JPH091181A - Floating photosynthesis reactor - Google Patents
Floating photosynthesis reactorInfo
- Publication number
- JPH091181A JPH091181A JP15624995A JP15624995A JPH091181A JP H091181 A JPH091181 A JP H091181A JP 15624995 A JP15624995 A JP 15624995A JP 15624995 A JP15624995 A JP 15624995A JP H091181 A JPH091181 A JP H091181A
- Authority
- JP
- Japan
- Prior art keywords
- reactor
- photosynthetic
- roof
- hydrogen
- water
- 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.)
- Granted
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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
- C12M43/00—Combinations of bioreactors or fermenters with other apparatus
- C12M43/06—Photobioreactors combined with devices or plants for gas production different from a bioreactor of fermenter
-
- 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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/38—Caps; Covers; Plugs; Pouring means
-
- 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
- C12M23/56—Floating elements
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Chemical & Material Sciences (AREA)
- Zoology (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Clinical Laboratory Science (AREA)
- Molecular Biology (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、光合成微生物を用いた
光合成リアクターに係り、特にその光合成リアクターを
海などの水面に浮かべた浮遊式光合成リアクター関する
ものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a photosynthetic reactor using photosynthetic microorganisms, and more particularly to a floating photosynthetic reactor in which the photosynthetic reactor is floated on the surface of water such as the sea.
【0002】[0002]
【従来の技術】一般に水素は主として、石油資源の熱分
解などによって製造されているが、この場合多量の化石
燃料を原料やエネルギーとして消費することになり、結
果として多量の二酸化炭素を発生する問題がある。2. Description of the Related Art Generally, hydrogen is mainly produced by thermal decomposition of petroleum resources, but in this case, a large amount of fossil fuel is consumed as a raw material and energy, resulting in a large amount of carbon dioxide. There is.
【0003】このため、近年におけるバイオテクノロジ
ーの急速な進展などを背景として、微生物の機能を活用
し、太陽光をエネルギー源として、効率的に水素を製造
する技術が注目されてきている。[0003] Therefore, against the background of rapid progress of biotechnology in recent years, a technique for efficiently producing hydrogen by utilizing the function of microorganisms and using sunlight as an energy source has been attracting attention.
【0004】自然界には光合成細菌やラン藻類などの水
素発生機能を持った微生物が存在している。これらの微
生物は、石油などの化石燃料を消費することなく、太陽
光をエネルギーとして水や有機物から効率的に水素を発
生する機能を有していると同時に、増殖によって水素発
生機能の自己複製を図ることができる。In the natural world, there are microorganisms having a hydrogen generating function such as photosynthetic bacteria and cyanobacteria. These microorganisms have the function of efficiently generating hydrogen from water and organic substances using sunlight as energy without consuming fossil fuels such as petroleum, and at the same time, they are capable of self-replicating the hydrogen generating function by multiplication. Can be planned.
【0005】従来、微生物を扱うリアクターとしては、
陸上設置型のタンク式リアクターやポンド式回遊リアク
ターなどがあり、使用目的の代表例が、下水処理上の曝
気槽や嫌気性消化槽、オキシデーションディッチ(酸化
池)などであるが、いずれも光を利用したものではな
く、これらの技術を、光合成微生物の増殖に、そのまま
適用することができない。Conventionally, as a reactor for treating microorganisms,
There are tank type reactors and pond type migratory reactors installed on land, and typical examples of the purpose of use are aeration tanks for sewage treatment, anaerobic digestion tanks, oxidation ditch (oxidation pond), etc. However, these techniques cannot be directly applied to the growth of photosynthetic microorganisms.
【0006】[0006]
【発明が解決しようとする課題】この光合成微生物をリ
アクターに収容して光合成で水素を製造しようとする場
合、太陽光が微生物にまんべんなく当たるためには、リ
アクターは、密閉型で、面積が大きく、しかも、底の浅
いものとしなければならない。[Problems to be Solved by the Invention] When the photosynthetic microorganisms are housed in a reactor to produce hydrogen by photosynthesis, in order for the sunlight to be evenly exposed to the microorganisms, the reactor is a closed type and has a large area. Moreover, it must have a shallow bottom.
【0007】しかしながら、密閉型で底の浅いものとし
て太陽光を当てると、リアクター内の温度が異常に上昇
し、微生物の成育に支障をきたすために冷却する必要が
ある。またリアクターには糖分などを含んだ有機性廃水
を供給すると共にリアクター内で十分に撹拌する必要が
あり、このため装置コストが、高くなる問題がある。However, when sunlight is applied as a hermetically sealed type having a shallow bottom, the temperature inside the reactor rises abnormally, and it is necessary to cool it in order to hinder the growth of microorganisms. Further, it is necessary to supply the organic wastewater containing sugar and the like to the reactor and to sufficiently stir the inside of the reactor, which causes a problem that the apparatus cost increases.
【0008】そこで、本発明の目的は、上記課題を解決
し、光合成リアクター内の昇温を抑制し、しかも良好に
撹拌できる浮遊式光合成リアクターを提供することにあ
る。Therefore, an object of the present invention is to solve the above problems and to provide a floating photosynthesis reactor which can suppress the temperature rise in the photosynthesis reactor and can stir well.
【0009】[0009]
【課題を解決するための手段】上記目的を達成するため
に本発明は、太陽光を利用して廃水中の有機物を分解し
て水素を製造する光合成微生物を収容する光合成リアク
ターにおいて、光合成リアクターの屋根部を山形状に形
成し、その屋根部下方が海などの水面に没するようにリ
アクターを浮かべて設けるものである。In order to achieve the above object, the present invention provides a photosynthetic reactor containing a photosynthetic microorganism that decomposes organic substances in wastewater to produce hydrogen by utilizing sunlight. The roof is formed in a mountain shape, and the reactor is floated so that the lower part of the roof is submerged on the surface of water such as the sea.
【0010】[0010]
【作用】上記構成によれば、光合成微生物を収容したリ
アクターを、その山形状の屋根部下方が海などの水面に
半没するように浮かべて設けることで、リアクター内
が、波の作用で適度に撹拌されると共に太陽光を受けて
昇温してもリアクターの屋根部下方より海水などで常時
冷却されているため、過度の温度上昇が抑制され、光合
成微生物が活動できる温度に維持できる。According to the above construction, the reactor containing the photosynthetic microorganisms is floated so that the lower part of the mountain-shaped roof part is submerged in the surface of the water such as the sea. Even if it is stirred and heated by sunlight, it is constantly cooled from below the roof of the reactor with seawater, etc., so that an excessive rise in temperature is suppressed and the temperature at which photosynthetic microorganisms can be maintained can be maintained.
【0011】[0011]
【実施例】以下、本発明の一実施例を添付図面に基づい
て詳述する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below in detail with reference to the accompanying drawings.
【0012】図1において、10は岸壁、11は海(沿
岸、沖合)、湖、池などの水面である。岸壁10には、
栄養補給槽12,沈澱槽13、嫌気性リアクター14、
水素貯蔵タンク15が設けられ、水面11には、光合成
微生物(R−1,S−2,K−2Y,K−6などの菌
株)を増殖させる光合成リアクター16が水面11に半
没するように浮かべて設けられる。In FIG. 1, reference numeral 10 is a quay, and 11 is a water surface such as the sea (coast or offshore), lake or pond. On the quay 10,
Nutrient supply tank 12, precipitation tank 13, anaerobic reactor 14,
A hydrogen storage tank 15 is provided, and on the water surface 11, a photosynthesis reactor 16 for growing photosynthetic microorganisms (strains such as R-1, S-2, K-2Y, and K-6) is semi-submerged on the water surface 11. It is provided by floating.
【0013】嫌気性リアクター14には、そのリアクタ
ー14内に糖などの有機性廃水を供給する廃水ライン1
7が接続され、嫌気性リアクター14の廃水口と光合成
リアクター16の入口16aとが処理水入口ライン18
で接続される。光合成リアクター16の出口16bと沈
澱槽13とが処理水出口ライン19で接続され、沈澱槽
13の上澄液が最終処理水ライン20で海中に排出され
るようになっている。The anaerobic reactor 14 has a wastewater line 1 for supplying organic wastewater such as sugar into the reactor 14.
7 is connected, and the wastewater outlet of the anaerobic reactor 14 and the inlet 16a of the photosynthesis reactor 16 are treated water inlet lines 18
Connected by The outlet 16b of the photosynthetic reactor 16 and the precipitation tank 13 are connected by a treated water outlet line 19, and the supernatant of the precipitation tank 13 is discharged into the sea by a final treated water line 20.
【0014】また光合成リアクター16の屋根部下方2
1の頂部21aにはフレキシブル配管からなる水素配管
22が接続され、製造された水素を水素貯蔵タンク15
に供給して貯蔵するようになっている。また嫌気性リア
クター14の頂部と水素貯蔵タンク15とが水素配管2
3で接続され、嫌気性リアクター14においても生じた
水素を水素貯蔵タンク15に貯蔵できるようになってい
る。The lower part 2 of the roof of the photosynthesis reactor 16
A hydrogen pipe 22 composed of a flexible pipe is connected to the top portion 21a of No. 1 and the produced hydrogen is stored in the hydrogen storage tank 15
It is designed to be supplied to and stored in. Further, the top of the anaerobic reactor 14 and the hydrogen storage tank 15 are connected to the hydrogen pipe 2.
3 is connected, and hydrogen generated in the anaerobic reactor 14 can be stored in the hydrogen storage tank 15.
【0015】栄養補給槽12と光合成リアクター15と
は養分供給ライン24で接続され、夜間などに栄養補給
槽12から窒素源などの栄養分が光合成リアクター16
に供給できるようになっている。The nutrient supply tank 12 and the photosynthetic reactor 15 are connected by a nutrient supply line 24, and the nutrient such as a nitrogen source is supplied from the nutrient supply tank 12 to the photosynthesis reactor 16 at night.
Can be supplied.
【0016】光合成リアクター16は、例えば、図2に
示すように、入口16aから出口16bに至る流路25
が複数に折り返されるように形成されると共にその各流
路25上の空間は、流路25ごとに独立した室を形成す
るように区画されて形成され、各室ごとに山形状に屋根
部下方21が形成されると共にその各頂部21aに水素
配管22(図1)が接続される。The photosynthesis reactor 16 is, for example, as shown in FIG. 2, a flow path 25 extending from an inlet 16a to an outlet 16b.
Are formed so as to be folded back into a plurality of parts, and the space on each flow path 25 is partitioned so as to form an independent chamber for each flow path 25, and each room has a mountain-like shape below the roof portion. 21 is formed, and a hydrogen pipe 22 (FIG. 1) is connected to each top 21a thereof.
【0017】図3に示すように、光合成リアクター16
の屋根部下方21は、流路25ごとに形成され、それぞ
れ屋根部下方21が、頂部21aを除いて水面11に没
するように設けられると共にリアクター16の屋根部下
方21を通して太陽光が差し込むようにされる。この屋
根部下方21は、南向きになるように、また屋根部下方
21が頂部21aを除いて水面11に没するようにその
浮力が調整されると共に係留索26で固定される。なお
リアクター16は、太陽の動きに合せて回転或いは移動
するように設けてもよい。As shown in FIG. 3, the photosynthetic reactor 16
The lower part 21 of the roof is formed for each flow path 25. The lower part 21 of the roof is provided so as to be submerged in the water surface 11 except for the top part 21a, and the sunlight is inserted through the lower part 21 of the reactor 16. To be The buoyancy of the lower roof portion 21 is adjusted so that the lower roof portion 21 faces south, and the lower roof portion 21 is submerged on the water surface 11 except for the top portion 21a, and is fixed by mooring ropes 26. The reactor 16 may be provided so as to rotate or move according to the movement of the sun.
【0018】屋根部下方21は、透明な合成樹脂板など
で形成するが、この際、微生物の光合成に寄与しない赤
外線領域の波長をカットする熱遮蔽板を積層しておくと
よい。The lower portion 21 of the roof portion is formed of a transparent synthetic resin plate or the like. At this time, it is preferable to stack a heat shield plate for cutting wavelengths in the infrared region that do not contribute to photosynthesis of microorganisms.
【0019】またリアクター16は、上下2室に形成
し、下部を嫌気性リアクター室とし、上部を光合成リア
クター室とすることも可能である。It is also possible to form the reactor 16 in two chambers, an upper chamber and a lower chamber, which are anaerobic reactor chambers and an upper chamber is a photosynthetic reactor chamber, respectively.
【0020】次に実施例の作用を述べる。Next, the operation of the embodiment will be described.
【0021】廃水ライン17から有機性廃水として、例
えばグルコースを10,000ppm含む廃液を嫌気性
リアクター14に供給し、嫌気性リアクター14内で、
嫌気性処理がなされて、酪酸塩800ppm,酢酸塩8
00ppm,プロピオン酸塩800ppmに分解され、
処理ライン18より、光合成リアクター16内に供給さ
れる。A waste liquid containing 10,000 ppm of glucose, for example, as an organic waste water is supplied from the waste water line 17 to the anaerobic reactor 14, and in the anaerobic reactor 14,
Anaerobic treatment, butyrate 800ppm, acetate 8
Decomposed to 00ppm, 800ppm propionate,
It is supplied from the processing line 18 into the photosynthesis reactor 16.
【0022】光合成リアクター16は、供給された廃水
が流路25に沿って流れる間に、光合成微生物が太陽光
をエネルギとして有機物を分解すると共に光合成反応に
より水素を発生する。発生した水素は、水素配管22よ
り水素貯蔵タンク15に貯蔵される。In the photosynthesis reactor 16, while the supplied wastewater flows along the flow path 25, photosynthetic microorganisms decompose organic matters by using sunlight as energy and generate hydrogen by the photosynthesis reaction. The generated hydrogen is stored in the hydrogen storage tank 15 through the hydrogen pipe 22.
【0023】リアクター16から排水された廃水は、処
理水出口ライン19より沈澱槽13に供給され、その上
澄液が最終処理水ライン20で海中に排出されるように
なっている。The waste water discharged from the reactor 16 is supplied to the settling tank 13 through the treated water outlet line 19, and the supernatant thereof is discharged into the sea through the final treated water line 20.
【0024】この光合成リアクター16は、水面11に
浮かべて設けられ、波で常時揺動するため、リアクター
16内の廃水の撹拌が良好となり、またリアクター16
は太陽光にて昇温しようとするが、屋根部下方21が一
部水面11に没しているため、屋根部下方21より冷却
され、過度に温度上昇することが防止される。すなわ
ち、屋根部下方21間には、常時海水が通り、波などで
屋根部下方21が濡らされており、昇温しようとしても
屋根部下方21の水の蒸発潜熱及び周囲海水により冷却
されるため、昇温することがない。The photosynthetic reactor 16 is provided so as to float on the water surface 11 and constantly oscillates by waves, so that the waste water in the reactor 16 can be well stirred and the reactor 16 can be agitated.
Tries to raise the temperature by sunlight, but since the lower part 21 of the roof is partly immersed in the water surface 11, it is cooled from the lower part 21 of the roof, and an excessive rise in temperature is prevented. That is, seawater always passes between the lower roof portions 21, and the lower roof portion 21 is wetted by waves or the like, and even if an attempt is made to raise the temperature, it is cooled by the latent heat of evaporation of water in the lower roof portion 21 and the surrounding seawater. There is no temperature rise.
【0025】この光合成リアクター16は、例えば横幅
50m,長さ125m、廃水深さ0.16mで、1日当
たりの廃水処理量を100m3 とすると、1000〜2
000m3 /日の水素を製造することができる。The photosynthetic reactor 16 has a width of 50 m, a length of 125 m, a wastewater depth of 0.16 m, and a wastewater treatment amount of 100 m 3 per day is 1000-2.
It is possible to produce 000 m 3 / day of hydrogen.
【0026】また太陽光が800kcal/m2 ・hの
エネルギで、リアクター16に入射するとしてもリアク
ター16内の1,000m3 ,30℃の水が日中10時
間温められても水温は45℃以上には上昇せず、光合成
微生物の成育に支障をきたさない。Even if the sunlight is incident on the reactor 16 with the energy of 800 kcal / m 2 · h, the water temperature of 45 ° C. is maintained even if the water of 1,000 m 3 at 30 ° C. in the reactor 16 is heated for 10 hours during the day. It does not rise above the above level and does not hinder the growth of photosynthetic microorganisms.
【0027】[0027]
【発明の効果】以上要するに本発明によれば、光合成微
生物を収容したリアクターを水面に浮かべて設けること
で、リアクター内が、波で適度に撹拌されると共に太陽
光を受けて昇温してもリアクターの外周が海水で常時冷
却されているため、過度の温度上昇が抑制され、光合成
微生物が活動できる温度に維持できる。In summary, according to the present invention, the reactor containing the photosynthetic microorganisms is floated on the water surface, so that the inside of the reactor is moderately stirred by the waves and is heated by the sunlight. Since the outer periphery of the reactor is constantly cooled with seawater, excessive temperature rise is suppressed and the temperature can be maintained at a level at which photosynthetic microorganisms can act.
【図1】本発明の一実施例を示す概略斜視図である。FIG. 1 is a schematic perspective view showing one embodiment of the present invention.
【図2】図1の光合成リアクターの流路を示す平断面図
である。FIG. 2 is a plan sectional view showing a flow path of the photosynthesis reactor of FIG.
【図3】図2の光合成リアクターの断面図である。3 is a cross-sectional view of the photosynthetic reactor of FIG.
11 水面 15 水素貯蔵タンク 16 光合成リアクター 18 処理水入口ライン 21 屋根部下方 11 Water Surface 15 Hydrogen Storage Tank 16 Photosynthesis Reactor 18 Treated Water Inlet Line 21 Below Roof
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 //(C12P 3/00 C12R 1:01) (C12P 3/00 C12R 1:89) (72)発明者 内山 茂 東京都港区西新橋2丁目8番11号 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 福永 栄 東京都港区西新橋2丁目8番11号 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 泉 雅之 東京都港区西新橋2丁目8番11号 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─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display part // (C12P 3/00 C12R 1:01) (C12P 3/00 C12R 1:89) (72) Inventor Shigeru Uchiyama 2-8-11 Nishi-shinbashi, Minato-ku, Tokyo Foundation Lawyer Institute for Global Environmental Industrial Technology CO2 fixation etc. Project room (72) Inventor Sakae Fukunaga 2-8-11 Nishi-shinbashi, Minato-ku, Tokyo Institute for Global Environment and Industrial Technology CO2 Immobilization Project Room (72) Inventor Masayuki Izumi 2-8-11 Nishishinbashi, Minato-ku, Tokyo Foundation Office National Institute for Global Environmental Technology Research CO2 Immobilization Project Room
Claims (1)
して水素を製造する光合成微生物を収容する光合成リア
クターにおいて、光合成リアクターの屋根部を山形状に
形成し、その屋根部の下方が海などの水面に没するよう
にリアクターを浮かべて設けることを特徴とする浮遊式
光合成リアクター。1. A photosynthetic reactor containing photosynthetic microorganisms that decomposes organic matter in wastewater using sunlight to produce hydrogen. The roof of the photosynthetic reactor is formed in a mountain shape, and the lower part of the roof is A floating photosynthetic reactor characterized in that the reactor is floated so as to be submerged in the water such as the sea.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15624995A JP3253235B2 (en) | 1995-06-22 | 1995-06-22 | Floating photosynthetic reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15624995A JP3253235B2 (en) | 1995-06-22 | 1995-06-22 | Floating photosynthetic reactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH091181A true JPH091181A (en) | 1997-01-07 |
| JP3253235B2 JP3253235B2 (en) | 2002-02-04 |
Family
ID=15623653
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15624995A Expired - Fee Related JP3253235B2 (en) | 1995-06-22 | 1995-06-22 | Floating photosynthetic reactor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3253235B2 (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002276387A (en) * | 2001-03-15 | 2002-09-25 | Mitsui Eng & Shipbuild Co Ltd | Biomass power generation system and biomass power generation method using the same |
| JP2006095394A (en) * | 2004-09-29 | 2006-04-13 | Akio Asahi | Method for purifying drinking water |
| JP2006217829A (en) * | 2005-02-08 | 2006-08-24 | Research Institute Of Innovative Technology For The Earth | Hydrogen production apparatus using microorganisms and fuel cell system using the same |
| WO2008153202A1 (en) * | 2007-06-14 | 2008-12-18 | Waseda University | Method of culturing photosynthetic microorganism using photosynthetic reactor allowed to float on water surface and photosynthetic reactor for producing hydrogen gas by photosynthetic microorganism |
| DE102008022676A1 (en) * | 2008-05-07 | 2009-11-12 | Phyton Energy Gmbh | Device for increasing carbon and/or oil containing microorganisms in nutrient fluid, comprises a self-supporting, vertically passing nutrient fluid chamber formed by line adhering connection of two foils |
| JP2010514446A (en) * | 2006-12-28 | 2010-05-06 | ソリックス バイオフューエルズ, インコーポレイテッド | Excellent diffused light large surface area water-supported photobioreactor |
| JP2011050902A (en) * | 2009-09-03 | 2011-03-17 | Toshiba Corp | Sewage water treatment system |
| JP2011152071A (en) * | 2010-01-27 | 2011-08-11 | Japan Research Institute Ltd | Microorganism culture apparatus |
| JP2011251286A (en) * | 2005-03-03 | 2011-12-15 | National Institute Of Advanced Industrial Science & Technology | Water treated by reducing concentration of nutrient salt in salt water and method for producing the same |
| KR101138762B1 (en) * | 2009-11-05 | 2012-04-25 | 삼성중공업 주식회사 | Hydrogen generating apparatus in a ship |
| JP2012510292A (en) * | 2008-12-03 | 2012-05-10 | インハ−インダストリー パートナーシップ インスティテュート | Photobioreactor for mass culture of marine microalgae using semipermeable membrane |
| JP2013119073A (en) * | 2011-12-08 | 2013-06-17 | Toshiba Corp | Water treatment apparatus |
| CN110145687A (en) * | 2019-05-05 | 2019-08-20 | 中广核研究院有限公司 | A Hydrogen Supply System for Offshore Small Reactors |
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| FR3075822B1 (en) * | 2017-12-27 | 2025-03-14 | Emmanuel Poirmeur | METHOD FOR TRANSFORMING AN ORGANIC SUBSTRATE IN IMMERSION |
-
1995
- 1995-06-22 JP JP15624995A patent/JP3253235B2/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002276387A (en) * | 2001-03-15 | 2002-09-25 | Mitsui Eng & Shipbuild Co Ltd | Biomass power generation system and biomass power generation method using the same |
| JP2006095394A (en) * | 2004-09-29 | 2006-04-13 | Akio Asahi | Method for purifying drinking water |
| JP2006217829A (en) * | 2005-02-08 | 2006-08-24 | Research Institute Of Innovative Technology For The Earth | Hydrogen production apparatus using microorganisms and fuel cell system using the same |
| JP2011251286A (en) * | 2005-03-03 | 2011-12-15 | National Institute Of Advanced Industrial Science & Technology | Water treated by reducing concentration of nutrient salt in salt water and method for producing the same |
| JP2010514446A (en) * | 2006-12-28 | 2010-05-06 | ソリックス バイオフューエルズ, インコーポレイテッド | Excellent diffused light large surface area water-supported photobioreactor |
| WO2008153202A1 (en) * | 2007-06-14 | 2008-12-18 | Waseda University | Method of culturing photosynthetic microorganism using photosynthetic reactor allowed to float on water surface and photosynthetic reactor for producing hydrogen gas by photosynthetic microorganism |
| DE102008022676A1 (en) * | 2008-05-07 | 2009-11-12 | Phyton Energy Gmbh | Device for increasing carbon and/or oil containing microorganisms in nutrient fluid, comprises a self-supporting, vertically passing nutrient fluid chamber formed by line adhering connection of two foils |
| JP2012510292A (en) * | 2008-12-03 | 2012-05-10 | インハ−インダストリー パートナーシップ インスティテュート | Photobioreactor for mass culture of marine microalgae using semipermeable membrane |
| US9181520B2 (en) | 2008-12-03 | 2015-11-10 | Inha-Industry Partnership Institute | Photobioreactor for mass-culturing marine microalgae using semi-permeable membrane |
| JP2011050902A (en) * | 2009-09-03 | 2011-03-17 | Toshiba Corp | Sewage water treatment system |
| KR101138762B1 (en) * | 2009-11-05 | 2012-04-25 | 삼성중공업 주식회사 | Hydrogen generating apparatus in a ship |
| JP2011152071A (en) * | 2010-01-27 | 2011-08-11 | Japan Research Institute Ltd | Microorganism culture apparatus |
| JP2013119073A (en) * | 2011-12-08 | 2013-06-17 | Toshiba Corp | Water treatment apparatus |
| CN110145687A (en) * | 2019-05-05 | 2019-08-20 | 中广核研究院有限公司 | A Hydrogen Supply System for Offshore Small Reactors |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3253235B2 (en) | 2002-02-04 |
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