JPS60126075A - Oxygen-producing bioreactor device - Google Patents
Oxygen-producing bioreactor deviceInfo
- Publication number
- JPS60126075A JPS60126075A JP23244883A JP23244883A JPS60126075A JP S60126075 A JPS60126075 A JP S60126075A JP 23244883 A JP23244883 A JP 23244883A JP 23244883 A JP23244883 A JP 23244883A JP S60126075 A JPS60126075 A JP S60126075A
- Authority
- JP
- Japan
- Prior art keywords
- oxygen
- culture
- photosynthesis
- photosynthetic
- container
- 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.)
- Pending
Links
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 56
- 239000001301 oxygen Substances 0.000 title claims abstract description 54
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 54
- 230000000243 photosynthetic effect Effects 0.000 claims abstract description 34
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 33
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 16
- 230000029553 photosynthesis Effects 0.000 claims abstract description 15
- 238000010672 photosynthesis Methods 0.000 claims abstract description 15
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 14
- 239000007789 gas Substances 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 241000195649 Chlorella <Chlorellales> Species 0.000 claims abstract description 7
- 239000013307 optical fiber Substances 0.000 claims abstract description 6
- 239000012528 membrane Substances 0.000 claims abstract description 5
- 238000000926 separation method Methods 0.000 claims abstract description 5
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 241000195628 Chlorophyta Species 0.000 claims description 4
- 239000000284 extract Substances 0.000 claims description 3
- 241000233855 Orchidaceae Species 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 12
- 238000003756 stirring Methods 0.000 abstract description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 abstract description 2
- 229910001882 dioxygen Inorganic materials 0.000 abstract description 2
- 238000000034 method Methods 0.000 abstract 1
- 239000011368 organic material Substances 0.000 abstract 1
- 238000006303 photolysis reaction Methods 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 description 8
- 229910052739 hydrogen Inorganic materials 0.000 description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 6
- 238000010586 diagram Methods 0.000 description 6
- 239000001963 growth medium Substances 0.000 description 5
- 238000005868 electrolysis reaction Methods 0.000 description 3
- 241000192700 Cyanobacteria Species 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 235000016425 Arthrospira platensis Nutrition 0.000 description 1
- 240000002900 Arthrospira platensis Species 0.000 description 1
- 241000192685 Calothrix Species 0.000 description 1
- 241001611009 Chamaesiphon Species 0.000 description 1
- 241000195585 Chlamydomonas Species 0.000 description 1
- 241000086006 Chlorochytrium Species 0.000 description 1
- 241001478240 Coccus Species 0.000 description 1
- 241000565779 Cylindrospermum Species 0.000 description 1
- 241001035792 Dictyosphaerium Species 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 241001464427 Gloeocapsa Species 0.000 description 1
- 241000761673 Gomphosphaeria Species 0.000 description 1
- 241000989913 Gunnera petaloidea Species 0.000 description 1
- 241001167739 Lagerheimia Species 0.000 description 1
- 241000658218 Lobella Species 0.000 description 1
- 241001134698 Lyngbya Species 0.000 description 1
- 241000192701 Microcystis Species 0.000 description 1
- 241000192656 Nostoc Species 0.000 description 1
- 241000192497 Oscillatoria Species 0.000 description 1
- 241000196152 Pediastrum Species 0.000 description 1
- 241000180182 Protosiphon Species 0.000 description 1
- 241001575211 Rivularia <snail> Species 0.000 description 1
- 241000195663 Scenedesmus Species 0.000 description 1
- 241000243446 Stigonema Species 0.000 description 1
- 241001439057 Syneches Species 0.000 description 1
- 241000192707 Synechococcus Species 0.000 description 1
- 241001078392 Tetrapedia Species 0.000 description 1
- 241000157473 Tolypothrix Species 0.000 description 1
- 241000736687 Trebouxia Species 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 210000003763 chloroplast Anatomy 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- -1 hydroxide ions Chemical class 0.000 description 1
- 239000002609 medium Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 229940082787 spirulina Drugs 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
-
- 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
- C12M23/24—Gas permeable parts
-
- 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
- C12M31/08—Means for providing, directing, scattering or concentrating light by conducting or reflecting elements located inside the reactor or in its structure
Landscapes
- 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)
- Biochemistry (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Molecular Biology (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Clinical Laboratory Science (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は元エネルギーを利用し光合底生vlJを用い
て2例えは人間の生命維持に必要な酸素を生産する酸素
生産バイオリアクタ装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an oxygen production bioreactor device that utilizes source energy to produce oxygen necessary for supporting human life, for example, by using photopolybenthos VlJ.
従来1酸素発生装置として第1図の構成図に示す水の電
気分解を利用したものがめった。図において+1)は陽
極、(2)は陰極、(3)は電解液を言む水。Conventionally, there have been few oxygen generators that utilize water electrolysis as shown in the block diagram of FIG. In the figure, +1) is the anode, (2) is the cathode, and (3) is water, which is the electrolyte.
(蜀は水の電気分解にょ多発生した酸素、(5)は同じ
く水素、(6)は直流電源、(7)、(8)は発生した
酸素及び水素を各々収容する酸素タンク(9)及び水素
タンクαQに送り込むポンプ、(Iυは補充用の水を収
容する水タンク、Q諺は補充用の′4解液を収容する′
1屏液タンクである。(Shu is oxygen generated by electrolysis of water, (5) is also hydrogen, (6) is a DC power source, (7) and (8) are oxygen tanks (9) that contain the generated oxygen and hydrogen, respectively, A pump that sends water to the hydrogen tank αQ, (Iυ is a water tank that stores water for replenishment, and Q proverbs contain '4 solution for replenishment.'
1 folding liquid tank.
次に動作について説明する。直流電源(6)よりIU流
電圧が電極tll、 +21間に印加されると、水の電
気分解により1場極(1)から酸素、陰極(2)よυ水
素が発生する。次いで気室に蓄積された酸素(4)及び
水素(5)をポンプ(力、(8)で各々酸素タンク(9
)、水素タンク61に送シ込む。Next, the operation will be explained. When an IU current voltage is applied between the electrodes tll and +21 from the DC power source (6), oxygen is generated from the first field electrode (1) and υ hydrogen is generated from the cathode (2) due to water electrolysis. Next, the oxygen (4) and hydrogen (5) accumulated in the air chamber are pumped (8) into oxygen tanks (9).
) and pumped into the hydrogen tank 61.
従来の装置は2以上のように構成されているので、酸素
を発生させるには直流電源から電力を供給し続けねけな
らず、14L刀消費が犬きく、有人宇宙基地や海中基地
のように外部からのエネルギーの補給が困難な閉鎖空間
で用いるには問題があった。Conventional devices are configured with two or more units, so in order to generate oxygen, power must be continuously supplied from a DC power source, which consumes 14L, and is not suitable for use in manned space bases or underwater bases. There was a problem in using it in a closed space where it was difficult to supply energy from the outside.
この発明は上記のような従来のものの欠点を除去するた
めになされたもので、培養液とともに光合成生物を収容
した培養容器、この培養容器に炭酸ガスを供給する炭酸
ガス源と光音導入する光ファイバ、上記光合底生生物が
光合成により生成した酸素を上記培養容器から導出して
収容する酸素容器を備えた酸素生産バイオリアクタ装置
にすることにより、省電力、省エネルギーを目的とする
ものである。This invention was made in order to eliminate the drawbacks of the conventional ones as described above, and it consists of a culture vessel containing a photosynthetic organism along with a culture solution, a carbon dioxide gas source that supplies carbon dioxide gas to the culture vessel, and a light that introduces light and sound. The purpose of the present invention is to save power and energy by providing an oxygen production bioreactor device equipped with fibers and an oxygen container that extracts and stores oxygen generated by the photosynthetic benthic organisms from the culture container, thereby saving power and energy.
以下、この発明の一実施例を図について説明する。第2
図において、Qυは培養容器、Qシは培養容器Qυに収
容された光合成生物を混入した培養液。An embodiment of the present invention will be described below with reference to the drawings. Second
In the figure, Qυ is a culture container, and Qshi is a culture solution mixed with photosynthetic organisms housed in the culture container Qυ.
(ハ)は外部より集光した太陽光あるいは人工光全培賢
容器Qv中に専き、培養液(2)中の光合成生物に供給
する元ファイバ、 &41は回転することにより培養液
襲4中の光合成生物を分散させる撹拌ンロベラ。(c) is a source fiber that is used to supply sunlight or artificial light from the outside to the culture medium (2), and is supplied to the photosynthetic organisms in the culture medium (2); Stirring lobella to disperse photosynthetic organisms.
(ハ)はクロベラG20全回転させるモータ、(ハ)は
光合成を促進させる温度コントローラ、罰は培養容器Q
υに炭酸ガスを供給する炭酸ガス源、この場合は炭酸ガ
スホンベ、(ハ)は酸素を培養液@と分離する気液分離
膜、 C71は光合成生物の光合成によシ発生した培養
容器Qυ円の酸素を収容する酸素容器、この場合は酸素
タンク、(至)は上記酸素を酸素タンクl/Jに送気す
るポンプ、C1υは補充用の光合成生物を収容する光合
成生物タンク、O3は補充用の培養液を収容する培地タ
ンク、(ハ)は廃液タンク、 C(訃、ぐっ。(c) is the motor that rotates the Blackbella G20 fully, (c) is the temperature controller that promotes photosynthesis, and the punishment is the culture container Q
A carbon dioxide gas source that supplies carbon dioxide to υ, in this case a carbon dioxide gas cylinder, (c) is a gas-liquid separation membrane that separates oxygen from the culture solution @, and C71 is a culture vessel Qυ generated by photosynthesis of photosynthetic organisms. An oxygen container that stores oxygen, in this case an oxygen tank, (to) a pump that delivers the above oxygen to the oxygen tank l/J, C1υ is a photosynthetic organism tank that stores photosynthetic organisms for replenishment, and O3 is an oxygen tank for replenishment. A culture medium tank that stores the culture solution, (C) is a waste liquid tank, and C (grrrr).
価)はポンプである。price) is a pump.
次にこの発明の動作について説明する。培養液(ハ)中
の光合成生物(例えばクロレラ)は光ファイバにより供
給された光のエネルギーにより炭酸を同化して有機物を
合成する光合成を行なう。この過穆で炭酸を還元して酸
素分子を発生するのであるが2水が光分解されて水酸イ
オンから電子が奪われることにより酸素ガスが発生する
。温度コントローラ弼は光合成生物の生育及び光合成に
適した温度に培養容器の温度をコントロールし、又は攪
拌プロペラ@は培養液(ハ)中の光合成生物を分散させ
、ともに光合成の促進を図るものである。さらに気液分
離膜(イ)は酸素タンク側、酸素汲み出し口側に設は無
重力状態においても使用できる様に酸素を培養液のから
分離するものである。Next, the operation of this invention will be explained. Photosynthetic organisms (for example, chlorella) in the culture solution (c) perform photosynthesis in which they assimilate carbon dioxide and synthesize organic matter using the energy of light supplied by the optical fiber. This supernatant reduces carbonic acid and generates oxygen molecules, but 2 water is photolyzed and electrons are taken away from hydroxide ions, thereby generating oxygen gas. The temperature controller (2) controls the temperature of the culture container to a temperature suitable for the growth and photosynthesis of photosynthetic organisms, and the stirring propeller (2) disperses the photosynthetic organisms in the culture solution (c), both of which promote photosynthesis. . Further, a gas-liquid separation membrane (a) is installed on the oxygen tank side and the oxygen outlet side to separate oxygen from the culture solution so that it can be used even in zero gravity conditions.
光合成生物としては緑藻やラン藻が用いられる。Green algae and cyanobacteria are used as photosynthetic organisms.
緑藻としては例えばクロレラ(Chlorella)
、クラミドモナX (Ohlam7dOmOnae )
、 ハイドロディクション(Hydrodictyo
n) 、りuoxファエラ(Ohloroephaer
a) 、クロロコツカス(Cb、1 o r o −c
occum)、カラ7ウム(Onaracium) 、
クロロントリウム(Ohlorochytrium)
、トvホ*7”(Trebouxia) 、ベディアス
トラA (Pediast−rum) 、オオシステイ
x (OOcystie) 、 =+ダテラ(Chod
atella)、ネフロシテイウム(Nephrocy
−tium) 、 ボトリオコツカス(Botryoc
occus)。Examples of green algae include Chlorella
, Chlamydomona X (Ohlam7dOmOnae)
, Hydrodiction
n), Ohloroephaer
a) Chlorococcus (Cb, 1 o r o -c
occum), Onaracium,
Chlorochytrium
, Trebouxia, Pediast-rum, OOcystie, Chod
atella), Nephrocyteium
-tium), Botryoccus
occurrence).
セレナストラム(eelθnastrum)、セネデス
ムス(Scenedesmus) 、デイクチオスファ
エリウム(Dictyosphaerium) 、 プ
ロトンフォア (Proto−siphon) などで
ある。ラン藻としては1例えばクロロコツカス(Ohr
oococcus)、シネコアステイス(Synech
OcystiB)、シネココツカス(Sy−necho
coccus) 、テトラベディア(Tetraped
ia) 。These include eelθnastrum, Scenedesmus, Dictyosphaerium, Proto-siphon, and the like. Examples of blue-green algae include Chlorococcus (Ohr).
oococcus), Synechosteis (Synech)
OcystiB), Synechococcus (Sy-necho
coccus), Tetrapedia (Tetraped)
ia).
ミクロシステイス(Microcystis) 、アフ
ァノカズサ(A、phanocapsa) 、メリスモ
ベディア(Maris−n+opedia) 、 ニー
カッシス(Eucapsiθ)、グロエオカプサ(Gl
oeocapea )、フイロデルマ(Phy−110
dlrlna)、ブローロカブサ(Pleurocap
sa)。Microcystis, A, phanocapsa, Maris-n+opedia, Eucapsiθ, Gloeocapsa
oeocapea), Phyloderma (Phy-110)
dlrlna), Pleurocap
sa).
オンコビルサ(oncobyre?) 、キセノコツカ
ス(Xenoccocus) 、ゴンフオスファエリア
(GOm−phosphaeria) 、デルモカルパ
(Dernnocarpa) 。Oncobyre?, Xenoccocus, GOm-phosphaeria, Dernnocarpa.
カマエ/フオン(Chamaesiphon) 、オシ
ラドリア(OscillatOria) 、スピルリナ
(Spiulina) 。Chamaesiphon, OscillatOria, Spirulina.
リングビヤ(Lyngbya)、フォルミゾイウム(P
horn+id1um) 、アナベナ(Anabaen
a) 、ノストック(Nostoc) 、シリンドロス
ベルマム(Cylindrospermum) 、リブ
ラリア(Rivularia) 。Lyngbya, Formizoium (P
horn+id1um), Anabaen
a), Nostoc, Cylindrospermum, Rivularia.
カロセリクス(Calothrix) 、 シトネマ(
ScytO−nama)、)リボスリクス(Tolyp
othrix) ステイゴネマ(S ti、gonem
a) 、 ハハo 77 オフ(11apaloB1p
hon) 、 マスディゴクラダX(mae−tigo
cl:adus) 、ブラフトリシア(Brachyt
ri−chia ) などである。特にクロレラは入手
しゃすく、二次的に食物としても利用できるので適当で
ある。Calothrix, Sitnema (
ScytO-nama),) Ribothrix (Tolyp
othrix) Stigonema (Sti, gonem)
a), haha o 77 off (11apaloB1p
hon), Mae-tigo
cl:adus), Brachyt
ri-chia) etc. Chlorella is particularly suitable because it is readily available and can be used as a secondary food.
第3図は光合成生物の光合成による酸素発生速度の経時
変化を示す特性図で、縦軸は酸素発生量。Figure 3 is a characteristic diagram showing changes over time in the rate of oxygen production by photosynthesis of photosynthetic organisms, where the vertical axis is the amount of oxygen production.
横軸は経時時間を表わしている。クロレラ及び数抽の緑
藻類を収容した5otの培養容器を用い。The horizontal axis represents elapsed time. A 5 ot culture container containing chlorella and several extracts of green algae was used.
光強[を1万ルツクスとし成育温度25℃の条件で行っ
たもので、平均的30 mt /min の発生速度で
酸素が得られた。又図から時間とともに漸次酸素発生量
は低下していくことが判る。これは培養液の老化、光合
成生物の死滅によるものと考えられるので、常にコンス
タントに一定量の酸素を得るためには新しい培養液、光
合成生物の補充。The growth was carried out at a light intensity of 10,000 lux and a growth temperature of 25° C., and oxygen was obtained at an average generation rate of 30 mt/min. The figure also shows that the amount of oxygen generated gradually decreases with time. This is thought to be due to aging of the culture medium and death of photosynthetic organisms, so in order to constantly obtain a constant amount of oxygen, new culture medium and photosynthetic organisms must be replenished.
あるいは交換が必要とされる。この条件の光強度1万ル
ツクスは酸素発生量の飽和手前で最も効率のよいもので
、同じく生育温度もクロレラ等の生育及び光合成を促進
するに適した温度である。又。Or replacement is required. The light intensity of 10,000 lux under these conditions is the most efficient before the amount of oxygen generation reaches saturation, and the growth temperature is also suitable for promoting the growth and photosynthesis of chlorella and the like. or.
例えばマスティゴグラダスの生育に適した温度は50℃
である。For example, the optimum temperature for growing mastigogradus is 50°C.
It is.
なお、上記実施例では光合成生物を培養液中で生育させ
たまま使用したが、微生物の菌体や微生物から抽出した
葉緑体をポリアクリルアミドなどのゲルに固定化したも
のを用いてもよい。In the above examples, photosynthetic organisms were used as they were grown in the culture solution, but cells of microorganisms or chloroplasts extracted from microorganisms may be immobilized in a gel such as polyacrylamide.
この発明の酸素生産バイオリアクタ装置は光合成生物の
光合成を利用し電力を用いずに光エネルギーを用いて酸
素を発生させるので、大きな電力量を必要としないため
、有人宇宙基地や海中基地などエネルギーの補給が困難
な場所で用いるのに適している。The oxygen production bioreactor device of this invention utilizes the photosynthesis of photosynthetic organisms to generate oxygen using light energy without using electricity, so it does not require a large amount of electricity, so it can be used as an energy source for manned space bases and underwater bases. Suitable for use in places where replenishment is difficult.
以上のように、この発明によれば培養液とともに光合成
生物を収容した培養容器、この培養容器に炭酸ガスを供
給する炭酸ガス源と光を導入する光ファイバ、上記光合
成生物が光合成にょ9生成しfc酸素を上記培養容器か
ら導出して収容する酸素容器を備えたものにすることに
ょ92元エネルギーを用いて光合成を行い敵索を発生さ
せる光合成生物を利用しているので、電力消費の少ない
。As described above, according to the present invention, there is provided a culture vessel containing a photosynthetic organism together with a culture solution, a carbon dioxide gas source that supplies carbon dioxide gas to the culture vessel, an optical fiber that introduces light, and a culture vessel in which the photosynthetic organism generates photosynthetic gas. Since the device is equipped with an oxygen container for deriving and storing fc oxygen from the culture container, it uses photosynthetic organisms that perform photosynthesis using 92 yuan energy and generate enemy search, so power consumption is low.
省エネルギーの酸素生産バイオリアクタ装置全提供でき
る効果がある。The energy-saving oxygen production bioreactor device can provide all the benefits.
第1図は従来の酸素発生装置を示す構成図、第2図はこ
の発明の一実施例の酵素生理バイオリアクタ装置を示す
栴成図、第3図は光合成生物の光合成による酸素発生速
度の経時変化を示す特性図である。
図において(1)は陽極、(2)は隘極、(3)は水、
(4)は発生した酸素、(5)は発生した水素、(6)
はm流電縣。
(71,(81はポンプ、(9)は酸素タンク、 01
は水素タンク、aυは補光用水タンク、a湯は補充用*
解液タンク、Qυ祉培養容器、(2)は光合成生物を混
入した培養液、cA3は光ファイバ、(2)は攪拌プロ
ペラ、(ホ)はモータ、(ハ)は温度コントローラ、@
は炭酸ガス源。
この場合は炭酸ガスボンベ、@は気液分離膜、(2)は
酸素容器、仁の場合は酸素タンク、−はポンプ。
0υは補充用光合成生物タンク、6っけ補充用培地タン
ク、0階は発数タンク、(ロ)、(至)、(至)はポン
プである。
代理人大岩増雄
昭和 年 月 日
1.事件の表示 特願昭58−232448号73、補
正をする者
5・補正の対象
明細書の発明の詳細な説明の欄。
6・ 補正の内容
(1)明細書の第6頁第20行の「5piulina
Jを「5pirul ina Jに訂正する。
(2)同第7頁第8行の[mas−JをrMas−Jに
訂正する。
以上Fig. 1 is a configuration diagram showing a conventional oxygen generating device, Fig. 2 is a schematic diagram showing an enzyme physiological bioreactor device according to an embodiment of the present invention, and Fig. 3 is a diagram showing the rate of oxygen generation by photosynthesis of photosynthetic organisms over time. FIG. 3 is a characteristic diagram showing changes. In the figure, (1) is the anode, (2) is the pole, (3) is the water,
(4) is generated oxygen, (5) is generated hydrogen, (6)
is the m current district. (71, (81 is the pump, (9) is the oxygen tank, 01
is a hydrogen tank, aυ is a water tank for supplementary lighting, and hot water is for replenishment *
Solution tank, Qυ culture container, (2) is a culture solution mixed with photosynthetic organisms, cA3 is an optical fiber, (2) is a stirring propeller, (E) is a motor, (C) is a temperature controller, @
is a carbon dioxide source. In this case, it is a carbon dioxide gas cylinder, @ is a gas-liquid separation membrane, (2) is an oxygen container, Jin is an oxygen tank, and - is a pump. 0υ is a photosynthetic organism tank for replenishment, a medium tank for 6-knife replenishment, the 0th floor is a firing tank, and (b), (to), and (to) are pumps. Agent Masuo Oiwa Showa Year Month Day 1. Display of case Japanese Patent Application No. 58-232448 No. 73, amended party 5, column for detailed explanation of the invention in the specification to be amended. 6. Contents of the amendment (1) “5piulina” on page 6, line 20 of the specification
Correct J to ``5pirul ina J.'' (2) Correct mas-J to rMas-J on page 7, line 8.
Claims (1)
、この培養容器に炭酸ガスを供給する炭酸ガス源、光を
上記培養容器に導入する光ファイバ。 上記光合成生物が光合成によシ生成した酸素を上記培養
容器から導出して収容する酸素容器を備えた酸素生産バ
イオリアクタ装置。 (2) 培養容器には光合成生物の光合成を促進する温
度コントローラが備わっている特許請求の範囲第1項記
載の酸素生産バイオリアクタ装置。 (3)培養容器には酸素を培養液から分離して酸素を酸
素容器に4出するように気液分離膜が備わっている特許
請求の範囲第1項又は第2項記載の酸素生産バイオリア
クタ装置。 (4) 光合成生物は緑藻である特許請求の範囲第1項
ないし第3項のいずれかに記載の酸素生産バイオリアク
タ装置。 (5) 光合成生物はクロレラである特許請求の範囲第
4項記載の酸素生産パイオリアクタ装置。 (6) 光合成生物はラン環である特許請求の範囲第1
項ないし第3項のいずれかに記載の酸素生産バイオリア
クタ装置。[Scope of Claims] +11 A culture vessel containing a photosynthetic organism along with a culture solution, a carbon dioxide gas source that supplies carbon dioxide gas to the culture vessel, and an optical fiber that introduces light into the culture vessel. An oxygen production bioreactor device comprising an oxygen container that extracts and stores oxygen produced by photosynthesis by the photosynthetic organisms from the culture container. (2) The oxygen production bioreactor device according to claim 1, wherein the culture container is equipped with a temperature controller that promotes photosynthesis of photosynthetic organisms. (3) The oxygen production bioreactor according to claim 1 or 2, wherein the culture container is equipped with a gas-liquid separation membrane to separate oxygen from the culture solution and release the oxygen into the oxygen container. Device. (4) The oxygen production bioreactor device according to any one of claims 1 to 3, wherein the photosynthetic organism is green algae. (5) The oxygen producing pyroreactor device according to claim 4, wherein the photosynthetic organism is chlorella. (6) Claim 1 that the photosynthetic organism is an orchid ring
The oxygen production bioreactor apparatus according to any one of Items 1 to 3.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23244883A JPS60126075A (en) | 1983-12-09 | 1983-12-09 | Oxygen-producing bioreactor device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23244883A JPS60126075A (en) | 1983-12-09 | 1983-12-09 | Oxygen-producing bioreactor device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60126075A true JPS60126075A (en) | 1985-07-05 |
Family
ID=16939435
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23244883A Pending JPS60126075A (en) | 1983-12-09 | 1983-12-09 | Oxygen-producing bioreactor device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60126075A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4894342A (en) * | 1986-05-12 | 1990-01-16 | C. D. Medical, Inc. | Bioreactor system |
KR100590296B1 (en) * | 2004-10-27 | 2006-06-19 | 진현진 | Chlorella culture method |
JP2017158541A (en) * | 2016-03-10 | 2017-09-14 | エアバス ディーエス ゲーエムベーハー | Transfer device |
US12264304B2 (en) | 2021-04-08 | 2025-04-01 | Premium Oceanic Inc. | Systems and methods for deepwater photobioreactor |
-
1983
- 1983-12-09 JP JP23244883A patent/JPS60126075A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4894342A (en) * | 1986-05-12 | 1990-01-16 | C. D. Medical, Inc. | Bioreactor system |
KR100590296B1 (en) * | 2004-10-27 | 2006-06-19 | 진현진 | Chlorella culture method |
JP2017158541A (en) * | 2016-03-10 | 2017-09-14 | エアバス ディーエス ゲーエムベーハー | Transfer device |
US10106767B2 (en) | 2016-03-10 | 2018-10-23 | Airbus Ds Gmbh | Transfer device |
US12264304B2 (en) | 2021-04-08 | 2025-04-01 | Premium Oceanic Inc. | Systems and methods for deepwater photobioreactor |
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