JP4405980B2 - Plant algae / microorganism photosynthesis reactor - Google Patents

Plant algae / microorganism photosynthesis reactor Download PDF

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JP4405980B2
JP4405980B2 JP2006139290A JP2006139290A JP4405980B2 JP 4405980 B2 JP4405980 B2 JP 4405980B2 JP 2006139290 A JP2006139290 A JP 2006139290A JP 2006139290 A JP2006139290 A JP 2006139290A JP 4405980 B2 JP4405980 B2 JP 4405980B2
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Description

本発明は、光合成反応器に関し、特に、植物性藻類・微生物光合成反応器に関する。   The present invention relates to a photosynthetic reactor, and more particularly to a plant algae / microbial photosynthetic reactor.

藍藻（スピルリナ、Spirulina）には、豊富なタンパク質やミネラル及び酵素など、人体に有益である複種類の栄養成分が含まれ、最近になって、食用に広く推薦される。藍藻の培養液は、十分な光合成により、必要とする養分を藻細胞に補給し、そして、培養液の中で生成した酸素を排出することによって、藍藻は、大量的に生長繁殖ができる。   Cyanobacteria (Spirulina) contains a variety of nutrients that are beneficial to the human body, such as abundant proteins, minerals and enzymes, and has recently been widely recommended for food. The culture solution of cyanobacteria can grow and reproduce in large quantities by supplying the necessary nutrients to the algal cells through sufficient photosynthesis and discharging the oxygen produced in the culture solution.

従来の藍藻の光合成反応方式は、藍藻の培養液を露天の大きな培養池の中に収納して、光合成を行わせる。しかし、大きな培養池は、大きな面積を占用すること、エネルギーの消費が膨大であること、使用上に天候の制限があること、そして、容易に汚染されることのため、藍藻の品質に悪影響を与え、生産業者にとって、解決すべき課題である。   In the conventional blue-green algae photosynthetic reaction method, the blue-green algae culture solution is stored in a large open-air culture pond for photosynthesis. However, large culture ponds have a negative impact on the quality of cyanobacteria because they occupy a large area, consume large amounts of energy, have limited weather on use, and are easily contaminated. It is a problem to be solved for the producer.

従来の他の藍藻の光合成反応方式は、藍藻の培養液を光合成反応器の中に収納して、光合成を行わせる。例えば、中国特許CN95219504.6号に記載されるスピルリナ光合成反応器は、反応塔と直立型両列平螺旋式導管とから構成される。これら反応塔と導管は、透光材質で作製され、その中の培養液を流して光合成を行わせるためのものである。反応塔の中には、泡立て板と温度交換器等の装置が設けられ、培養液の中に生成した酸素を排出することと培養液の温度を制御することに供する。スピルリナ光合成反応器は、主として、閉鎖式の循環系を提供することにより、従来の大きな培養池の様々な問題点を解決する。しかし、スピルリナ光合成反応器は、製造が複雑であること、コストが高いこと、容易に破損すること、酸素を排出し難いこと、培養液の温度を必要とする標準に制御し難いこと、反応塔の清浄や維持が簡単ではないことにより、光合成の効果の低減や藍藻の品質の不安定等の問題点があり、工業化の大量生産に向いていない。   According to another conventional method of photosynthetic reaction of cyanobacteria, a culture solution of cyanobacteria is stored in a photosynthesis reactor, and photosynthesis is performed. For example, the Spirulina photosynthetic reactor described in Chinese Patent CN95219504.6 is composed of a reaction tower and an upright double-row flat spiral conduit. These reaction towers and conduits are made of a light-transmitting material, and are used for carrying out photosynthesis by flowing a culture solution therein. In the reaction tower, devices such as a foaming plate and a temperature exchanger are provided to discharge oxygen generated in the culture solution and to control the temperature of the culture solution. The Spirulina photosynthetic reactor solves the various problems of conventional large culture ponds, mainly by providing a closed circulation system. However, Spirulina photosynthetic reactors are complex to manufacture, costly, easily broken, difficult to vent oxygen, difficult to control to standards that require the temperature of the culture solution, Since it is not easy to clean and maintain, there are problems such as reduced photosynthesis effects and instability in the quality of cyanobacteria, which are not suitable for industrial mass production.

以上の説明のように、上記従来の藍藻の光合成反応方式は、実際の製造や使用上では明らかに困難であり、欠点が存在するため、改善しなければならない。   As described above, the conventional cyanobacterial photosynthetic reaction method is obviously difficult in actual production and use, and has drawbacks, so it must be improved.

本発明者は、改善しなければならない上記の欠点があるため、慎重に研究を繰り返し、そして、知識的な運用に合わせて、設計が合理的で、有効的に上記の欠点を改善する本発明を提案する。   The present inventor has carefully repeated research due to the above-mentioned drawbacks that must be improved, and the present invention has a design that is rational and effectively ameliorates the above-mentioned disadvantages in accordance with the knowledge operation. Propose.

本発明の主な目的は、占用する面積が小さくなり、エネルギーの消費が低減され、稼働が天候の影響を受けず、そして、汚染されることのないように、藻類の優れた品質を維持できる植物性藻類・微生物光合成反応器を提供する。   The main object of the present invention is to maintain the excellent quality of algae so that the occupied area is reduced, the consumption of energy is reduced, the operation is not affected by the weather and is not contaminated. A plant algae / microbial photosynthetic reactor is provided.

本発明の目的は、培養液の中で生成した酸素を容易に且つ素早く排出することで、生産効率を向上することにより、工業化の大量生産に有利である植物性藻類・微生物光合成反応器を提供する。   An object of the present invention is to provide a plant algae / microbial photosynthetic reactor that is advantageous for industrial mass production by improving production efficiency by easily and quickly discharging oxygen produced in a culture solution. To do.

本発明の更に他の目的は、製造と組み立てが簡単で、容易に破損せず、コストが低減される植物性藻類・微生物光合成反応器を提供する。   Still another object of the present invention is to provide a plant algae / microbial photosynthetic reactor that is simple to manufacture and assemble, is not easily damaged, and reduces costs.

本発明の更に他の目的は、清浄や維持が簡単であることにより、光合成の効果や藻類の品質を確保できる植物性藻類・微生物光合成反応器を提供する。   Still another object of the present invention is to provide a plant algae / microorganism photosynthesis reactor that can ensure the effect of photosynthesis and the quality of algae by being easy to clean and maintain.

本発明の更に他の目的は、有効的に培養液の温度を制御する植物性藻類・微生物光合成反応器を提供する。   Still another object of the present invention is to provide a plant algae / microbial photosynthetic reactor that effectively controls the temperature of a culture solution.

上記の目的を達成するための本発明は、光合成反応管路と、加圧輸液モジュールと、酸素排出・調節モジュールとが含まれる植物性藻類・微生物光合成反応器を提供する。当該光合成反応管路は、透光管路である。当該加圧輸液モジュールの入り口端は、当該透光管路の出口端に連通される。当該酸素排出・調節モジュールには、中空の噴射酸素排出装置と中空の液面調節装置とが含まれる。当該噴射酸素排出装置には、互い組み合わされた酸素排出筒と集液筒とがある。当該酸素排出筒には、液入り口と上排気口と中空の管壁とがある。当該液入り口は、当該加圧輸液モジュールの出口端に連通される。当該上排気口は、当該酸素排出筒の上部に位置する。当該中空の管壁は、当該上排気口から下へ延びて当該液入り口の内側に位置する。当該液面調節装置には、調節筒が含まれる。当該調節筒は、当該集液筒に連通される。当該透光管路の入り口端は、当該調節筒に連通される。   To achieve the above object, the present invention provides a plant algae / microbial photosynthetic reactor including a photosynthetic reaction line, a pressurized infusion module, and an oxygen discharge / regulation module. The photosynthetic reaction conduit is a translucent conduit. The inlet end of the pressurized infusion module communicates with the outlet end of the translucent conduit. The oxygen discharge / regulation module includes a hollow injection oxygen discharge device and a hollow liquid level adjustment device. The jet oxygen discharge device includes an oxygen discharge cylinder and a liquid collection cylinder combined with each other. The oxygen discharge tube has a liquid inlet, an upper exhaust port, and a hollow tube wall. The liquid inlet communicates with the outlet end of the pressurized infusion module. The upper exhaust port is located above the oxygen exhaust cylinder. The hollow tube wall extends downward from the upper exhaust port and is located inside the liquid inlet. The liquid level adjustment device includes an adjustment cylinder. The adjustment cylinder communicates with the liquid collection cylinder. The entrance end of the translucent conduit is communicated with the adjustment cylinder.

当該光合成反応管路と当該加圧輸液モジュールと当該酸素排出・調節モジュールとを組み立てることにより、その中に注入された植物性藻類及び微生物の培養液及び藻種は、垂直的且つ立体的な多数の導管に閉鎖され、循環的に光合成と酸素排出とを行う。そのため、占用する面積が小さくなり、エネルギーの消費が低減され、稼働が天候の影響を受けず、そして、汚染されることのないように、藻類の品質を維持できる。また、当該液入り口と当該上排気口と当該中空の管壁との配置により、培養液の中で生成した酸素は、容易に且つ素早く排出され、生産効率が向上される。また、当該酸素排出筒と当該集液筒とからなる当該噴射酸素排出装置により、製造や組み立てが簡単で、容易に破損せず、コストの低減を実現する。当該酸素排出筒と当該集液筒との組み立てと、当該透光管路の設計とにより、清浄と維持とが容易にでき、光合成の効果や藻類の品質を確保する。   By assembling the photosynthetic reaction pipeline, the pressurized infusion module, and the oxygen discharge / regulation module, the plant algae and microorganism culture solutions and algal species injected therein are many vertical and three-dimensional species. It is closed by a conduit and performs photosynthesis and oxygen discharge cyclically. Therefore, the quality of the algae can be maintained so that the occupied area is reduced, the consumption of energy is reduced, the operation is not affected by the weather, and is not contaminated. In addition, due to the arrangement of the liquid inlet, the upper exhaust port, and the hollow tube wall, oxygen generated in the culture medium is easily and quickly discharged, and production efficiency is improved. In addition, the injection oxygen discharge device including the oxygen discharge cylinder and the liquid collection cylinder is easy to manufacture and assemble, is not easily damaged, and realizes cost reduction. The assembly of the oxygen discharge cylinder and the liquid collection cylinder and the design of the translucent pipe line facilitate cleaning and maintenance, and ensure the effect of photosynthesis and the quality of algae.

また、当該噴射酸素排出装置には、当該酸素排出筒の中に組み立てられる排気管がある。当該酸素排出筒の中段には、口絞り部と横排気口とが設けられる。当該横排気口は、当該口絞り部の下方に位置する。当該排気管の上端は、当該中空の管壁の中へ貫設される。当該排気管の下端には、当該横排気口の内側に位置する拡充部が形成される。これにより、培養液の中で生成した酸素が素早く排出される。   Further, the injection oxygen exhaust device has an exhaust pipe assembled in the oxygen exhaust cylinder. In the middle stage of the oxygen discharge cylinder, a mouth restricting portion and a lateral exhaust port are provided. The lateral exhaust port is located below the aperture restrictor. The upper end of the exhaust pipe penetrates into the hollow pipe wall. At the lower end of the exhaust pipe, an expanded portion located inside the lateral exhaust port is formed. Thereby, the oxygen produced | generated in the culture solution is discharged | emitted quickly.

また、本発明に係わる植物性藻類・微生物光合成反応器には、更に、当該透光管路の出口端と当該加圧輸液モジュールの入り口端との間に接続される加熱モジュールが設けられる。   Further, the plant algae / microorganism photosynthesis reactor according to the present invention is further provided with a heating module connected between the outlet end of the translucent conduit and the inlet end of the pressurized infusion module.

また、本発明に係わる植物性藻類・微生物光合成反応器には、更に、当該光合成反応管路の上方に位置する散水モジュールが設けられる。   Further, the plant algae / microorganism photosynthesis reactor according to the present invention is further provided with a watering module located above the photosynthesis reaction pipeline.

当該加熱モジュールと当該散水モジュールとの配置により、有効的に培養液の温度が制御される。   The temperature of the culture solution is effectively controlled by the arrangement of the heating module and the watering module.

以下の図面を用いた詳細な説明により、本発明に係わる目的や技術手段、効果及び特徴が良く分かるようになるが、図面はただ参考及び説明のためにあり、本発明はそれによって制限されるものではない。   The following detailed description using the drawings will provide a better understanding of the objects, technical means, effects, and features of the present invention. However, the drawings are only for reference and explanation, and the present invention is limited thereby. It is not a thing.

図１と図２は、本発明に係わる植物性藻類・微生物光合成反応器であり、これには、植物性藻類、微生物の培養液及び藻種が注入され、例えば、藍藻の培養液で循環的に光合成と酸素排出を行わせ、様々な栄養成分が含まれる藍藻を大量に生長繁殖できる。植物性藻類・微生物光合成反応器は、光合成反応管路１０と、加圧輸液モジュール２０と、酸素排出・調節モジュール３０とが含まれる。   1 and 2 are plant algae / microorganism photosynthesis reactors according to the present invention, in which plant algae, a culture solution of microorganisms and algae species are injected, for example, circulating in a culture solution of cyanobacteria. Can produce and reproduce a large amount of cyanobacteria containing various nutrients. The plant algae / microorganism photosynthesis reactor includes a photosynthesis reaction line 10, a pressurized infusion module 20, and an oxygen discharge / regulation module 30.

光合成反応管路１０は、藍藻の培養液をその中に流すための、ガラスやアクリル等の透光材質で作製される透光管路である。本実施例において、光合成反応管路１０には、複数の直管１２と複数の湾曲管１４とがあり、直管１２と湾曲管１４とにより、等間隔である両列の傾斜する立体螺旋式透光管路が形成され、その中を流れる培養液は、順に下へ周航するように流れ、そして、十分に光線を吸收して光合成を行う。透光管路において、最も上方の位置には、培養液及び藻種を注入し、透光管路の中の圧力を調節し、そして、透光管路を清浄するための補助開口１６が設けられる。   The photosynthetic reaction tube 10 is a light-transmitting tube made of a light-transmitting material such as glass or acrylic for flowing a culture solution of cyanobacteria therein. In the present embodiment, the photosynthetic reaction pipe line 10 includes a plurality of straight pipes 12 and a plurality of curved pipes 14, and the straight pipe 12 and the curved pipes 14 are inclined in two rows that are equidistant from each other. A light-transmitting conduit is formed, and the culture solution flowing through the conduit flows in order to circulate downward, and sufficiently absorbs light to perform photosynthesis. In the translucent pipe, an auxiliary opening 16 is provided at the uppermost position for injecting culture medium and algae species, adjusting the pressure in the translucent pipe, and cleaning the translucent pipe. It is done.

加圧輸液モジュール２０は、入り口端が透光管路の出口端に連通される加圧輸液ポンプである。   The pressurized infusion module 20 is a pressurized infusion pump whose inlet end communicates with the outlet end of the translucent conduit.

酸素排出・調節モジュール３０は、中空の噴射酸素排出装置４０と、中空の液面調節装置５０と、連通装置６０とが含まれる。噴射酸素排出装置４０には、組み合わせられる酸素排出筒４２と集液筒４４とが含まれ、酸素排出筒４２は、ステンレス材質で作製され、集液筒４４は、ガラスやアクリル等の透光材質で作製されてよいが、それは、容易な製造と組み立てのためであり、その材質はそれによって制限されない。酸素排出筒４２の上段には、液入り口４２１と、上排気口４２２と、中空の管壁４２３とが設けられ、液入り口４２１は、輸送管２２で、加圧輸液モジュール２０の出口端と連通され、上排気口４２２は、酸素排出筒４２の上部に位置し、中空の管壁４２３は、上排気口４２２から下へ延びて液入り口４２１の内側に位置する。酸素排出筒４２の中段には、口絞り部４２４と横排気口４２５とが設けられ、横排気口４２５は、口絞り部４２４の下方に位置する。噴射酸素排出装置４０には、更に排気管４６があり、この排気管４６は、酸素排出筒４２の中に組み立てられ、排気管４６の上端は、中空の管壁４２３の中に貫設され、排気管４６の下端には、横排気口４２５の内側に位置する拡充部４６１が形成される。液面調節装置５０には、組み合わされる延伸筒５２と調節筒５４とが含まれ、延伸筒５２は、ステンレス材質で作製され、延伸筒５２と調節筒５４の内壁を容易に清浄するために、延伸筒上段５２２と延伸筒下段５２３との２段に分けてもいいし、また、調節筒５４は、ガラスやアクリル等の透光材質で作製されてもよいが、それは、容易に製造と組み立てのためであり、その材質はそれによって制限されない。延伸筒５２の上部には、圧力調整開口５２１が設けられる。連通装置６０は、集液筒４４の底部と調節筒５４の底部に接続され、これにより、調節筒５４は集液筒４４に連通される。連通装置６０には、更に清浄バルブ部品６２がある。透光管路の入り口端は、下へ湾曲して調節筒５４に連通される。   The oxygen discharge / regulation module 30 includes a hollow injection oxygen discharge device 40, a hollow liquid level adjustment device 50, and a communication device 60. The injection oxygen discharge device 40 includes an oxygen discharge tube 42 and a liquid collection tube 44 to be combined. The oxygen discharge tube 42 is made of a stainless material, and the liquid collection tube 44 is made of a light-transmitting material such as glass or acrylic. However, it is for easy manufacturing and assembly, and its material is not limited thereby. A liquid inlet 421, an upper exhaust port 422, and a hollow tube wall 423 are provided in the upper stage of the oxygen discharge cylinder 42, and the liquid inlet 421 communicates with the outlet end of the pressurized infusion module 20 through the transport pipe 22. The upper exhaust port 422 is located at the upper part of the oxygen exhaust cylinder 42, and the hollow tube wall 423 extends downward from the upper exhaust port 422 and is located inside the liquid inlet 421. A mouth restricting portion 424 and a lateral exhaust port 425 are provided in the middle stage of the oxygen discharge cylinder 42, and the lateral exhaust port 425 is located below the mouth restricting portion 424. The injection oxygen exhaust device 40 further includes an exhaust pipe 46, which is assembled in the oxygen exhaust cylinder 42, and the upper end of the exhaust pipe 46 is provided through the hollow pipe wall 423. At the lower end of the exhaust pipe 46, an enlarged portion 461 located inside the lateral exhaust port 425 is formed. The liquid level adjusting device 50 includes an extending cylinder 52 and an adjusting cylinder 54 to be combined. The extending cylinder 52 is made of a stainless steel material, and in order to easily clean the inner walls of the extending cylinder 52 and the adjusting cylinder 54, The drawing cylinder upper stage 522 and the drawing cylinder lower stage 523 may be divided into two stages, and the adjustment cylinder 54 may be made of a light-transmitting material such as glass or acrylic, but it is easily manufactured and assembled. And its material is not limited thereby. A pressure adjustment opening 521 is provided in the upper part of the drawing cylinder 52. The communication device 60 is connected to the bottom of the liquid collection cylinder 44 and the bottom of the adjustment cylinder 54, whereby the adjustment cylinder 54 is communicated with the liquid collection cylinder 44. The communication device 60 further includes a cleaning valve component 62. The entrance end of the translucent conduit is curved downward and communicated with the adjustment cylinder 54.

本発明の植物性藻類・微生物光合成反応器には、更に、採集バルブ部品７０が含まれる。採集バルブ部品７０は、透光管路の出口端と加圧輸液モジュール２０の入り口端との間に接続され、透光管路の中で流れる培養液を汲取る。   The plant algae / microorganism photosynthesis reactor of the present invention further includes a collection valve component 70. The collection valve part 70 is connected between the outlet end of the light-transmitting conduit and the inlet end of the pressurized infusion module 20 and pumps the culture fluid flowing in the light-transmitting conduit.

本発明の植物性藻類・微生物光合成反応器を使用する時、藍藻の培養液を透光管路の補助開口１６から透光管路の中に注入する。培養液は、透光管路の中を流れ、光合成を行って酸素を生成し、加圧輸液モジュール２０へ流れる。培養液は、延伸筒５２の圧力調整開口５２１から調節筒５４の中に注入してもいい。加圧輸液モジュール２０を駆動して、培養液を強制的に透光管路から酸素排出・調節モジュール３０へ流す。培養液が液入り口４２１を介して酸素排出筒４２の中に噴射する時、その培養液は、まず、酸素排出・調節モジュール３０の酸素排出筒４２に衝突して空間を飛んで回転し、酸素が上排気口４２２から有効（ないし好適）に排出される。また、培養液は、落下して口絞り部４２４に收集された後、排気管４６の拡充部４６１に衝突して空間を飛んで拡散し、酸素が横排気口４２５から有効に排出される。最後に、培養液は、落下して集液筒４４の中に收集され、酸素が排気管４６の上端から有効に排出される。これにより、殆どの酸素が排出されるため、培養液による光合成の能力が向上される。培養液は、酸素排出筒４２を通過する時、酸素を一杯含有する液体になっているため、光合成を行い難いので、酸素排出筒４２は、ステンレス等の不透光材質で作製されてもよい。一方、培養液は、集液筒４４に收集された時、殆どの酸素が排出されているため、光合成を続行するので、集液筒４４は、ガラス等の透光材質で作製される。これにより、酸素排出筒４２と集液筒４４とは、製造と組み立てがより簡単で、また、破損しにくい。培養液は、連通装置６０を介して調節筒５４まで流された時、一時的に清浄バルブ部品６２を駆動して、比較的に重い沈降物を清浄してもいいし、培養液をサンプリングしてテストしてもいい。圧力調整開口５２１は、排気して液面調節装置５０の中の圧力を維持することに供するが、液面調節装置５０の中で生成した余計な泡を当該圧力調整開口５２１から吸い取ることもできるほか、圧力調整開口５２１に補給管を貫設すれば、例えば二酸化炭素など、培養液の生長繁殖に有利な養分を添加することもできる。加圧輸液モジュール２０の圧力により、透光管路の中において負圧になるため、培養液は、調節筒５４から透光管路の中に吸い取られ、再び光合成を行う。透光管路の中の圧力が増大するため、液面調節装置５０の中の培養液の液面が上昇した場合、加圧輸液モジュール２０の出力圧を調整して、培養液の液面を降下させる。これにより、培養液は、垂直的且つ立体的な多数の導管に閉鎖され、循環的に光合成と酸素排出とを行い、より多い栄養成分を成長することが実現される。培養液は、採集バルブ部品７０からサンプリングされてテストされ、培養液は、必要とする養分濃度に達する時、採集バルブ部品７０や清浄バルブ部品６２から排出されて採集される。   When the plant algae / microorganism photosynthesis reactor of the present invention is used, a culture solution of cyanobacteria is injected into the light transmission line from the auxiliary opening 16 of the light transmission line. The culture fluid flows through the light-transmitting conduit, performs photosynthesis, generates oxygen, and flows to the pressurized infusion module 20. The culture solution may be injected into the adjustment cylinder 54 from the pressure adjustment opening 521 of the extension cylinder 52. The pressurized infusion module 20 is driven, and the culture solution is forced to flow from the light transmission line to the oxygen discharge / regulation module 30. When the culture solution is injected into the oxygen discharge cylinder 42 through the liquid inlet 421, the culture solution first collides with the oxygen discharge cylinder 42 of the oxygen discharge / regulation module 30 and rotates in a space to rotate. Is effectively (or preferably) discharged from the upper exhaust port 422. In addition, the culture solution falls and is collected in the mouth restrictor 424, then collides with the expansion portion 461 of the exhaust pipe 46, flies through the space and diffuses, and oxygen is effectively discharged from the lateral exhaust port 425. Finally, the culture solution falls and is collected in the collection tube 44, and oxygen is effectively discharged from the upper end of the exhaust pipe 46. Thereby, since most oxygen is discharged | emitted, the capability of the photosynthesis by a culture solution improves. Since the culture solution is a liquid that contains a full amount of oxygen when passing through the oxygen discharge tube 42, it is difficult to perform photosynthesis, and therefore the oxygen discharge tube 42 may be made of an opaque material such as stainless steel. . On the other hand, since most of oxygen is exhausted when the culture solution is collected in the collection tube 44, photosynthesis is continued, so the collection tube 44 is made of a translucent material such as glass. Thereby, the oxygen discharge cylinder 42 and the liquid collection cylinder 44 are easier to manufacture and assemble, and are less likely to be damaged. When the culture solution is flowed to the control cylinder 54 via the communication device 60, the cleaning valve component 62 may be temporarily driven to clean a relatively heavy sediment, or the culture solution may be sampled. You can test it. The pressure adjustment opening 521 serves to evacuate and maintain the pressure in the liquid level adjustment device 50, but it is also possible to suck out excess bubbles generated in the liquid level adjustment device 50 from the pressure adjustment opening 521. In addition, if a replenishment pipe is provided through the pressure adjustment opening 521, for example, carbon dioxide or the like can be added to a nutrient that is advantageous for growth and propagation of the culture solution. Since the pressure of the pressurized infusion module 20 causes a negative pressure in the light-transmitting conduit, the culture solution is sucked into the light-transmitting conduit from the adjustment tube 54 and again performs photosynthesis. When the liquid level of the culture solution in the liquid level control device 50 rises because the pressure in the light transmission line increases, the output pressure of the pressurized infusion module 20 is adjusted to change the level of the culture solution. Lower. As a result, the culture solution is closed to a large number of vertical and three-dimensional conduits, and it is possible to cyclically perform photosynthesis and oxygen discharge to grow more nutrient components. The culture fluid is sampled and tested from the collection valve component 70, and the culture fluid is discharged from the collection valve component 70 and the clean valve component 62 and collected when the required nutrient concentration is reached.

本発明の植物性藻類・微生物光合成反応器には、更に、加熱モジュール８０が設けられる。加熱モジュール８０には、複数の加熱管８２と、入り口スイッチング部８４と、出口スイッチング部８６とが設けられる。加熱管８２は、夫々、入り口スイッチング部８４と出口スイッチング部８６とを介して、透光管路の出口端と加圧輸液モジュール２０の入り口端との間に接続される。加熱モジュール８０は、手動式や自動感応式で、加熱モジュール８０の中に収納される水を加熱することにより、水の熱エネルギーが加熱管８２に伝達されて、培養液の温度を制御する。加熱管８２は、ステンレス材質で作製されることにより、加熱の効果や耐久性が向上される。   The plant algae / microorganism photosynthesis reactor of the present invention is further provided with a heating module 80. The heating module 80 is provided with a plurality of heating tubes 82, an entrance switching unit 84, and an exit switching unit 86. The heating pipe 82 is connected between the outlet end of the translucent conduit and the inlet end of the pressurized infusion module 20 via the inlet switching unit 84 and the outlet switching unit 86, respectively. The heating module 80 is manually or automatically sensitive, and heats the water stored in the heating module 80, whereby the heat energy of the water is transmitted to the heating tube 82 to control the temperature of the culture solution. The heating tube 82 is made of stainless steel, so that the heating effect and durability are improved.

本発明の植物性藻類・微生物光合成反応器には、更に、散水モジュール９０が設けられる。散水モジュール９０は、光合成反応管路１０の上方に位置し、また、ワーク環境の必要に従って、手動式や自動感応式で定期定温で散水し、透光管路の中にある培養液の温度を降下させる。   The plant algae / microorganism photosynthesis reactor of the present invention is further provided with a watering module 90. The water sprinkling module 90 is located above the photosynthetic reaction pipe 10 and sprays water at a regular constant temperature manually or automatically according to the needs of the work environment to control the temperature of the culture solution in the light transmitting pipe. Lower.

以上の説明は、ただ、本発明のより良い実施例であり、本発明の特許請求の範囲は、それにより制限されるものではないため、本発明の特許請求の範囲や明細書の内容に従って、簡単な等価変化や修正すべては、本発明の特許請求の範囲に含まれている。   The above description is merely a better embodiment of the present invention, and the scope of the claims of the present invention is not limited thereby. Therefore, according to the scope of the claims of the present invention and the contents of the specification, All simple equivalent changes and modifications are within the scope of the claims of the present invention.

本発明に係わる植物性藻類・微生物光合成反応器の一部の断面概念図である。1 is a conceptual cross-sectional view of a part of a plant algae / microorganism photosynthesis reactor according to the present invention. 本発明に係わる植物性藻類・微生物光合成反応器の噴射酸素排出装置の立体概念図である。It is a three-dimensional conceptual diagram of the injection oxygen discharge device of the plant algae / microorganism photosynthesis reactor according to the present invention.

符号の説明Explanation of symbols

１０ 光合成反応管路
１２ 直管
１４ 湾曲管
１６ 補助開口
２０ 加圧輸液モジュール
２２ 輸送管
３０ 酸素排出・調節モジュール
４０ 噴射酸素排出装置
４２ 酸素排出筒
４２１ 液入り口
４２２ 上排気口
４２３ 中空な管壁
４２４ 口絞り部
４２５ 横排気口
４４ 集液筒
４６ 排気管
４６１ 拡充部
５０ 液面調節装置
５２ 延伸筒
５２１ 圧力調整開口
５２２ 延伸筒上段
５２３ 延伸筒下段
５４ 調節筒
６０ 連通装置
６２ 清浄バルブ部品
７０ 採集バルブ部品
８０ 加熱モジュール
８２ 加熱管
８４ 入り口スイッチング部
８６ 出口スイッチング部
９０ 散水モジュール DESCRIPTION OF SYMBOLS 10 Photosynthesis reaction pipe | tube 12 Straight pipe 14 Curved pipe 16 Auxiliary opening 20 Pressurized infusion module 22 Transport pipe 30 Oxygen discharge | emission adjustment module 40 Oxygen discharge apparatus 42 Oxygen discharge cylinder 421 Liquid inlet 422 Upper exhaust port 423 Hollow pipe wall 424 Mouth restricting portion 425 Horizontal exhaust port 44 Liquid collecting cylinder 46 Exhaust pipe 461 Expansion portion 50 Liquid level adjusting device 52 Stretching cylinder 521 Pressure adjusting opening 522 Stretching cylinder upper stage 523 Stretching cylinder lower stage 54 Adjustment cylinder 60 Communication device 62 Clean valve part 70 Collection valve Parts 80 Heating module 82 Heating tube 84 Entrance switching unit 86 Exit switching unit 90 Sprinkling module

Claims (5)

透光管路である光合成反応管路と、
入り口端が当該透光管路の出口端に連通される加圧輸液モジュールと、
中空の噴射酸素排出装置及び中空の液面調節装置を含む酸素排出・調節モジュールとを備え、
当該噴射酸素排出装置には、互いに組み合わされた酸素排出筒と集液筒とがあり、
当該酸素排出筒には、液入り口と上排気口と中空の管壁とがあり、
当該液入り口は、当該加圧輸液モジュールの出口端に連通され、
当該上排気口は、当該酸素排出筒の上部に位置し、
当該中空の管壁は、当該上排気口から下へ延びて当該液入り口の内側に位置し、
当該液面調節装置には、調節筒が含まれ、
当該調節筒は、当該集液筒に連通され、
当該透光管路の入り口端は、当該調節筒に連通され、
当該噴射酸素排出装置には、排気管があり、
当該排気管は、当該酸素排出筒の中に組み立てられ、
当該酸素排出筒の中段には、口絞り部と横排気口とが設けられ、
当該横排気口は、当該口絞り部の下方に位置し、
当該排気管の上端は、当該中空の管壁の中に貫設され、
当該排気管の下端には、当該横排気口の内側に位置する拡充部が形成される
ことを特徴とする植物性藻類・微生物光合成反応器。 A photosynthetic reaction line that is a light-transmitting line;
A pressurized infusion module whose inlet end communicates with the outlet end of the translucent conduit;
An oxygen discharge / regulation module including a hollow injection oxygen discharge device and a hollow liquid level adjustment device,
The jet oxygen discharge device has an oxygen discharge cylinder and a liquid collection cylinder combined with each other,
The oxygen exhaust tube has a liquid inlet, an upper exhaust port, and a hollow tube wall,
The liquid inlet communicates with the outlet end of the pressurized infusion module,
The upper exhaust port is located above the oxygen exhaust cylinder,
The hollow tube wall extends downward from the upper exhaust port and is located inside the liquid inlet,
The liquid level adjustment device includes an adjustment cylinder,
The adjustment cylinder communicates with the liquid collection cylinder,
The entrance end of the translucent conduit is communicated with the adjustment cylinder ,
The injection oxygen exhaust device has an exhaust pipe,
The exhaust pipe is assembled in the oxygen exhaust cylinder,
The middle stage of the oxygen exhaust cylinder is provided with a mouth restrictor and a lateral exhaust port,
The lateral exhaust port is located below the throttle part,
The upper end of the exhaust pipe penetrates into the hollow pipe wall,
A plant algae / microorganism photosynthesis reactor characterized in that an expanded portion located inside the horizontal exhaust port is formed at the lower end of the exhaust pipe . 複数の直管と複数の湾曲管とにより、等間隔である両列の傾斜する立体螺旋式透光管路を形成することを特徴とする請求項１記載の植物性藻類・微生物光合成反応器。   2. The plant algae / microorganism photosynthesis reactor according to claim 1, wherein a plurality of straight pipes and a plurality of curved pipes form a three-dimensional spiral light-transmitting pipe line that is inclined in both rows at equal intervals. 当該透光管路の最も上方の位置に、補助開口が設けられることを特徴とする請求項１記載の植物性藻類・微生物光合成反応器。   The plant algae / microorganism photosynthesis reactor according to claim 1, wherein an auxiliary opening is provided at an uppermost position of the light transmission conduit. 当該液面調節装置には、組み合わせられる延伸筒と当該調節筒とが含まれ、
当該延伸筒には、圧力調整開口が設けられる
ことを特徴とする請求項１記載の植物性藻類・微生物光合成反応器。 The liquid level adjusting device includes an extending cylinder and the adjusting cylinder to be combined,
The plant algae / microorganism photosynthesis reactor according to claim 1 , wherein the extending cylinder is provided with a pressure adjusting opening . 当該酸素排出・調節モジュールには、連通装置が含まれ、
当該連通装置は、当該集液筒の底部と当該調節筒の底部に接続され、
また、当該連通装置には、清浄バルブ部品がある
ことを特徴とする請求項１記載の植物性藻類・微生物光合成反応器。 The oxygen discharge / regulation module includes a communication device,
The communication device is connected to the bottom of the liquid collection cylinder and the bottom of the adjustment cylinder,
The plant algae / microorganism photosynthesis reactor according to claim 1 , wherein the communication device includes a clean valve component .
JP2006139290A 2004-09-21 2006-05-18 Plant algae / microorganism photosynthesis reactor Expired - Fee Related JP4405980B2 (en)

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TW93215067 2004-09-21

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DE102007012745A1 (en) * 2007-03-16 2008-09-25 Chao-Hui Lu Method and system of photosynthetic reaction of algae and microbes
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FR2943685B1 (en) 2009-03-25 2011-04-29 Microphyt PHOTOSYNTHETIC REACTOR FOR MICROORGANIC CULTURE AND METHOD FOR CULTIVATION OF MICROORGANISMS
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EP2499229B1 (en) 2009-11-10 2015-03-04 Microphyt Reaction casing for a photosynthetic reactor and associated photosynthetic reactor
US8822199B2 (en) 2009-11-10 2014-09-02 Microphyt Reaction jacket for a photosynthetic reactor and related photosynthetic reactor
JP5646895B2 (en) * 2010-07-20 2014-12-24 株式会社日立製作所 Culture tank
JP5658938B2 (en) * 2010-07-28 2015-01-28 バイオジェニック株式会社 Algae culture equipment
FR2982874B1 (en) 2011-11-17 2013-12-20 Microphyt REACTION ENVELOPE FOR A PHOTOSYNTHETIC REACTOR AND ASSOCIATED PHOTOSYNTHETIC REACTOR
EP2961824A1 (en) * 2013-02-26 2016-01-06 Heliae Development LLC Modular tubular bioreactor
WO2018019659A1 (en) 2016-07-29 2018-02-01 Algowinn Facility for culturing photosynthetic microorganisms, in particular microalgae, in a pond
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