JP3463062B2 - Photosynthetic reactor with built-in light energy converter - Google Patents
Photosynthetic reactor with built-in light energy converterInfo
- Publication number
- JP3463062B2 JP3463062B2 JP18157997A JP18157997A JP3463062B2 JP 3463062 B2 JP3463062 B2 JP 3463062B2 JP 18157997 A JP18157997 A JP 18157997A JP 18157997 A JP18157997 A JP 18157997A JP 3463062 B2 JP3463062 B2 JP 3463062B2
- Authority
- JP
- Japan
- Prior art keywords
- light
- photosynthetic
- reactor
- light energy
- energy
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/02—Photobioreactors
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/02—Form or structure of the vessel
- C12M23/04—Flat or tray type, drawers
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M31/00—Means for providing, directing, scattering or concentrating light
- C12M31/02—Means for providing, directing, scattering or concentrating light located outside the reactor
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- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Zoology (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- General Health & Medical Sciences (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- Biomedical Technology (AREA)
- Molecular Biology (AREA)
- Clinical Laboratory Science (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Photovoltaic Devices (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、微生物を利用して
光合成を行うための光合成リアクターに関し、光合成に
おける光エネルギーの有効利用に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a photosynthetic reactor for photosynthesis utilizing microorganisms, and more particularly to effective utilization of light energy in photosynthesis.
【0002】[0002]
【従来の技術】光合成微生物は、光照射下で水素などの
有用物質を生産する。光合成微生物を用いた物質生産
は、装置が簡単であることから光エネルギー変換方法と
して有用である。しかし効率的な物質生産を行うために
は、光合成リアクターの光エネルギー変換効率を高める
ことが必要である。Photosynthetic microorganisms produce useful substances such as hydrogen under light irradiation. The substance production using photosynthetic microorganisms is useful as a method for converting light energy because the device is simple. However, it is necessary to increase the light energy conversion efficiency of the photosynthetic reactor in order to efficiently produce substances.
【0003】従来の光合成リアクターとして代表的なも
のは、図6に示したような平板型の培養器あるいは構造
物1である。その受光面2に太陽光3が当たり、受光面
2を透過し、内部に培養されている微生物により光エネ
ルギーが利用され、物質生産が行われる。このタイプの
光合成リアクターは構造が単純であり、メンテナンスも
容易であるという利点を持つ。A typical conventional photosynthetic reactor is a plate-type incubator or structure 1 as shown in FIG. Sunlight 3 hits the light-receiving surface 2, passes through the light-receiving surface 2, and the light energy is utilized by the microorganisms cultured inside to carry out the substance production. This type of photosynthetic reactor has the advantages of simple structure and easy maintenance.
【0004】また、光エネルギー変換効率の向上を目的
として、様々な改良が行われている。例えば実公昭60
−19580号では、光合成リアクターの受光面に1つ
以上の光透過可能なくぼみを設けることで、体積当たり
の受光面積を増大させている。またApplied B
iochem.Biotechnol.,34/35,
449−458,1992では、海産シアノバクテリウ
ムの一種であるシネココッカス(Synechococ
cus sp.Optiumu)を培養してCO2放出
とバイオマスの形成を行う際に、面発光型の光ファイバ
(光拡散光ファイバ)を光合成リアクター内部に配置す
ることで、より多くの菌体に光を照射できるようにし
て、高密度培養を可能にしている。Various improvements have been made for the purpose of improving the light energy conversion efficiency. For example, real public sho 60
In No. -19580, the light receiving area per volume is increased by providing one or more light-transmitting depressions on the light receiving surface of the photosynthetic reactor. See also Applied B
iochem. Biotechnol. , 34/35,
449-458, 1992, Synechococc, which is a type of marine cyanobacterium.
cus sp. Optomu) is cultured to release CO 2 and form biomass, by arranging a surface-emission type optical fiber (light diffusion optical fiber) inside the photosynthesis reactor, more cells can be irradiated with light. Thus, high density culture is possible.
【0005】しかしこれら従来の光合成リアクターは、
単に光伝達体を用いて光合成リアクター内部に光を伝
達、分散照射させるものであり、構造が複雑であり、メ
ンテナンスに不便である点や、コスト的に不利であると
いった問題点がある。However, these conventional photosynthetic reactors are
The light is simply transmitted to the inside of the photosynthesis reactor by using a light transmitter to disperse and irradiate the light, and there are problems that the structure is complicated, maintenance is inconvenient, and cost is disadvantageous.
【0006】[0006]
【発明が解決しようとする課題】一般に、光合成微生物
の物質生産速度は、照射する光エネルギー強度に比例し
て増加するが、光エネルギー強度がある値を超えると、
それ以上は増加しなくなる。この光エネルギー強度を飽
和光エネルギー強度とよぶ。一例を示すと、光合成細菌
Rhodobactor sphaeroides R
V(ロドバクタースフェロイデスsp.‐RV、寄託番
号FERMP−7254号)の水素発生における飽和光
エネルギー強度は約0.3kW/m2 である。Generally, the substance production rate of photosynthetic microorganisms increases in proportion to the light energy intensity of irradiation, but when the light energy intensity exceeds a certain value,
It will not increase any further. This light energy intensity is called saturated light energy intensity. As an example, the photosynthetic bacterium Rhodobacter sphaeroides R
V (Rhodobacter sphaeroides sp.-RV, Deposit No. FERMP-7254) has a saturated light energy intensity of about 0.3 kW / m 2 in hydrogen generation.
【0007】ところが、実際には太陽光の光エネルギー
強度は、日照時間の大半において、0.3kW/m2 以
上である。したがって、光合成微生物に太陽光を照射す
る場合、大部分の光エネルギーが無駄になる。このよう
に太陽光の光エネルギー強度が大きすぎることが、光エ
ネルギー変換効率の向上を妨げる原因であることが判明
した。However, in reality, the light energy intensity of sunlight is 0.3 kW / m 2 or more in most of the sunshine hours. Therefore, when the photosynthetic microorganisms are irradiated with sunlight, most of the light energy is wasted. It has been found that such an excessively high light energy intensity of sunlight is a cause of hindering the improvement of light energy conversion efficiency.
【0008】従って、本発明は物質生産量を低下させる
ことなく、物質生産に利用されない光エネルギーを他の
エネルギーとして回収できる光合成リアクターおよび光
合成微生物の培養方法を提供することを目的とする。[0008] Therefore, an object of the present invention is to provide a photosynthetic reactor and a method for culturing photosynthetic microorganisms, which can recover light energy not used for the production of substances as other energy without reducing the amount of substances produced.
【0009】[0009]
【課題を解決するための手段】本発明者らは前述した課
題を解決する手段として、光合成リアクター表面を光エ
ネルギー変換体で部分的に覆うことで、物質生産量を低
下させることなく、これまで無駄になっていた光エネル
ギーを他のエネルギーとして回収できることを見出し
た。As a means for solving the above-mentioned problems, the present inventors have partially covered the surface of the photosynthesis reactor with a photoenergy converter, so that the material production amount has not been lowered, and thus far. It was found that the wasted light energy can be recovered as other energy.
【0010】すなわち、本発明の光合成リアクターは、
光合成微生物を培養するための、光エネルギー変換体を
具えた光合成リアクターであって、前記光エネルギー変
換体は前記光合成微生物リアクターの受光面積の34%
を遮光し、前記光エネルギー変換体は集熱パイプを用い
た光熱変換装置であることを特徴とする。 That is, the photosynthetic reactor of the present invention is
A light energy converter for culturing photosynthetic microorganisms
A photosynthetic reactor comprising:
The substitute is 34% of the light receiving area of the photosynthetic microbial reactor
The light energy converter uses a heat collecting pipe
It is a photothermal conversion device .
【0011】また、本発明の光合成微生物の培養方法
は、光合成微生物を光合成リアクター内で培養する方法
において、前記光合成リアクターの受光面積の34%
を、集熱パイプを用いた光熱変換装置で遮光し、前記光
合成リアクターの受光面に光をあてることにより、光合
成微生物を培養して水素を生産させると共に、前記光熱
変換装置により光エネルギーを熱エネルギーに変換さ
せ、前記生産された水素および熱エネルギーを回収す
る、ことを特徴とする。The method for culturing the photosynthetic microorganism of the present invention
Is a method of culturing photosynthetic microorganisms in a photosynthetic reactor
At 34% of the light receiving area of the photosynthetic reactor
Is shielded by a photothermal conversion device using a heat collecting pipe,
By shining light on the light receiving surface of the synthesis reactor,
The adult microorganism is cultured to produce hydrogen, and
The light energy is converted into heat energy by the converter.
And recover the produced hydrogen and heat energy.
It is characterized by
【0012】[0012]
【0013】[0013]
【0014】[0014]
【0015】[0015]
【0016】[0016]
【0017】[0017]
【0018】[0018]
【0019】[0019]
【発明の実施の形態】光合成リアクターの受光面を完全
に構造物で覆えば、リアクター内部に光が浸透しないた
め物質生産は期待できない。しかし部分的に覆う場合
は、リアクター内部を対流や撹拌によって移動している
光合成微生物の菌体は、明の部分と暗の部分とを交互に
通過することになる。したがって菌体が単位時間に受け
る光エネルギー強度は、光合成リアクター表面をまった
く覆わない場合に比べて小さくなる。しかし菌体が受け
る光エネルギー強度が飽和光エネルギー強度を下回らな
ければ、光合成リアクター表面をまったく覆わない場合
と同量の物質生産が保証される。BEST MODE FOR CARRYING OUT THE INVENTION If the light receiving surface of a photosynthetic reactor is completely covered with a structure, no light will penetrate into the interior of the reactor, so that material production cannot be expected. However, when it is partially covered, the photosynthetic microorganisms moving inside the reactor by convection or stirring pass through the light and dark portions alternately. Therefore, the light energy intensity received by the bacterial cells per unit time is smaller than that when the surface of the photosynthetic reactor is not covered at all. However, if the light energy intensity received by the bacteria is not lower than the saturated light energy intensity, the same amount of substance production as when the photosynthetic reactor surface is not covered is guaranteed.
【0020】また、光合成リアクターの受光面を太陽電
池あるいは光熱変換装置などの光エネルギー変換体で覆
うことで、従来無駄になっていた光エネルギーを他のエ
ネルギー、特に電気エネルギー、温水として回収できる
ため、全体のエネルギー効率は著しく向上する。Further, by covering the light receiving surface of the photosynthesis reactor with a light energy converter such as a solar cell or a photothermal converter, the light energy which was conventionally wasted can be recovered as other energy, particularly electric energy and hot water. , The overall energy efficiency is significantly improved.
【0021】図1は本発明の光合成リアクターの一例を
示す模式的斜視図である。光合成リアクター10はその
少なくとも1つの外表面を受光面11とし、この受光面
11は光源からの光12の光エネルギーが内部に透過す
る材質で形成されている。受光面11上にはその一部に
遮光部13が設けられている。遮光部13の形状は
(A)に示すようにストライプ状でも、(B)に示すよ
うにパッチ状でも、(C)に示すようにメッシュ状であ
っても、あるいは他のパターンをしていてもよい。遮光
部13は光を内部に透過せず、光エネルギーを他のエネ
ルギーに変換する光エネルギー変換体で形成されてい
る。光源としては太陽光、白熱灯、アーク灯、蛍光灯等
が利用できる。光エネルギー変換体としては、例えば太
陽電池などの光電変換装置、熱媒体例えば水を循環させ
た集熱用パイプを接続した光熱変換装置等がある。光合
成リアクター10にはその入口部14から光合成微生物
を培養基とともに装入し、図示しないキャップをして太
陽光12にあて培養する。同時に、遮光部でとらえた光
エネルギーを電気エネルギーや熱エネルギーの形で利用
する。FIG. 1 is a schematic perspective view showing an example of the photosynthetic reactor of the present invention. At least one outer surface of the photosynthesis reactor 10 is a light receiving surface 11, and the light receiving surface 11 is formed of a material through which the light energy of the light 12 from the light source is transmitted. A light shielding portion 13 is provided on a part of the light receiving surface 11. The light-shielding portion 13 may have a stripe shape as shown in (A), a patch shape as shown in (B), a mesh shape as shown in (C), or another pattern. Good. The light-shielding portion 13 does not transmit light inside and is formed of a light energy converter that converts light energy into other energy. As the light source, sunlight, incandescent lamp, arc lamp, fluorescent lamp or the like can be used. Examples of the light energy converter include a photoelectric conversion device such as a solar cell and a light-heat conversion device connected with a heat collecting pipe in which a heat medium such as water is circulated. A photosynthetic microorganism is charged into the photosynthesis reactor 10 from the inlet 14 together with a culture medium, and a cap (not shown) is put on the photosynthesis reactor 10 to cultivate it in sunlight 12. At the same time, the light energy captured by the light shield is used in the form of electric energy or heat energy.
【0022】本発明に供される光合成微生物としては、
光エネルギーを利用して有用物質を産生するいずれの微
生物でもかまわないが、本例では光合成細菌Rhodo
bactor sphaeroides RV(ロドバ
クタースフェロイデスSP‐RV、寄託番号FERMP
−7254号)における水素生産について例示する。こ
の微生物は乳酸、酢酸、プロピオン酸等の脂肪酸を培地
として光合成により水素を放出する。The photosynthetic microorganisms used in the present invention include:
Although any microorganism that produces a useful substance by using light energy may be used, in this example, the photosynthetic bacterium Rhodo is used.
vector sphaeroides RV (Rhodobacter sphaeroides SP-RV, deposit number FERMP
No. 7254). This microorganism releases hydrogen by photosynthesis using fatty acids such as lactic acid, acetic acid, and propionic acid as a medium.
【0023】本菌を使用して光合成による水素生産を行
う場合、光量が増すにつれて受光面の遮蔽度と水素生産
量との関係は図2(A)に示すように、ほぼ0.3kW
/m2 の光エネルギー強度で飽和する。この飽和光エネ
ルギー強度以上では水素生産量は増加しない。そのた
め、光エネルギー強度の増加分は物質生産では利用され
ないことになる。従って、この利用されない分の光エネ
ルギーが内部に透過しないように受光面に遮蔽部を設
け、この遮蔽部で光合成には利用されないエネルギーを
受け、他のエネルギーの形で利用することにより全体的
なエネルギー利用効率を向上できる。図2(B)は受光
面の一部を遮光した場合の遮光率と水素生産量との関係
を示す。同図から明らかなように、遮光率34%に達す
るまでは水素生産量は低下せず、遮光率34%を越える
と水素生産量が低下する。従って遮光率を34%とと
し、すなわち、光エネルギーを他のエネルギーに振り向
ける割合が34%のときに全体の光エネルギー利用効率
が最適になることがわかる。When hydrogen is produced by photosynthesis using the present bacterium, as the amount of light increases, the relationship between the degree of shielding of the light receiving surface and the amount of hydrogen produced is approximately 0.3 kW, as shown in FIG. 2 (A).
Saturate at a light energy intensity of / m 2 . Above this saturated light energy intensity, hydrogen production does not increase. Therefore, the increase in light energy intensity will not be used in material production. Therefore, a shield is provided on the light-receiving surface so that the unused light energy is not transmitted to the inside, and this shield receives energy that is not used for photosynthesis, and by using it in the form of other energy, the overall Energy use efficiency can be improved. FIG. 2B shows the relationship between the light shielding rate and the hydrogen production amount when a part of the light receiving surface is shielded. As is clear from the figure, the hydrogen production amount does not decrease until the shading rate reaches 34%, and the hydrogen production amount decreases when the shading rate exceeds 34%. Therefore, it is understood that the light-shielding rate is set to 34%, that is, when the ratio of directing light energy to other energy is 34%, the overall light energy utilization efficiency is optimum.
【0024】[0024]
【実施例】以下に、本発明を実施例によりさらに詳細に
説明するが、本発明はこれらの実施例に限定されないこ
とはもちろんである。EXAMPLES The present invention will be described in more detail below with reference to examples, but it goes without saying that the present invention is not limited to these examples.
【0025】<実施例1>図3は、本発明の第1の実施
例による光エネルギー変換体組み込み型光合成リアクタ
ーの主要な構成部材の配置関係を示す模式的斜視図であ
る。図3において、光エネルギー変換体である太陽電池
13aは、光合成リアクターの受光面11上に、一定の
間隔をおいて配置される。この場合、遮光部としての太
陽電池13aの占める表面積が遮光部を設ける前の受光
面の面積に対して34%となるように設定した。この光
合成リアクターに光合成細菌Rhodobactor
sphaeroides RV(ロドバクタースフェロ
イデスSP‐RV、寄託番号FERMP−7254号)
と乳酸、酢酸、プロピオン酸等の脂肪酸を培地として装
入し、太陽光線を当てて培養したところ水素の発生と、
太陽電池による電力が得られた。<Embodiment 1> FIG. 3 is a schematic perspective view showing an arrangement relationship of main components of a photosynthetic reactor incorporating a light energy converter according to a first embodiment of the present invention. In FIG. 3, the solar cells 13a, which are light energy converters, are arranged on the light-receiving surface 11 of the photosynthesis reactor at regular intervals. In this case, the surface area occupied by the solar cell 13a as the light shielding portion was set to be 34% of the area of the light receiving surface before the light shielding portion was provided. The photosynthetic bacterium Rhodactor is added to this photosynthetic reactor.
sphaeroides RV (Rhodobacter sphaeroides SP-RV, deposit number FERMP-7254)
And fatty acids such as lactic acid, acetic acid, and propionic acid were added as a medium, and the cells were cultured by exposing them to sunlight.
Power from the solar cell was obtained.
【0026】<実施例2>図4は本発明の第2の実施例
による光エネルギー変換体組み込み型光合成リアクター
の主要な構成部材の配置関係を示す模式図である。図4
において、光エネルギー変換体である、光熱変換装置1
5に付随する集熱用パイプ16は、光合成リアクターの
受光面11上に、一定の間隔をおいて配置される。この
場合、投影図における集熱パイプの占める面積が集熱パ
イプを設ける前の受光面の面積の34%となるように設
定する。実施例1と同様に太陽光線を当てて光合成細菌
を培養したところ、水素が発生し、熱が回収された。<Embodiment 2> FIG. 4 is a schematic view showing an arrangement relationship of main constituent members of a photosynthetic reactor incorporating a light energy converter according to a second embodiment of the present invention. Figure 4
In, a photothermal conversion device 1 which is a light energy converter
The heat collecting pipes 16 associated with 5 are arranged at regular intervals on the light receiving surface 11 of the photosynthesis reactor. In this case, the area occupied by the heat collecting pipe in the projected view is set to be 34% of the area of the light receiving surface before the heat collecting pipe is provided. When the photosynthetic bacteria were cultured in the same manner as in Example 1 by applying sunlight, hydrogen was generated and heat was recovered.
【0027】<試験例1>図5は、本発明の実施例によ
る光エネルギー変換体組み込み型光合成リアクターの効
果を試験するために用いた実験装置の要部の構成を示す
模式図である。図5において、例えぱ、タングステンラ
ンプやハロゲンランプなどの白色光の光源20から出た
光は、恒温水槽21中に配置された光合成リアクター2
2に達する。光合成リアクター22内には光合成細菌懸
濁液23が満たされており、ここで発生した水素ガス2
4は、輸送管25を通って恒温水槽21中に置かれたガ
ラスシリンジ26に導かれる。ガラスシリンジ26はあ
らかじめ水で満たしておき、水素ガス24が導入される
とともに、水が底部から抜けるようにしてある。恒温水
槽21は温度制御装置(図示を省略)を用いて、水温を
30℃の一定温度としている。<Test Example 1> FIG. 5 is a schematic diagram showing the construction of the main part of an experimental apparatus used for testing the effect of the photosynthetic reactor incorporating a light energy converter according to the embodiment of the present invention. In FIG. 5, for example, light emitted from a white light source 20 such as a tungsten lamp or a halogen lamp is a photosynthesis reactor 2 arranged in a constant temperature water tank 21.
Reach 2. The photosynthetic reactor 22 is filled with the photosynthetic bacterial suspension 23, and the hydrogen gas 2 generated here is generated.
4 is guided through a transport pipe 25 to a glass syringe 26 placed in the constant temperature water bath 21. The glass syringe 26 is filled with water in advance so that the hydrogen gas 24 is introduced and water is discharged from the bottom. The constant temperature water tank 21 uses a temperature controller (not shown) to keep the water temperature constant at 30 ° C.
【0028】表1に実験に用いた四種類の光合成リアク
ターの受光面を示す模式図、および各光合成リアクター
から得られた水素発生量を示した。光合成リアクターA
およぴCは受光面に一切の構造物を配置していない。一
方、光合成リアクターBは太さ1cmの黒色の粘着テー
プを、光合成リアクターDはメッシュ状に編んだ金属製
ワイヤーを、それぞれ受光面の34%を遮光するように
貼付している。光合成リアクターAおよびBには培地と
して乳酸を、光合成リアクターCおよびDでは培地とし
て酢酸とプロピオン酸の1:1混合物を用いた。光合成
リアクターはいずれも、構造物(遮光部)を設けないと
きの受光面積は150cm2 であった。従って、遮光部
の面積は51cm2 であった。これらの光合成リアクタ
ーでそれぞれ光合成細菌Rhodobactor sp
haeroides RV(ロドバクタースフェロイデ
スSP‐RV、寄託番号FERMP−7254号)を培
養した。培養時の光条件としては、光合成リアクターA
およびBでは0.53kW/cm2 で12時間、光合成
リアクターCおよびDでは0.60kW/cm2 で12
時間照射した。その結果、光合成リアクターAおよびB
では1.1リットル(L)/12時間/リアクターおよ
び1.0リットル(L)/12時間/リアクター、光合
成リアクターCおよびDではそれぞれ0.1リットル
(L)/12時間/リアクターの水素が発生した。これ
らの結果を表1に示す。Table 1 shows a schematic diagram showing the light receiving surfaces of the four types of photosynthesis reactors used in the experiment, and the hydrogen generation amount obtained from each photosynthesis reactor. Photosynthesis reactor A
In C, no structure is arranged on the light receiving surface. On the other hand, the photosynthesis reactor B is attached with a black adhesive tape having a thickness of 1 cm, and the photosynthesis reactor D is attached with a metal wire knitted in a mesh shape so as to shield 34% of the light receiving surface. Lactic acid was used as a medium in the photosynthetic reactors A and B, and a 1: 1 mixture of acetic acid and propionic acid was used as a medium in the photosynthetic reactors C and D. In each of the photosynthetic reactors, the light receiving area when the structure (light shielding portion) was not provided was 150 cm 2 . Therefore, the area of the light shielding portion was 51 cm 2 . In these photosynthetic reactors, the photosynthetic bacteria Rhodobacter sp
haeroides RV (Rhodobacter sphaeroides SP-RV, deposit number FERMP-7254) was cultured. The light conditions during the culture are Photosynthesis Reactor A
And 12 hours at 0.53 kW / cm 2 at B, and photosynthetic reactors C and D in 0.60kW / cm 2 12
Irradiated for an hour. As a result, photosynthetic reactors A and B
1.1 liters (L) / 12 hours / reactor and 1.0 liters (L) / 12 hours / reactor, and photosynthesis reactors C and D each produce 0.1 liters (L) / 12 hours / reactor hydrogen did. The results are shown in Table 1.
【0029】表1において、光合成リアクターAとB、
光合成リアクターCとDをそれぞれ比較すると、光合成
リアクターBとDでは構造物を配置し光合成細菌が光を
受ける面積を小さくしたにもかかわらず、構造物を配置
しない場合とほぼ同量の水素を発生することが分かる。
また構造物の形状として、面積の狭いパッチ状でも同様
の効果が期待される。In Table 1, photosynthetic reactors A and B,
Comparing the photosynthetic reactors C and D, respectively, the photosynthetic reactors B and D generate almost the same amount of hydrogen as when the structures are not arranged, although the structures are arranged and the area where the photosynthetic bacteria receive light is reduced. I know what to do.
The same effect can be expected even if the structure has a patch shape having a small area.
【0030】<試験例2>本発明の効果について、実施
例1を用いて検証する。計算には、表1の光合成リアク
タ一AおよびBを用いた実験結果を利用した。<Test Example 2> The effect of the present invention will be verified using Example 1. For the calculation, the experimental results using the photosynthetic reactors A and B in Table 1 were used.
【0031】光合成リアクターAおよびBを用いて水素
生産を行ったとき、光エネルギー変換効率はそれぞれ
1.8%、1.7%であった。なお光エネルギー変換効
率は、When hydrogen was produced using the photosynthetic reactors A and B, the light energy conversion efficiencies were 1.8% and 1.7%, respectively. The light energy conversion efficiency is
【0032】[0032]
【数1】光エネルギー変換効率=[発生した水素の燃焼
エネルギー]÷[照射した光エネルギー]×100
で算出した。## EQU1 ## Light energy conversion efficiency = [combustion energy of generated hydrogen] / [irradiated light energy] × 100.
【0033】つぎに光合成リアクターBについて、実施
例1のように、粘着テープを貼付した部分に変換効率7
%の太陽電池を配置したとする。この時の光エネルギー
変換効率を、Next, in the photosynthetic reactor B, as in Example 1, the conversion efficiency 7 was applied to the portion to which the adhesive tape was attached.
It is assumed that% solar cells are arranged. The light energy conversion efficiency at this time is
【0034】[0034]
【数2】光エネルギー変換効率=〔発生した水素の燃焼
エネルギー+太陽電池が発電した電気エネルギー]÷
[射した光エネルギー]×100
で算出すると、4.0%となる。[Equation 2] Light energy conversion efficiency = [combustion energy of generated hydrogen + electrical energy generated by solar cell] ÷
[Emitted light energy] × 100 gives 4.0%.
【0035】すなわち、従来の光合成リアクターである
Aに比べて、本発明を実施することで光エネルギー変換
効率は約2倍向上する。That is, as compared with A which is a conventional photosynthetic reactor, the light energy conversion efficiency is improved by about 2 times by implementing the present invention.
【0036】[0036]
【表1】 [Table 1]
【0037】[0037]
【発明の効果】本発明は、広い面積が必要とされる光合
成リアクターの受光面を、光エネルギー変換体で覆うと
いう容易な技術で、光エネルギー変換効率が約2倍にな
るといった効果を得ることができる。したがって、光合
成微生物を用いた物質生産の実用化に大きく寄与するも
のである。INDUSTRIAL APPLICABILITY The present invention is an easy technique of covering the light-receiving surface of a photosynthesis reactor, which requires a large area, with a light energy converter, and has the effect of doubling the light energy conversion efficiency. You can Therefore, it greatly contributes to the practical application of the substance production using the photosynthetic microorganism.
【図1】本発明の実施例による光エネルギー変換体組み
込み型光合成リアクターの主要な構成部材の配置関係を
示す模式的斜視図であり、(A)はストライプ状配置、
(B)はパッチ状配置、(C)はメッシュ状配置を示
す。FIG. 1 is a schematic perspective view showing an arrangement relationship of main constituent members of a photosynthetic reactor incorporating a light energy converter according to an embodiment of the present invention, FIG.
(B) shows a patch-like arrangement and (C) shows a mesh-like arrangement.
【図2】光合成細菌の水素生産量を示すグラフであり、
(A)はエネルギー強度との関係を示し、(B)は遮光
率との関係を示す。FIG. 2 is a graph showing the hydrogen production of photosynthetic bacteria,
(A) shows the relationship with the energy intensity, and (B) shows the relationship with the light blocking rate.
【図3】本発明の実施例による光エネルギー変換体組み
込み型光合成リアクターの主要な構成部材の配置関係を
示す模式的斜視図である。FIG. 3 is a schematic perspective view showing an arrangement relationship of main components of a photosynthetic reactor incorporating a light energy converter according to an example of the present invention.
【図4】本発明の実施例により光エネルギー変換体組み
込み型光合成リアクターの主要な構成部材の配置関係を
示す模式的斜視図である。FIG. 4 is a schematic perspective view showing an arrangement relationship of main constituent members of a photosynthetic reactor incorporating a light energy converter according to an embodiment of the present invention.
【図5】本発明の試験例に用いた実験装置の要部の構成
を示す模式図である。FIG. 5 is a schematic diagram showing a configuration of a main part of an experimental apparatus used in a test example of the present invention.
【図6】従来の光合成リアクターを示す模式的斜視図で
ある。FIG. 6 is a schematic perspective view showing a conventional photosynthetic reactor.
1 構造物(培養器) 2 受光面 3 太陽光 10 光合成リアクター 11 受光面 12 光源からの光 13a 太陽電池 14 入口部 15 光熱変換装置 16 集熱用パイプ 20 光源 21 恒温水槽 22 光合成リアクター 23 光合成細菌懸濁液 24 水素ガス 25 水素ガス輸送管 26 ガラスシリンジ 1 structure (incubator) 2 Light receiving surface 3 sunlight 10 Photosynthesis reactor 11 Light receiving surface 12 Light from the light source 13a solar cell 14 Entrance 15 Photothermal conversion device 16 Heat collection pipe 20 light sources 21 Constant Temperature Water Tank 22 Photosynthesis reactor 23 Photosynthetic bacterial suspension 24 Hydrogen gas 25 Hydrogen gas transport pipe 26 glass syringe
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C12R 1:01) H01L 31/04 Q (73)特許権者 000154358 株式会社富士電機総合研究所 神奈川県横須賀市長坂2丁目2番1号 (74)上記1名の代理人 100077481 弁理士 谷 義一 (外2名) (72)発明者 三宅 淳 茨城県つくば市東1丁目1番3 工業技 術院生命工学工業技術研究所内 (72)発明者 浅田 泰男 茨城県つくば市東1丁目1番3 工業技 術院生命工学工業技術研究所内 (72)発明者 木村 正昭 東京都港区西新橋2−8−11 第7東洋 海事ビル8階 財団法人地球環境産業技 術研究機構CO2固定化等プロジェクト 室内 (72)発明者 若山 樹 東京都港区西新橋2−8−11 第7東洋 海事ビル8階 財団法人地球環境産業技 術研究機構CO2固定化等プロジェクト 室内 (72)発明者 中田 栄寿 東京都港区西新橋2−8−11 第7東洋 海事ビル8階 財団法人地球環境産業技 術研究機構CO2固定化等プロジェクト 室内 (56)参考文献 特開 平6−350119(JP,A) 特開 平8−275791(JP,A) (58)調査した分野(Int.Cl.7,DB名) C12M 1/00 - 3/00 C12P 3/00 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI C12R 1:01) H01L 31/04 Q (73) Patent holder 000154358 Fuji Electric Research Institute, Ltd. 2-2 Nagasaka, Yokosuka City, Kanagawa Prefecture No. 1 (74) Attorney for the above 1 person 100077481 Attorney Yoshikazu Tani (2 outside) (72) Inventor Atsushi Miyake 1-3-1, Higashi, Tsukuba, Ibaraki Prefectural Institute of Biotechnology and Industrial Technology (72) ) Inventor Yasuo Asada, 1-3-1, Higashi, Tsukuba-shi, Ibaraki Institute of Industrial Science and Technology, Institute of Biotechnology (72) Masaaki Kimura 2-8-11 Nishishinbashi, Minato-ku, Tokyo 7th Toyo Kaiji Building 8F Foundation Corporation Global Environment Industrial Technology Research Institute CO2 fixation project indoor (72) Inventor Ju Wakayama 2-8-11 Nishi-Shimbashi, Minato-ku, Tokyo 7th Toyo Kaiji Building 8F Property Institute for Global Environmental Industrial Technology CO2 fixation project indoor (72) Inventor Eiju Nakata 2-8-11 Nishi-Shimbashi, Minato-ku, Tokyo 7th Toyo Kaiji Building 8th floor Foundation for Global Environmental Industrial Technology CO2 fixation Chemical conversion project room (56) References JP-A-6-350119 (JP, A) JP-A-8-275791 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) C12M 1 / 00-3/00 C12P 3/00
Claims (2)
ギー変換体を具えた光合成リアクターであって、前記光
エネルギー変換体は前記光合成微生物リアクターの受光
面積の34%を遮光し、前記光エネルギー変換体は集熱
パイプを用いた光熱変換装置であることを特徴とする光
合成リアクター。1. A for cultivating photosynthetic microorganisms, light energy
A photosynthetic reactor equipped with ghee converter, the light
The energy converter receives light from the photosynthetic microbial reactor .
Shields 34% of the area, and the light energy converter collects heat
A photosynthesis reactor characterized by being a photothermal conversion device using a pipe .
する方法において、 前記光合成リアクターの受光面積の34%を、集熱パイ
プを用いた光熱変換装置で遮光し、前記光合成リアクターの受光面に光をあてることによ
り、 光合成微生物を培養して水素を生産させると共に、前記光熱変換装置により光エネルギーを熱エネルギーに
変換させ、 前記生産された水素および熱エネルギーを回収する 、ことを特徴とする 光合成微生物の培養方法。2. A method for culturing a photosynthetic microorganism in a photosynthesis reactor, wherein 34% of the light receiving area of the photosynthesis reactor is a heat collecting pie.
Light is blocked by a photothermal conversion device using a lamp, and light is applied to the light receiving surface of the photosynthetic reactor.
In addition to culturing photosynthetic microorganisms to produce hydrogen , the photothermal conversion device converts light energy into heat energy.
A method for culturing a photosynthetic microorganism , which comprises converting and recovering the produced hydrogen and heat energy .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18157997A JP3463062B2 (en) | 1997-07-07 | 1997-07-07 | Photosynthetic reactor with built-in light energy converter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18157997A JP3463062B2 (en) | 1997-07-07 | 1997-07-07 | Photosynthetic reactor with built-in light energy converter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH1118754A JPH1118754A (en) | 1999-01-26 |
| JP3463062B2 true JP3463062B2 (en) | 2003-11-05 |
Family
ID=16103282
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18157997A Expired - Lifetime JP3463062B2 (en) | 1997-07-07 | 1997-07-07 | Photosynthetic reactor with built-in light energy converter |
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| JP (1) | JP3463062B2 (en) |
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| JP6165523B2 (en) * | 2013-06-28 | 2017-07-19 | 株式会社日本医化器械製作所 | Algae culture lighting device |
| DE102014216606A1 (en) * | 2014-08-21 | 2016-02-25 | LOTBIT Global B.V. | Shading element for solar photobioreactors and solar photobioreactors comprising a shading element |
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- 1997-07-07 JP JP18157997A patent/JP3463062B2/en not_active Expired - Lifetime
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|---|---|
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