組み立てられる。尚、本実施の形態では、長尺のボルト8を外筒5の外側に配置したが、これを内筒4の内側に配しても良い。又、各側壁6,7をそれぞれ短いボルトとこれに螺合するナットで各々独立に取り付ける構成を採用しても良い。更に、内筒4と外筒5の撓みを防ぐために両者間にスペーサを介設しても良く、この場合、スペーサには孔を形成しておくことが望ましい。
他方、枠体状を成す前記支持台3の左右上部には、側壁6,7の外形形状に沿った円弧状の固定ブラケット10(図1及び図2参照)が設けられており、培養容器2は、その左右の側壁6,7下部の2箇所が前記2本のボルト8とこれに螺合するナット9によって固定ブラケット10に共締めされることによって支持台3に水平に固定支持されている。
而して、上記培養容器2内に形成された内筒4と外筒5及び両側壁6,7によって囲まれた空間内には培養液11が注入され、その液位は内筒4の上端面よりも高くなるように保たれている。尚、内筒4と外筒5の左右両端は不図示のシール部材を介して両側壁6,7に結合されており、シール部材のシール作用によって培養液11の培養容器2外への漏出が防がれている。
ここで、培養容器2を構成する内筒4と外筒5及び両側壁6,7は太陽光(可視光線)を透過する透明材料で構成されており、本実施の形態では、透明材料としてアクリル樹脂を用いている。尚、透明材料としては、光透過性に優れ、耐候性及び耐紫外線の高い材料であれば任意のものを使用することができ、例えばポリカーボネート、ポリプロピレン、ポリエチレン、ポリ塩化ビニル等の樹脂、ガラス等を選定することができる。又、本実施の形態では、内筒4と外筒5及び両側壁6,7を透明部材で構成したが、本発明の目的を達成するためには、少なくとも外筒5が透明部材で構成されていれば良い。
又、図2〜図4に示すように、培養容器2の外筒5の一方の側壁6に近い側の幅方向中央下部には円孔状のドレン孔5a(図4参照)が穿設されており、このドレン孔5aにはドレンパイプ12が差し込まれて結着されている。そして、このドレンパイプ12の途中にはドレンバルブ13が設けられおり、このドレンバルブ13を開けることによって培養容器2内の培養液11を外部に排出することができる。
更に、培養容器2の外筒5の下部(具体的には、図4に示すように、内筒4と外筒5の中心軸を通る水平面Fより下方で、且つ、同中心軸を通る鉛直面Fの左右何れか一方)の長さ方向3箇所には円孔状のガス吹込口5b(図3及び図4参照)が穿設されている。
そして、培養容器2の下方にはガス導入パイプ14が長さ方向に水平に延設されており、このガス導入パイプ14から分岐して培養容器2側に向かって延びる3本の枝管15は、培養容器2の外筒5の下部に穿設された前記各ガス吹込口5bにそれぞれ差し込まれて結着されている。尚、図示しないが、ガス導入パイプ14は、空気又は二酸化炭素と空気との混合気体を供給するコンプレッサ等のガス供給源に接続されている。
他方、培養容器2(外筒)の頂部には、円筒状のガス排出筒16が取り付けられており、その内部は培養容器2内に開口するガス排出用開口部17が形成されている。そして、ガス排出筒16の上部には、下向きに開口する逆皿状のキャップ18が被着されており、ガス排出用開口部17がキャップ18によって覆われることによって培養容器2内の培養液11への埃やゴミ或は空気中の浮遊微生物等の混入を防ぐことができる。尚、キャップ18に代えてガス排出用開口部17にフィルタを設けることによっても同様の効果が得られる。
又、培養容器2の上部の前記ガス排出筒16を挟んでこれの左右には温調水導入パイプ19が長さ方向に平行を成して水平に延設されており、これらの温調水導入パイプ19は左右両側壁6,7の各上部に取り付けられた左右一対の支持ブラケット20に挿通支持されている。そして、各温調水導入パイプ19の下部には、図3に示すように複数の散水口19aが穿設されており、温調水導入パイプ19は冷却水ポンプ等の不図示の温調水供給源に接続されている。
次に、以上の構成を有する微細藻類培養装置1の作用について説明する。
当該微細藻類培養装置1を屋外に設置するとともに、培養容器2に培養すべき微細藻類と培養液11を入れ、不図示のガス供給源を駆動して二酸化炭素を含むガス(空気又は二酸化炭素と空気との混合気体)をガス導入パイプ14に流すと、ガスは3本の枝管15から培養容器2内に供給される。
培養容器2内に供給されたガスは、培養容器2の底部3箇所から図4に示すように気泡となって培養容器2内を上昇し、その過程で培養液11中の微細藻類に二酸化炭素を供給する。そして、このガスの気泡の上昇によって、培養容器2内には、図4に矢印にて示すように同一方向(図4において反時計方向)に旋回する培養液11の流れが形成される。
又、透明部材から成る外筒5及び側壁6,7を透過して太陽光線が培養容器2内に入射するため、培養容器2内の微細藻類は光合成作用によってビタミン類、アミノ酸、色素類、タンパク質、多糖類、脂肪酸等の有用成分を製造するとともに、地球温暖化の一因となっている二酸化炭素を吸収処理する。そして、光合成作用によって発生した酸素は、培養容器2の頂部に形成されたガス排出用開口部17及びガス排出筒16とキャップ18の間の隙間を通って大気中に排出される。尚、本実施の形態においては、培養容器2の内筒4内の中心部に人工光源を設置することができ、昼夜に亘って微細藻類に連続的に光合成を行わせることができ、微細藻類の増殖が促進される。
そして、必要に応じて、温調水供給源を駆動して温調水(冷却水)を温調水導入パイプ19に流せば、温調水は温調水導入パイプ19に穿設された複数の散水口19aから散水されて外筒5の外面に沿って流れ、培養容器2内の培養液11を冷却等してその温度をコントロールするため、培養液11を季節によらず一年中適温に保つことができ、特に夏期における培養液11の過昇温による藻類成長への悪影響を効果的に解消することができる。尚、本実施の形態では、培養容器2の外筒5外面への温調水の散水によって培養液11の温度をコントロールする構成を採用したが、外筒11の外側に形成された不図示の水通路への温調水の通水又は内筒4内への温調水の通水によっても同様に培養液11の温度をコントロールして同様の効果を得ることができる。
以上において、本実施の形態に係る微細藻類培養装置1においては、ガスの吹き込みによって培養容器2内に培養液11の旋回流を形成するようにしたため、培養液11の十分な撹拌がなされて全ての微細藻類が公平に受光することができ、これによって高生産性を達成することができる。
又、培養溶液11内での気泡通過時の混相乱流と壁面における乱流境界層及び二重円筒状を成す培養容器2の曲面壁に沿って培養液11が流れることによるゲルトラー渦によって、外筒5の曲面壁から内筒4の曲面壁及び内筒4の曲面壁から外筒5の曲面壁に向かう渦が発生し、この渦によって培養液11が滞留することなく十分撹拌されるため、微細藻類が培養容器2の壁面に付着したりコロニーを形成して沈殿することがなくなり、微細藻類によって光の透過が遮られることがなく、微細藻類は効率良く且つ均一に受光するために微細藻類を効率良く培養することができ、長期に亘って高い培養効率を維持することができる。
微細藻類が培養容器2の壁面に付着したりコロニーを形成して沈殿すると、微細藻類の受光が妨げられるので好ましくないが、微細藻類培養装置1によれば、種類の異なる混相乱流と乱流境界層とゲルトラー渦(以下に詳述)とが発生するので、内筒4と外筒5の間に渦や乱れが発生して、微細藻類によって光の透過が遮られることがない。
混相乱流:液相中を運動する気泡が引き起こす乱流
乱流境界層:壁面付近を流れが通過するとき、流れの相似側を表すパラメータであるReynolds数が高くなる(壁面上方の流れが速くなるか、流れが壁面に接する距離が長くなる)と、壁面付近に形成される速度の遅い層である境界層が乱流化する。この乱流化された層を乱流境界層という。
ゲルトラー渦:凹曲面を曲率に並行に流れがあるとき、流れの相似則を表すパラメータであるReynolds数が高くなる(壁面上方の流れが速くなるか、流れが壁面に接する距離が長くなる)と、流れに垂直な回転渦を生じる。この回転渦をゲルトラー渦という。
更に、培養容器2を耐圧強度の高い内筒4と外筒5で構成したため、その板厚を小さく抑えて培養装置1の軽量化及びコストダウンを図ることができる。
又、本実施の形態では、円筒から成る内筒4と外筒5を同心状に配置することによって培養容器2を容易に構成することができる。
そして、内筒4と外筒5を同心状に配置して成る培養容器2において、ガスの吹込み口5bを内筒4と外筒5の中心軸を通る水平面Fより下方で、且つ、同中心軸を通る鉛直面Fの左右何れか一方に配置したため、培養容器2内に一方向に旋回する培養液11の流れを容易に形成できるとともに、混相乱流、乱流境界層、ゲルトラー渦の発生が容易である。尚、図5に示すようにガス吹込口5bを鉛直面Fの反対側に形成すれば、本実施の形態とは逆方向(図5において時計方向)に旋回する培養液11の流れを形成することができる。又、図示しないが、内外筒の中心軸を通る鉛直面の左右両側にガスの吹込口を形成し、両吹込口を所定時間毎に交互に切り替えるようにすれば、培養容器内の培養液の旋回方向を交互に切り替えることができ、培養液を更に効率良く撹拌することができる。更に、培養容器2の長手方向において部分的に培養液11の旋回方向を定常的又は過渡的に変えるようにしても良い。培養容器2の長手方向に複数のガス吹込口5bを配置し、培養容器2の一端側のガス吹込口5bからガスを所定の時間差をもって順次吹き込むことによって培養容器2内に培養液11の培養容器2の長手方向に沿って変化する旋回流を形成しても良い。培養容器2の長手方向に沿って複数のガス吹込口5bを内筒の中心軸を通る鉛直面の左右に交互に配置し、各ガス吹込口5bからガスを吹き込むことによって培養容器2内に方向が長手方向に交互に異なる培養液11の旋回流を形成してもよい。
ところで、本実施の形態では、円筒から成る内筒4と外筒5を同心状に配置して培養容器2を構成したが、図6に示すように、円筒から成る内筒4と外筒5を偏心させて配置することによって培養容器2を構成しても良く、この場合、ガスの吹込口4aを図示のように内筒4の中心軸を通る水平面Fより下方で、且つ、同中心軸を通る鉛直面Fの左右何れか一方に配置すれば、培養容器2内で培養液11の同一方向(図示例では、反時計方向)に旋回する流れを容易に形成できるとともに、混相乱流、乱流境界層、ゲルトラー渦の発生が容易である。
又、図7に示すように楕円筒から成る内筒4’と外筒5’を同心状に配置して培養容器2’を構成し、或は図8に示すように長円筒から成る内筒4”と外筒5”を同心状に配置して培養容器2”を構成しても良く、これらの場合はガスの吹込口4a’,5b”を内筒4’,4”と外筒5’,5”の中心軸を通る水平面Fより下方で、且つ、同中心軸を通る鉛直面Fの左右何れか一方に配置することによって培養容器2’,2”内に同一方向(図示例では、反時計方向)に旋回する培養液11の流れを形成することができる。尚、図示しないが、楕円筒又は長円筒から成る内筒と外筒を偏心させて配置することによって培養容器を構成しても良く、これらの場合はガスの吹込口を内筒の中心軸を通る水平面より下方で、且つ、同中心軸を通る鉛直面の左右何れか一方に配置することによって培養容器内に同一方向に旋回する培養液の流れを形成することができる。
ここで、本実施の形態に係る微細藻類培養装置1を用いた実際の生産設備例を図9に示すが、実際の生産設備においては、図示のように複数の微細藻類培養装置1を一列に連続して繋げたものが数列に亘って配設される。この場合、各列において各1本のガス導入パイプ14と各2本の温調水導入パイプ19が各培養装置1について共用される。
次に、本発明に係る微細藻類培養装置を用いて行った培養実験の結果について説明する。
微細藻類としてクロロコッカムリトラーレ(Chlorococcum littorale)を用いて培養実験を13日間に亘って行った。この場合の日照時間は10時間/日、南中時光量子量800μmol/m/s、日中平均光量子量340μmol/m/s、培養液量70リットルであり、培養結果は平均増殖速度0.15g乾燥重量/リットル/日であった。又、培養期間中に微細藻類の培養容器壁面への付着は発生しなかった。
又、別の培養実験において、微細藻類としてスピルリナ・プラテンシス(Spirulina platencis)を培養した結果、従来の培養池方式では培養濃度0.3〜0.5g/リットル、一日あたりの生産性0.1〜0.2g/リットルであるのに対して、本発明に係る微細藻類培養装置では培養濃度10〜20g/リットル、一日あたりの生産性2.8〜7.0g/リットルという好結果が得られた。
<産業上の利用可能性>
以上の説明で明らかなように、本発明によれば、頂部に開口部を有する培養容器の中に培養液を入れ、該培養液中に二酸化炭素を含むガスを吹き込みつつ、可視光線を入射させることによって前記培養容器内で微細藻類を培養する微細藻類培養装置において、前記培養容器を横置きされた内筒と外筒から成る二重円筒状に成形するとともに、少なくとも外筒を可視光線を透過する透明材料で構成し、前記ガスの吹き込みによって前記培養容器内に前記培養液の旋回流を形成するようにしたため、培養液の十分な撹拌を実現して高い生産性を得ることができるとともに、微細藻類の培養容器壁面への付着や培養容器底面への沈殿を防いで長期に亘って高い培養効率を維持することができるという効果が得られる。
また、本発明によれば、頂部に開口部を有する培養容器の中に培養液を入れ、該培養液中に二酸化炭素を含むガスを吹き込みつつ、可視光線を入射させることによって前記培養容器内で微細藻類を培養する微細藻類培養方法において、同心に横置された内筒と外筒とで二重円筒状に成形され、少なくとも外筒を可視光線を透過する透明材料で構成して成る培養容器の下部に開口するガス吹込口を、内筒と外筒の中心軸を通る鉛直面の左右何れか一方に配置し、該ガス吹込口から前記ガスを吹き込むことによって、あるいは、偏心して横置きされた内筒と外筒とで二重円筒状に成形され、少なくとも外筒を可視光線を透過する透明材料で構成して成る培養容器の下部に開口するガス吹込口を、内筒の中心軸を通る鉛直面の左右何れか一方に配置し、該ガス吹込口から前記ガスを吹き込むことによって、培養容器内に培養液の旋回流を形成するため、培養液の十分な撹拌を容易に実現して高い生産性を得ることができるとともに、微細藻類の培養容器壁面への付着や培養容器底面への沈殿を防いで長期に亘って高い培養効率を維持することができるという効果が得られる。
【図面の簡単な説明】
図1は、本発明に係る微細藻類培養装置の斜視図である。
図2は、本発明に係る微細藻類培養装置の破断正面図(図1の矢視A方向の破断面図)である。
図3は、本発明に係る微細藻類培養装置の側断面図である。
図4は、図3のB−B線断面図である。
図5は、本発明に係る微細藻類培養装置の培養容器の別形態を示す横断面図である。
図6は、本発明に係る微細藻類培養装置の培養容器の別形態を示す横断面図である。
図7は、本発明に係る微細藻類培養装置の培養容器の別形態を示す横断面図である。
図8は、本発明に係る微細藻類培養装置の培養容器の別形態を示す横断面図である。
図9は、本発明に係る微細藻類培養装置を用いた実際の生産設備例を示す斜視図である。
なお、図中の符号、1は微細藻類培養装置、2,2’,2”は培養容器、4,4’,4”は内筒、4a,4a’はガス吹込口、5,5,5”は外筒、5b,5b”はガス吹込口、6,7は側壁、11は培養液、14はガス導入パイプ、17はガス排出用開口部、18はキャップ、19は温調水導入パイプである。
<Technical field>
The present invention relates to a closed-type microalgae culture apparatus and a microalgae culture method for culturing microalgae that are photosynthetic organisms.
<Background technology>
Microalgae that are photosynthetic organisms are cultivated for aquaculture feed, etc., because they absorb carbon dioxide and produce useful components such as vitamins, amino acids, pigments, proteins, polysaccharides, and fatty acids by photosynthesis. . In addition, this type of microalgae is also used as a means for treating carbon dioxide, which is one of the causes of global warming, and recently, a culture apparatus for culturing this in large quantities has been studied.
By the way, the culture apparatus is for culturing microalgae in a culture solution, and the light necessary for photosynthesis mainly uses sunlight, and carbon dioxide is air or a mixed gas of carbon dioxide and air. Supply by blowing into.
Thus, in order to efficiently cultivate microalgae using solar energy efficiently in the culture device,
(1) Large amount of light received
(2) Thoroughly stir the culture solution, efficiently illuminate the microalgae, supply nutrients and carbon dioxide uniformly, and remove oxygen discharged from the microalgae
(3) Achieving agitation without stagnation of the culture solution, and reducing precipitation due to adhesion of microalgae to the wall and colonization.
Is required.
Conventionally, as a method for culturing microalgae, an open culture method using a culture pond, a raceway culture pond, or the like has been implemented. However, since this method does not allow sufficient agitation of the culture solution, light is only on the surface layer. Only microalgae that can be cultured under special conditions such as high pH and high salinity because the culture concentration is low, the culture concentration is low, and dust and dirt or airborne microorganisms cannot be prevented. There is a problem that the culture cannot be performed and the temperature of the culture solution is difficult to adjust.
Therefore, various types of closed-type culture devices for culturing microalgae in a culture vessel by putting visible light into the culture solution while injecting a gas containing carbon dioxide into the culture solution are proposed. Has been.
By the way, the capacity per installation area of the closed type culture apparatus is smaller than that of the open type culture method, and high concentration culture is required to increase high productivity.
However, in a closed type culture apparatus, light attenuates as it reaches from the light receiving wall side to the inside, so that algae that strikes the light and algae that do not strike are formed. Therefore, sufficient agitation of the culture solution in the apparatus is achieved. Without it, there is a problem that all algae cannot receive light fairly and high productivity cannot be achieved.
In a closed type culture device, microalgae adhere to the inner wall of the culture vessel, or microalgae form colonies in the culture vessel and precipitate, thereby blocking the transmission of light and significantly reducing the culture efficiency. There is a problem of doing. Furthermore, when microalgae settle in the culture vessel, it becomes a hotbed of bacteria, which also causes the culture solution to rot.
The present invention has been made in view of the above problems, and the intended treatment is that sufficient agitation of the culture solution can be realized to obtain high productivity, and adhesion of microalgae to the culture vessel wall surface and An object of the present invention is to provide a microalgae culture apparatus and a microalgae culture method that can prevent precipitation on the bottom surface of a culture vessel and maintain high culture efficiency over a long period of time.
<Disclosure of invention>
In order to achieve the above-mentioned object, the invention described in claim 1 includes a culture solution placed in a culture vessel having an opening at the top, and a gas containing carbon dioxide is blown into the culture solution while being visible. In the microalgae culture apparatus for cultivating microalgae in the culture vessel by making light incident, the culture vessel is formed into a double cylindrical shape consisting of a horizontally placed inner cylinder and an outer cylinder, and at least the outer cylinder is It is made of a transparent material that transmits visible light, and a gas blowing port for blowing a gas for forming a swirling flow of the culture solution into the culture vessel is opened at the lower part of the culture vessel.
The invention according to claim 2 is the invention according to claim 1, wherein the inner cylinder and the outer cylinder are constituted by a cylinder, an elliptic cylinder, or a long cylinder, and these inner cylinder and outer cylinder. Are arranged concentrically or eccentrically.
The invention according to claim 3 is characterized in that the culture solution is put into a culture vessel having an opening at the top, and visible light is incident while blowing a gas containing carbon dioxide into the culture solution. In the microalgae culture method for culturing microalgae in a culture vessel, the inner cylinder and the outer cylinder placed concentrically are formed into a double cylinder shape, and at least the outer cylinder is made of a transparent material that transmits visible light. A gas inlet opening in the lower part of the culture vessel is arranged on either the left or right of the vertical plane passing through the central axis of the inner cylinder and the outer cylinder, and the gas is blown from the gas inlet into the culture container. A swirling flow of the culture solution is formed.
The invention according to claim 4 is characterized in that the culture solution is put into a culture vessel having an opening at the top, and a visible ray is incident while blowing a gas containing carbon dioxide into the culture solution. In the microalgae cultivation method for culturing microalgae in a culture vessel, the inner cylinder and the outer cylinder, which are eccentrically placed horizontally, are formed into a double cylinder shape, and at least the outer cylinder is made of a transparent material that transmits visible light. The gas blowing port that opens at the lower part of the culture vessel is arranged on either the left or right side of the vertical plane that passes through the central axis of the inner cylinder, and the gas is blown from the gas blowing port so that the culture solution is introduced into the culture vessel. The swirl flow is formed.
The invention according to claim 5 is the invention according to claim 3 or 4, wherein the gas inlets are arranged on the left and right of the vertical plane passing through the central axis of the inner cylinder of the culture vessel. In addition, the swirling direction of the culture solution in the culture vessel is alternately switched by alternately switching both gas blowing ports every predetermined time.
The invention according to claim 6 is the invention according to claim 3 or 4, wherein a plurality of gas injection ports are arranged in the longitudinal direction of the culture vessel, and A swirling flow of the culture solution that changes along the longitudinal direction of the culture vessel is formed in the culture vessel by sequentially blowing gas from the gas blowing port with a predetermined time difference.
The invention according to claim 7 is the invention according to claim 3 or 4, wherein the plurality of gas injection ports pass through the central axis of the inner cylinder along the longitudinal direction of the culture vessel. It arrange | positions alternately at right and left of a vertical surface, and forms the swirl | vortex flow of the culture solution from which a direction differs in a longitudinal direction alternately in a culture container by blowing in gas from each gas blowing port.
The invention according to claim 8 is the invention according to any one of claims 3 to 7, wherein water of temperature-controlled water is sprayed on the outer surface of the outer cylinder of the culture vessel, and the outer side of the outer cylinder. The temperature of the culture solution is controlled by passing the temperature-controlled water through the water passage formed in the above or the temperature-controlled water flowing into the inner cylinder.
Therefore, according to the invention described in claim 1, since the gas blowing port for blowing the gas for forming the swirling flow of the culture solution into the culture vessel is opened at the lower part in the culture vessel, The swirling flow forms a swirling flow of the culture solution in the culture vessel, and the culture solution is sufficiently agitated so that all the microalgae can receive light evenly, thereby achieving high productivity. . Also, the curved surface of the outer cylinder is caused by the mixed-phase turbulent flow during passage of bubbles in the culture solution, the turbulent boundary layer on the wall surface, and the geltler vortex caused by the flow of the culture solution along the curved wall of the double cylindrical culture vessel. A vortex is generated from the wall to the curved wall of the inner cylinder and from the curved wall of the inner cylinder to the curved wall of the outer cylinder, and the vortex stirs well without stagnation of the culture solution. There is no deposit or colony formation and precipitation, light transmission is not blocked by the microalgae, and the microalgae can efficiently and uniformly cultivate the microalgae to receive light efficiently, High culture efficiency can be maintained over a long period of time. Furthermore, since the culture vessel is composed of an inner cylinder and an outer cylinder with high pressure resistance, the plate thickness can be kept small, and the weight and cost of the apparatus can be reduced.
According to the invention described in claim 2, the culture vessel can be easily configured by arranging the inner cylinder and the outer cylinder made of a cylinder, an elliptic cylinder, or a long cylinder concentrically or eccentrically.
According to claim 3 of the present invention, there is provided a culture vessel which is formed into a double cylinder shape by an inner cylinder and an outer cylinder placed concentrically, and at least the outer cylinder is made of a transparent material that transmits visible light. A gas blowing port that opens in the lower part is disposed on either the left or right of the vertical plane that passes through the central axis of the inner cylinder and the outer cylinder, and the culture solution is blown into the culture vessel by blowing the gas from the gas blowing port. In order to form a swirling flow, sufficient agitation of the culture solution is facilitated, and all the microalgae can receive light fairly, thereby achieving high productivity. In addition, turbulent multiphase flow during the passage of bubbles in the culture solution, turbulent boundary layer on the wall surface and geltler vortex caused by the flow of the culture solution along the curved wall of the double cylindrical culture vessel The vortex from the curved wall of the outer cylinder to the curved wall of the inner cylinder and the curved wall of the inner cylinder to the curved wall of the outer cylinder is easily generated, and the culture solution is sufficiently stirred without stagnation by this vortex. The microalgae do not adhere to the wall of the culture vessel or form a colony and settle, the light transmission is not blocked by the microalgae, and the microalgae receive the microalgae in order to receive light efficiently and uniformly. Culture can be performed efficiently, and high culture efficiency can be maintained over a long period of time.
According to the fourth aspect of the present invention, there is provided a culture vessel formed of a double cylinder having an inner cylinder and an outer cylinder that are eccentrically placed horizontally, and at least the outer cylinder is made of a transparent material that transmits visible light. A gas blowing port that opens in the lower part is arranged on either the left or right of the vertical plane passing through the central axis of the inner cylinder, and the swirling flow of the culture solution is formed in the culture vessel by blowing the gas from the gas blowing port. Therefore, sufficient agitation of the culture solution is facilitated, and all microalgae can receive light fairly, thereby achieving high productivity. In addition, turbulent multiphase flow during the passage of bubbles in the culture solution, turbulent boundary layer on the wall surface and geltler vortex caused by the flow of the culture solution along the curved wall of the double cylindrical culture vessel The vortex from the curved wall of the outer cylinder to the curved wall of the inner cylinder and the curved wall of the inner cylinder to the curved wall of the outer cylinder is easily generated, and the culture solution is sufficiently stirred without stagnation by this vortex. The microalgae do not adhere to the wall of the culture vessel or form a colony and settle, the light transmission is not blocked by the microalgae, and the microalgae receive the microalgae in order to receive light efficiently and uniformly. Culture can be performed efficiently, and high culture efficiency can be maintained over a long period of time.
According to the invention described in claim 5, the gas injection ports are arranged on the left and right of the vertical plane passing through the central axis of the inner cylinder of the culture vessel, and the two gas injection ports are alternately switched every predetermined time. Thus, the culture solution can be stirred more efficiently by alternately switching the swirling direction of the culture solution in the culture vessel.
The invention according to claim 6, that is, culturing by arranging a plurality of gas injection ports in the longitudinal direction of the culture vessel and sequentially injecting gas from the gas injection port on one end side of the culture vessel with a predetermined time difference. By forming a swirling flow of the culture solution that changes along the longitudinal direction of the culture vessel in the vessel, sufficient agitation of the culture solution can be realized to obtain high productivity, and cultivation of microalgae can be achieved. High culture efficiency can be maintained over a long period of time by preventing adhesion to the vessel wall surface and precipitation on the bottom surface of the culture vessel.
The invention according to claim 7, that is, a plurality of gas injection ports are alternately arranged on the left and right of the vertical plane passing through the central axis of the inner cylinder along the longitudinal direction of the culture vessel, and from each gas injection port By blowing gas, a swirling flow of the culture solution whose direction is alternately different in the longitudinal direction can be formed in the culture vessel, so that sufficient agitation of the culture solution can be realized and high productivity can be obtained. High culture efficiency can be maintained over a long period of time by preventing adhesion of algae to the culture vessel wall surface and precipitation on the bottom surface of the culture vessel.
According to the invention described in claim 8, since the temperature of the culture solution can be controlled by sprinkling or passing the temperature-controlled water to the culture vessel, the culture solution is kept at a suitable temperature throughout the year regardless of the season. In particular, adverse effects on algae growth due to excessive heating of the culture solution in summer can be effectively eliminated.
<Best Mode for Carrying Out the Invention>
Embodiments of the present invention will be described below with reference to the accompanying drawings.
FIG. 1 is a perspective view of the microalgae culture apparatus according to the present invention, FIG. 2 is a cutaway front view of the microalgae culture apparatus (fracture sectional view in the direction of arrow A in FIG. 1), and FIG. 4 is a sectional view taken along line BB in FIG.
A microalgae culture apparatus 1 according to the present invention is configured by horizontally placing a culture vessel 2 having an outer shape in a drum shape on a support base 3.
As shown in FIGS. 2 to 3, the culture vessel 2 has a double-cylindrical inner cylinder 4 and an outer cylinder 5 that are concentrically placed horizontally by ring-shaped side walls 6 and 7. It is configured to be closed. That is, side walls 6 and 7 are respectively incorporated in the left and right ends of the inner cylinder 4 and the outer cylinder 5 placed concentrically, and a plurality of (6 in the example shown) are formed in the outer peripheral edges of the side walls 6 and 7. The culture vessel 2 whose outer shape forms a drum shape by passing a long bolt 8 horizontally through a circular hole (not shown) (see FIG. 1) and tightening a nut 9 screwed into the end of each bolt 8. Is assembled. In the present embodiment, the long bolt 8 is arranged outside the outer cylinder 5, but it may be arranged inside the inner cylinder 4. Moreover, you may employ | adopt the structure which attaches each side wall 6 and 7 each independently with a short volt | bolt and a nut screwed together. Further, a spacer may be interposed between the inner cylinder 4 and the outer cylinder 5 in order to prevent the inner cylinder 4 and the outer cylinder 5 from being bent. In this case, it is desirable to form a hole in the spacer.
On the other hand, arc-shaped fixing brackets 10 (see FIGS. 1 and 2) along the outer shape of the side walls 6 and 7 are provided on the left and right upper portions of the support base 3 having a frame shape. Are fixedly supported horizontally on the support base 3 by being fastened to the fixing bracket 10 by the two bolts 8 and nuts 9 screwed into the two bolts 8 on the left and right side walls 6, 7. .
Thus, the culture solution 11 is injected into the space surrounded by the inner cylinder 4 and the outer cylinder 5 and the side walls 6 and 7 formed in the culture vessel 2, and the liquid level is above the inner cylinder 4. It is kept higher than the end face. The left and right ends of the inner cylinder 4 and the outer cylinder 5 are connected to both side walls 6 and 7 via seal members (not shown), and the culture medium 11 leaks out of the culture vessel 2 by the sealing action of the seal members. It is prevented.
Here, the inner cylinder 4 and the outer cylinder 5 and both side walls 6 and 7 constituting the culture vessel 2 are made of a transparent material that transmits sunlight (visible light). In this embodiment, acrylic is used as the transparent material. Resin is used. As the transparent material, any material can be used as long as it is excellent in light transmittance and has high weather resistance and high ultraviolet resistance. For example, resin such as polycarbonate, polypropylene, polyethylene, polyvinyl chloride, glass, etc. Can be selected. In the present embodiment, the inner cylinder 4 and the outer cylinder 5 and the side walls 6 and 7 are made of a transparent member. However, in order to achieve the object of the present invention, at least the outer cylinder 5 is made of a transparent member. It should be.
As shown in FIGS. 2 to 4, a circular drain hole 5 a (see FIG. 4) is formed in the center lower portion in the width direction on the side close to one side wall 6 of the outer cylinder 5 of the culture vessel 2. A drain pipe 12 is inserted into and connected to the drain hole 5a. A drain valve 13 is provided in the middle of the drain pipe 12. By opening the drain valve 13, the culture solution 11 in the culture vessel 2 can be discharged to the outside.
Furthermore, the lower part of the outer cylinder 5 of the culture vessel 2 (specifically, as shown in FIG. 4, a horizontal plane F passing through the central axes of the inner cylinder 4 and the outer cylinder 5). H A vertical plane F that is lower and passes through the same central axis V A circular gas inlet 5b (see FIG. 3 and FIG. 4) is bored at three locations in the length direction of either one of the left and right sides.
A gas introduction pipe 14 is horizontally extended below the culture vessel 2 in the length direction, and three branch pipes 15 branched from the gas introduction pipe 14 and extending toward the culture vessel 2 side are provided. Each of the gas blowing ports 5b formed in the lower portion of the outer cylinder 5 of the culture vessel 2 is inserted and bound. Although not shown, the gas introduction pipe 14 is connected to a gas supply source such as a compressor that supplies air or a mixed gas of carbon dioxide and air.
On the other hand, a cylindrical gas discharge tube 16 is attached to the top of the culture vessel 2 (outer tube), and a gas discharge opening 17 that opens into the culture vessel 2 is formed inside thereof. An inverted dish-shaped cap 18 that opens downward is attached to the upper portion of the gas discharge cylinder 16, and the gas discharge opening 17 is covered with the cap 18, whereby the culture solution 11 in the culture vessel 2 is covered. It is possible to prevent contamination of dust, dirt or airborne microorganisms in the air. A similar effect can be obtained by providing a filter in the gas discharge opening 17 instead of the cap 18.
In addition, temperature control water introduction pipes 19 extend horizontally in parallel to the length direction on the left and right sides of the gas discharge cylinder 16 at the top of the culture vessel 2, and these temperature control water The introduction pipe 19 is inserted and supported by a pair of left and right support brackets 20 attached to the upper portions of the left and right side walls 6 and 7. As shown in FIG. 3, a plurality of water spouts 19a are formed in the lower portion of each temperature adjustment water introduction pipe 19, and the temperature adjustment water introduction pipe 19 is a temperature adjustment water (not shown) such as a cooling water pump. Connected to the supply source.
Next, the effect | action of the micro algae culture apparatus 1 which has the above structure is demonstrated.
The microalgae culture apparatus 1 is installed outdoors, and the microalgae to be cultured and the culture solution 11 are placed in the culture vessel 2, and a gas supply source (not shown) is driven to provide a gas containing carbon dioxide (air or carbon dioxide and When a gas mixture with air is passed through the gas introduction pipe 14, the gas is supplied from the three branch pipes 15 into the culture vessel 2.
The gas supplied into the culture vessel 2 becomes bubbles from the three bottom portions of the culture vessel 2 as shown in FIG. 4 and rises in the culture vessel 2, and in the process, carbon dioxide is supplied to the microalgae in the culture solution 11. Supply. As the gas bubbles rise, a flow of the culture solution 11 swirling in the same direction (counterclockwise in FIG. 4) is formed in the culture vessel 2 as indicated by an arrow in FIG.
Further, since the sunlight passes through the outer cylinder 5 and the side walls 6 and 7 made of a transparent member and enters the culture vessel 2, the microalgae in the culture vessel 2 are vitamins, amino acids, pigments, proteins by photosynthesis. In addition to producing useful components such as polysaccharides and fatty acids, carbon dioxide that contributes to global warming is absorbed. The oxygen generated by the photosynthetic action is discharged into the atmosphere through the gas discharge opening 17 formed at the top of the culture vessel 2 and the gap between the gas discharge tube 16 and the cap 18. In the present embodiment, an artificial light source can be installed in the center of the inner cylinder 4 of the culture vessel 2, and the microalgae can be continuously photosynthesised day and night. Is promoted.
Then, if necessary, if the temperature adjustment water supply source is driven and the temperature adjustment water (cooling water) flows through the temperature adjustment water introduction pipe 19, the temperature adjustment water is plurally provided in the temperature adjustment water introduction pipe 19. In order to control the temperature of the culture solution 11 in the culture vessel 2 by cooling it or the like, the temperature of the culture solution 11 is controlled throughout the year regardless of the season. In particular, adverse effects on algae growth due to excessive heating of the culture solution 11 in summer can be effectively eliminated. In the present embodiment, a configuration is adopted in which the temperature of the culture solution 11 is controlled by sprinkling temperature-controlled water on the outer surface of the outer cylinder 5 of the culture vessel 2, but not shown in the figure formed outside the outer cylinder 11. The same effect can be obtained by similarly controlling the temperature of the culture solution 11 by passing the temperature-controlled water through the water passage or the temperature-controlled water through the inner cylinder 4.
In the above, in the microalgae culture apparatus 1 according to the present embodiment, the swirl flow of the culture solution 11 is formed in the culture vessel 2 by blowing gas, so that the culture solution 11 is sufficiently agitated and all The microalgae can receive light fairly, thereby achieving high productivity.
In addition, the mixed-phase turbulent flow during the passage of bubbles in the culture solution 11, the turbulent boundary layer on the wall surface, and the Gertler vortex caused by the flow of the culture solution 11 along the curved wall of the culture vessel 2 having a double cylindrical shape A vortex is generated from the curved wall of the cylinder 5 toward the curved wall of the inner cylinder 4 and from the curved wall of the inner cylinder 4 to the curved wall of the outer cylinder 5, and the culture solution 11 is sufficiently agitated by this vortex without being retained, The microalgae is not attached to the wall of the culture vessel 2 or forming a colony, and the microalgae are not blocked by the microalgae, and the microalgae receive light efficiently and uniformly. Can be efficiently cultured, and high culture efficiency can be maintained over a long period of time.
If the microalgae adhere to the wall surface of the culture vessel 2 or form a colony and precipitate, it is not preferable because the light reception of the microalgae is hindered. However, according to the microalgae culture device 1, different types of mixed-phase turbulence and turbulence Since the boundary layer and the Gertler vortex (described in detail below) are generated, vortices and disturbances are generated between the inner cylinder 4 and the outer cylinder 5, and light transmission is not blocked by the microalgae.
Multiphase turbulence: turbulence caused by bubbles moving in the liquid phase
Turbulent boundary layer: When the flow passes near the wall surface, the Reynolds number, which is a parameter representing the similarity side of the flow, becomes high (the flow above the wall surface becomes faster or the distance at which the flow contacts the wall surface) The boundary layer, which is a slow layer formed near the wall surface, becomes turbulent. This turbulent layer is called a turbulent boundary layer.
Geltler vortex: When there is a flow in parallel with the curvature of the concave surface, the Reynolds number, which is a parameter representing the similarity law of the flow, increases (the flow above the wall becomes faster or the distance that the flow contacts the wall becomes longer) This produces a rotating vortex perpendicular to the flow. This rotating vortex is called the Gertler vortex.
Furthermore, since the culture vessel 2 is composed of the inner cylinder 4 and the outer cylinder 5 having a high pressure resistance, the thickness of the culture apparatus 1 can be reduced and the culture apparatus 1 can be reduced in weight and cost.
Moreover, in this Embodiment, the culture container 2 can be comprised easily by arrange | positioning the inner cylinder 4 and the outer cylinder 5 which consist of a cylinder concentrically.
In the culture vessel 2 in which the inner cylinder 4 and the outer cylinder 5 are arranged concentrically, a horizontal plane F passing through the central axis of the inner cylinder 4 and the outer cylinder 5 through the gas blowing port 5b. H A vertical plane F that is lower and passes through the same central axis V Therefore, it is possible to easily form a flow of the culture solution 11 rotating in one direction in the culture vessel 2 and to easily generate a multiphase turbulent flow, a turbulent boundary layer, and a geltler vortex. In addition, as shown in FIG. V If it is formed on the opposite side, the flow of the culture solution 11 swirling in the opposite direction to the present embodiment (clockwise in FIG. 5) can be formed. In addition, although not shown, if gas inlets are formed on the left and right sides of the vertical plane passing through the central axis of the inner and outer cylinders, and the two inlets are alternately switched every predetermined time, the culture solution in the culture vessel The swirl direction can be switched alternately, and the culture solution can be stirred more efficiently. Furthermore, you may make it change the turning direction of the culture solution 11 partly or transiently partially in the longitudinal direction of the culture vessel 2. A plurality of gas injection ports 5b are arranged in the longitudinal direction of the culture vessel 2, and a culture vessel of the culture solution 11 is introduced into the culture vessel 2 by sequentially injecting gas from the gas injection ports 5b on one end side of the culture vessel 2 with a predetermined time difference. You may form the swirl | vortex flow which changes along 2 longitudinal directions. A plurality of gas blowing ports 5b are alternately arranged on the left and right of the vertical plane passing through the central axis of the inner cylinder along the longitudinal direction of the culture vessel 2, and the gas is blown from each gas blowing port 5b to enter the culture vessel 2 However, a swirl flow of the culture solution 11 may be alternately formed in the longitudinal direction.
By the way, in this embodiment, the inner tube 4 and the outer tube 5 made of a cylinder are arranged concentrically to constitute the culture vessel 2. However, as shown in FIG. 6, the inner tube 4 and the outer tube 5 made of a cylinder. The culture vessel 2 may be configured by arranging the gas outlets eccentrically, and in this case, the gas blowing port 4a is passed through the central axis of the inner cylinder 4 as shown in the horizontal plane F. H A vertical plane F that is lower and passes through the same central axis V Can be easily formed in the culture vessel 2 to swirl the culture medium 11 in the same direction (counterclockwise in the illustrated example), and mixed phase turbulence, turbulent boundary layer, Gerdler vortices are easy to generate.
Further, as shown in FIG. 7, an inner cylinder 4 ′ and an outer cylinder 5 ′ made of an elliptic cylinder are concentrically arranged to constitute a culture vessel 2 ′, or an inner cylinder made of a long cylinder as shown in FIG. The culture vessel 2 ″ may be configured by concentrically arranging 4 ″ and the outer cylinder 5 ″. In these cases, the gas inlets 4a ′ and 5b ″ are connected to the inner cylinder 4 ′ and 4 ″ and the outer cylinder 5 respectively. Horizontal plane F passing through the central axis of ', 5 " H A vertical plane F that is lower and passes through the same central axis V The flow of the culture solution 11 swirling in the same direction (counterclockwise in the illustrated example) can be formed in the culture vessels 2 ′ and 2 ″. In addition, the culture vessel may be configured by arranging the inner cylinder and the outer cylinder made of an elliptical cylinder or a long cylinder in an eccentric manner. In these cases, the gas inlet is located below the horizontal plane passing through the central axis of the inner cylinder. In addition, the flow of the culture solution swirling in the same direction can be formed in the culture vessel by arranging it on either the left or right side of the vertical plane passing through the same central axis.
Here, FIG. 9 shows an example of actual production equipment using the microalgae culture apparatus 1 according to the present embodiment. In the actual production equipment, a plurality of microalgae culture apparatuses 1 are arranged in a row as shown in the figure. Those connected continuously are arranged over several rows. In this case, each gas introduction pipe 14 and each two temperature-controlled water introduction pipes 19 are shared for each culture apparatus 1 in each row.
Next, the result of the culture experiment performed using the microalgae culture apparatus according to the present invention will be described.
Cultivation experiments were performed over 13 days using Chlorococcum litorale as a microalgae. In this case, the sunshine duration is 10 hours / day, and the photon amount in the south and middle is 800 μmol / m. 2 / S, daytime average photon amount 340 μmol / m 2 The culture result was an average growth rate of 0.15 g dry weight / liter / day. Also, no microalgae adhered to the culture vessel wall during the culture period.
In another culture experiment, as a result of culturing Spirulina platensis as a microalgae, the conventional culture pond system has a culture concentration of 0.3 to 0.5 g / liter and a daily productivity of 0.1. The microalgae culture apparatus according to the present invention has a good result of a culture concentration of 10 to 20 g / liter and a productivity per day of 2.8 to 7.0 g / liter, whereas it is ˜0.2 g / liter. It was.
<Industrial applicability>
As is clear from the above description, according to the present invention, a culture solution is placed in a culture vessel having an opening at the top, and visible light is incident while blowing a gas containing carbon dioxide into the culture solution. In the microalgae culturing apparatus for culturing microalgae in the culture vessel, the culture vessel is formed into a double cylinder composed of an inner cylinder and an outer cylinder placed horizontally, and at least the outer cylinder transmits visible light. Since the swirl flow of the culture solution is formed in the culture vessel by blowing the gas, it is possible to achieve sufficient productivity by realizing sufficient stirring of the culture solution, It is possible to obtain an effect that high culture efficiency can be maintained over a long period of time by preventing adhesion of microalgae to the culture vessel wall surface and precipitation on the bottom surface of the culture vessel.
Further, according to the present invention, a culture solution is placed in a culture vessel having an opening at the top, and a visible ray is incident on the culture solution by injecting a gas containing carbon dioxide into the culture solution. In a microalgae culture method for culturing microalgae, a culture vessel formed of a transparent material that transmits at least visible light, which is formed into a double cylinder shape with an inner cylinder and an outer cylinder placed concentrically The gas inlet opening at the lower part of the gas cylinder is arranged on either the left or right side of the vertical plane passing through the central axis of the inner cylinder and the outer cylinder, and the gas is blown from the gas inlet, or eccentrically placed horizontally. The gas injection port that opens at the bottom of the culture vessel formed of a transparent material that transmits visible light is formed at least by the inner cylinder and the outer cylinder. Arranged on either the left or right side of the vertical plane In addition, since the swirling flow of the culture solution is formed in the culture vessel by blowing the gas from the gas blowing port, sufficient agitation of the culture solution can be easily realized and high productivity can be obtained. It is possible to obtain an effect that high culture efficiency can be maintained over a long period of time by preventing algae from adhering to the culture vessel wall surface and precipitation on the bottom surface of the culture vessel.
[Brief description of the drawings]
FIG. 1 is a perspective view of a microalgae culture apparatus according to the present invention.
FIG. 2 is a cutaway front view (fracture sectional view in the direction of arrow A in FIG. 1) of the microalgae culture apparatus according to the present invention.
FIG. 3 is a side sectional view of the microalgae culture apparatus according to the present invention.
4 is a cross-sectional view taken along line BB in FIG.
FIG. 5 is a cross-sectional view showing another embodiment of the culture vessel of the microalgae culture apparatus according to the present invention.
FIG. 6 is a cross-sectional view showing another embodiment of the culture vessel of the microalgae culture apparatus according to the present invention.
FIG. 7 is a cross-sectional view showing another embodiment of the culture vessel of the microalgae culture apparatus according to the present invention.
FIG. 8 is a cross-sectional view showing another embodiment of the culture vessel of the microalgae culture apparatus according to the present invention.
FIG. 9 is a perspective view showing an example of actual production equipment using the microalgae culture apparatus according to the present invention.
In the figure, reference numeral 1 is a microalgae culture apparatus, 2,2 ', 2 "are culture vessels, 4,4', 4" are inner cylinders, 4a, 4a 'are gas inlets, 5,5,5, "Is an outer cylinder, 5b, 5b" is a gas inlet, 6 and 7 are side walls, 11 is a culture solution, 14 is a gas introduction pipe, 17 is a gas discharge opening, 18 is a cap, 19 is a temperature-controlled water introduction pipe It is.

Claims (8)

頂部に開口部を有する培養容器の中に培養液を入れ、該培養液中に二酸化炭素を含むガスを吹き込みつつ、可視光線を入射させることによって前記培養容器内で微細藻類を培養する微細藻類培養装置において、
前記培養容器を横置きされた内筒と外筒から成る二重円筒状に成形するとともに、少なくとも外筒を可視光線を透過する透明材料で構成し、前記培養容器内に前記培養液の旋回流を形成するためのガスを吹き込むガス吹込口を培養容器内下部に開口せしめたことを特徴とする微細藻類培養装置。
Microalgae culture for culturing microalgae in the culture vessel by putting visible light into the culture broth while blowing a gas containing carbon dioxide into the culture solution having an opening at the top In the device
The culture vessel is formed into a double cylindrical shape composed of a horizontally placed inner cylinder and an outer cylinder, and at least the outer cylinder is made of a transparent material that transmits visible light, and the swirling flow of the culture solution is put into the culture container. A microalgae culture apparatus characterized in that a gas inlet for injecting a gas for forming a gas is opened in the lower part of the culture vessel.
前記内筒と外筒を円筒、楕円筒又は長円筒で構成するとともに、これらの内筒と外筒を同心又は偏心させて配置したことを特徴とする請求の範囲第1項に記載の微細藻類培養装置。  The microalgae according to claim 1, wherein the inner cylinder and the outer cylinder are constituted by a cylinder, an elliptic cylinder, or a long cylinder, and the inner cylinder and the outer cylinder are arranged concentrically or eccentrically. Culture device. 頂部に開口部を有する培養容器の中に培養液を入れ、該培養液中に二酸化炭素を含むガスを吹き込みつつ、可視光線を入射させることによって前記培養容器内で微細藻類を培養する微細藻類培養方法において、
同心に横置された内筒と外筒とで二重円筒状に成形され、少なくとも外筒を可視光線を透過する透明材料で構成して成る培養容器の下部に開口するガス吹込口を、内筒と外筒の中心軸を通る鉛直面の左右何れか一方に配置し、該ガス吹込口から前記ガスを吹き込むことによって培養容器内に前記培養液の旋回流を形成することを特徴とする微細藻類培養方法。
Microalgae culture for culturing microalgae in the culture vessel by putting visible light into the culture broth while blowing a gas containing carbon dioxide into the culture solution having an opening at the top In the method
A gas blowing port that opens in the lower part of the culture vessel formed of a transparent material that is formed of a transparent material that allows visible light to pass through is formed into a double cylindrical shape by an inner cylinder and an outer cylinder that are concentrically placed, A fine arrangement characterized in that it is arranged on either the left or right side of the vertical plane passing through the central axis of the cylinder and the outer cylinder, and the swirling flow of the culture solution is formed in the culture vessel by blowing the gas from the gas blowing port. Algal culture method.
頂部に開口部を有する培養容器の中に培養液を入れ、該培養液中に二酸化炭素を含むガスを吹き込みつつ、可視光線を入射させることによって前記培養容器内で微細藻類を培養する微細藻類培養方法において、
偏心して横置きされた内筒と外筒とで二重円筒状に成形され、少なくとも外筒を可視光線を透過する透明材料で構成して成る培養容器の下部に開口するガス吹込口を、内筒の中心軸を通る鉛直面の左右何れか一方に配置し、該ガス吹込口から前記ガスを吹き込むことによって培養容器内に前記培養液の旋回流を形成することを特徴とする微細藻類培養方法。
Microalgae culture for culturing microalgae in the culture vessel by putting visible light into the culture broth while blowing a gas containing carbon dioxide into the culture solution having an opening at the top In the method
A gas injection port that opens at the bottom of a culture vessel formed of a transparent material that is formed of a transparent material that transmits visible light is formed into a double cylinder shape with an inner cylinder and an outer cylinder that are eccentrically placed horizontally. A method for culturing microalgae, which is arranged on either the left or right side of a vertical plane passing through the central axis of a cylinder and forms a swirling flow of the culture solution in a culture vessel by blowing the gas from the gas blowing port .
前記培養容器の内筒の中心軸を通る鉛直面の左右に前記ガス吹込口を配置し、両ガス吹込口を所定時間毎に交互に切り替えることによって培養容器内の培養液の旋回方向を交互に切り替えることを特徴とする請求の範囲第3項又は第4項に記載の微細藻類培養方法。  The gas blowing ports are arranged on the left and right of the vertical plane passing through the central axis of the inner cylinder of the culture vessel, and the swirl directions of the culture medium in the culture vessel are alternately switched by alternately switching both gas blowing ports every predetermined time. The method for culturing microalgae according to claim 3 or 4, wherein switching is performed. 前記培養容器の長手方向に複数のガス吹込口を配置し、培養容器の一端側のガス吹込口からガスを所定の時間差をもって順次吹き込むことによって培養容器内に培養液の前記培養容器の長手方向に沿って変化する旋回流を形成することを特徴とする請求の範囲第3項又は第4項に記載の微細藻類培養方法。  A plurality of gas injection ports are arranged in the longitudinal direction of the culture vessel, and gas is sequentially blown from the gas injection port on one end side of the culture vessel with a predetermined time difference in the culture vessel in the longitudinal direction of the culture vessel. The microalgae culture method according to claim 3 or 4, wherein a swirling flow that changes along the flow path is formed. 前記培養容器の長手方向に沿って複数のガス吹込口を内筒の中心軸を通る鉛直面の左右に交互に配置し、各ガス吹込口からガスを吹き込むことによって培養容器内に方向が長手方向に交互に異なる培養液の旋回流を形成することを特徴とする請求の範囲第3項又は第4項に記載の微細藻類培養方法。  A plurality of gas inlets are alternately arranged on the left and right of the vertical plane passing through the central axis of the inner cylinder along the longitudinal direction of the culture vessel, and the direction is longitudinal in the culture vessel by blowing gas from each gas inlet 5. The method of culturing microalgae according to claim 3 or 4, wherein swirl flows of different culture solutions are alternately formed. 前記培養容器の外筒外面への温調水の散水、外筒の外側に形成された水通路への温調水の通水又は内筒内への温調水の通水によって前記培養液の温度をコントロールすることを特徴とする請求の範囲第3項〜第7項の何れかに記載の微細藻類培養方法。  Sprinkling of temperature-controlled water to the outer surface of the outer cylinder of the culture vessel, passing temperature-controlled water to a water passage formed outside the outer cylinder, or passing temperature-controlled water into the inner cylinder The method for culturing microalgae according to any one of claims 3 to 7, wherein the temperature is controlled.
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