JPH0412955B2 - - Google Patents
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- Publication number
- JPH0412955B2 JPH0412955B2 JP57017132A JP1713282A JPH0412955B2 JP H0412955 B2 JPH0412955 B2 JP H0412955B2 JP 57017132 A JP57017132 A JP 57017132A JP 1713282 A JP1713282 A JP 1713282A JP H0412955 B2 JPH0412955 B2 JP H0412955B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen production
- production method
- cycle
- hydrogen
- cyanobacteria
- 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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- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Description
本発明は、明暗サイクルを利用したラン藻によ
る水素生産方法に関する。
近年、石油や石炭などの化石燃料に替わるクリ
ーンエネルギー源として水素が注目を集めてい
る。水素エネルギーは、(1)燃料電池を使えば高効
率で電気エネルギーへ変換することが可能であ
る、(2)単位重量当りの発熱量が石油の3〜4倍に
達し、しかも燃焼しても水となるだけで環境汚染
の恐れがない、(3)原料である水は無尽蔵に近い、
などの特徴を有している。この様な水素を太陽エ
ネルギーを利用して生産しようとする試みが、半
導体を用いた水分解などの非生物的方法と光合成
生物を利用する生物学的方法の両面から進められ
ている。後者の生物学的方法に関しては、水分解
能を有する高等植物および藻類の代謝を制御する
ことにより、または水素発生能を有する微生物と
組み合わせることにより水の生物学的光分解によ
る水素生産を行なう系が提案されている。しか
し、従来の系では水分解の結果生じる酸素は水素
発生系(ヒドロゲナーゼ)に対し失活ないし阻害
作用をもたらし、不安定性の主要因となることに
加え、水素の分離、精製が煩雑であり、水素−酸
素混合ガスの爆発の危険性があるなど、実用的な
水素生産方法とはいえない。
本発明者らは、優れた生産性と持続性を有する
生物学的水素生産方法を開発すべく研究を行なつ
た結果、特定の系では酸素の発生と水素の発生を
時間的に分離することにより、効率的に水素を生
産できることを見い出し本発明を完成するに至つ
た。
すなわち、本発明の要旨は、水素発生能を有す
るラン藻を、明好気条件下に水中で培養するサイ
クルと暗微好気条件下に水中で培養するサイクル
を交互に繰り返すことから成り、明好気条件下の
培養中に光合成を行なわせ、暗微好気条件下の培
養中に光合成により蓄積した物質を分解して水素
を発生させることを特徴とする明暗サイクルを利
用したラン藻による水素生産方法に存する。
本発明で使用するラン藻は、水素発生能を有す
るものならいずれでもよいが、就中シネココツク
ス属(Synechococcus sp.)が好ましい。ラン藻
は、いずれの増殖相(phase)のものも使用可能
であるが、暗微好気条件下での水素発生量(以
下、暗水素発生量という。)が多くなることから、
対数増殖期、特に対数増殖期中期のものが好まし
く使用される。
本発明方法では、明好気条件下の培養中に光合
成が行なわれてラン藻でん粉などの有機物が細胞
内で蓄積され、暗微好気条件下の培養中に蓄積さ
れた有機物が分解されて水素が発生する。
明好気条件下の培養は、適当な無機成分を含ん
だ培地中、光照射下、通気しながら行なう。培養
温度は用いるラン藻の種類によつて異なるが、通
常15〜70℃が好ましい。通気する空気中に、2〜
5容量%の二酸化炭素を混合するとでん粉などの
有機物の蓄積量が増すので好ましい。適当な培地
の例は、デトマー改変培地またはBG−11培地な
どである。これらの組成を下表に示す。
The present invention relates to a method for producing hydrogen using cyanobacteria using a light-dark cycle. In recent years, hydrogen has attracted attention as a clean energy source that can replace fossil fuels such as oil and coal. Hydrogen energy (1) can be converted into electrical energy with high efficiency using fuel cells, (2) has a calorific value per unit weight that is 3 to 4 times that of oil, and even when combusted. (3) Water, which is a raw material, is almost inexhaustible.
It has the following characteristics. Attempts to produce such hydrogen using solar energy are underway using both abiotic methods such as water splitting using semiconductors and biological methods using photosynthetic organisms. Regarding the latter biological method, there are systems that produce hydrogen through biological photolysis of water by controlling the metabolism of higher plants and algae that have the ability to decompose water, or by combining them with microorganisms that have the ability to generate hydrogen. Proposed. However, in conventional systems, oxygen generated as a result of water splitting deactivates or inhibits the hydrogen generation system (hydrogenase), becoming the main cause of instability, and the separation and purification of hydrogen is complicated. It cannot be said to be a practical hydrogen production method because there is a risk of explosion of the hydrogen-oxygen mixed gas. The present inventors conducted research to develop a biological hydrogen production method with excellent productivity and sustainability. As a result, in a specific system, the generation of oxygen and the generation of hydrogen can be temporally separated. They discovered that hydrogen can be efficiently produced by this method and completed the present invention. That is, the gist of the present invention consists of alternately repeating a cycle of culturing cyanobacteria capable of hydrogen generation in water under light aerobic conditions and a cycle of culturing them in water under dark microaerobic conditions. Hydrogen produced by cyanobacteria using a light-dark cycle, which is characterized by photosynthesizing during cultivation under aerobic conditions and decomposing substances accumulated through photosynthesis during cultivation under dark microaerobic conditions to generate hydrogen. It depends on the production method. The cyanobacteria used in the present invention may be any species as long as they have hydrogen-generating ability, but Synechococcus sp. is particularly preferred. Cyanobacteria in any growth phase can be used, but the amount of hydrogen produced under dark microaerobic conditions (hereinafter referred to as dark hydrogen production) increases.
Those in the logarithmic growth phase, particularly in the mid-logarithmic growth phase, are preferably used. In the method of the present invention, organic matter such as cyanobacteria starch is accumulated within the cells due to photosynthesis during cultivation under light aerobic conditions, and organic matter accumulated during cultivation under dark microaerobic conditions is decomposed. Hydrogen is generated. Cultivation under light and aerobic conditions is carried out in a medium containing appropriate inorganic components under light irradiation and with aeration. The culture temperature varies depending on the type of blue-green algae used, but is usually preferably 15 to 70°C. In the ventilated air, 2~
It is preferable to mix 5% by volume of carbon dioxide because it increases the amount of organic matter such as starch accumulated. Examples of suitable media include Detmer modified medium or BG-11 medium. Their compositions are shown in the table below.
【表】【table】
【表】【table】
【表】
暗微好気条件下の培養は、微量の酸素を含む窒
素雰囲気下、光を遮断して行なう。温度は用いる
ラン藻の最適増殖温度付近が好ましい。窒素雰囲
気中に含まれる酸素の量は培養条件により異なる
が、あまり多くなると水素発生系に阻害的に作用
して好ましくなく、通常0.1容量%を越えないこ
とが好ましい。暗条件での培養開始時に、0.30容
量%を越えない、特に0.23容量%を越えない量の
酸素を気相中に存在させると暗水素発生速度が増
すので好ましい。また、暗水素発生量は培地を攪
拌または振盪することにより増加する。
明暗サイクルは、人工的に作り出すこともでき
るが、昼夜の明暗サイクルに合わせるのが適当で
ある。
本発明の方法では、太陽エネルギーを利用して
非常に経済的にかつ効率的に水素を生産すること
ができるだけでなく、明条件で増殖するラン藻を
回収してバイオマスなどの有用物質生産に用いる
ことも可能である。
次に実施例を示し、本発明方法を具体的に説明
する。
実施例
明条件における培養
別府温泉より分離した単細胞好熱性ラン藻
(Synechococcus sp.)を、BG−11培地(PH7.0)
500mlを入れた1フラスコに加え、蛍光灯照射
下、培養増殖させた。フラスコは、45℃に保つた
空気恒温室中において100rpmで往復振盪した。
暗水素発生
藻濃度が約20μg drywt./mlに達した時、遠
心分離により藻を集菌し、BG−11培地で2回洗
浄した後、同培地10mlに再懸濁した。このときの
藻濃度は0.17mg/mlであつた。懸濁液を遮光した
試験管(内容積34ml)に入れ、ゴム栓で密封し
た。気相を窒素ガスで置換し、少量酸素を注射器
で添加した。45℃の恒温槽内で100rpmの往復振
盪を加えた。振盪開始後2,6.5,12および20時
間目に気相試料500μを採取し、組成をガスク
ロマトグラフイにより求めた。
結果を第4表に示す。[Table] Cultivation under dark microaerobic conditions is carried out in a nitrogen atmosphere containing a trace amount of oxygen, with light blocked. The temperature is preferably around the optimal growth temperature of the blue-green algae used. The amount of oxygen contained in the nitrogen atmosphere varies depending on the culture conditions, but if it is too large, it will inhibit the hydrogen generation system and is undesirable, so it is usually preferable not to exceed 0.1% by volume. It is preferable to include oxygen in the gas phase in an amount not exceeding 0.30% by volume, particularly not exceeding 0.23% by volume, at the start of cultivation under dark conditions, since this increases the rate of dark hydrogen generation. Furthermore, the amount of dark hydrogen generated increases by stirring or shaking the medium. Although the light-dark cycle can be created artificially, it is appropriate to match it to the day-night light-dark cycle. The method of the present invention not only makes it possible to produce hydrogen very economically and efficiently using solar energy, but also collects cyanobacteria that proliferate under light conditions and uses them to produce useful substances such as biomass. It is also possible. Next, examples will be shown to specifically explain the method of the present invention. Example Culture under light conditions Unicellular thermophilic cyanobacteria (Synechococcus sp.) isolated from Beppu Onsen were cultured in BG-11 medium (PH7.0).
It was added to one flask containing 500 ml and cultured and grown under fluorescent light irradiation. The flask was shaken reciprocally at 100 rpm in a constant air chamber maintained at 45°C. Dark Hydrogen Generation When the algae concentration reached approximately 20 μg drywt./ml, the algae were collected by centrifugation, washed twice with BG-11 medium, and then resuspended in 10 ml of the same medium. The algae concentration at this time was 0.17 mg/ml. The suspension was placed in a light-shielded test tube (inner volume: 34 ml) and sealed with a rubber stopper. The gas phase was replaced with nitrogen gas and a small amount of oxygen was added via syringe. Reciprocating shaking at 100 rpm was applied in a constant temperature bath at 45°C. At 2, 6.5, 12, and 20 hours after the start of shaking, 500μ samples of the gas phase were taken, and the composition was determined by gas chromatography. The results are shown in Table 4.
【表】
気相部酸素濃度が0.08容量%のときは20時間後
も水素発生は認められなかつたが、0.3容量%の
酸素を含むときは、6.5時間頃から水素の生成が
認められ、その後少なくとも10数時間水素発生が
持続した。[Table] When the gas phase oxygen concentration was 0.08% by volume, no hydrogen generation was observed even after 20 hours, but when the oxygen concentration was 0.3% by volume, hydrogen generation was observed from around 6.5 hours, and then Hydrogen evolution continued for at least 10 hours.
Claims (1)
に水中で培養するサイクルと暗微好気条件下に水
中で培養するサイクルを交互に繰り返すことから
成り、明好気条件下の培養中に光合成を行なわ
せ、暗微好気条件下の培養中に光合成により蓄積
した物質を分解して水素を発生させることを特徴
とする明暗サイクルを利用したラン藻による水素
生産方法。 2 明好気条件下の培養中、水中に空気と二酸化
炭素の混合ガスを通気する特許請求の範囲第1項
記載の水素生産方法。 3 二酸化炭素と空気の容量比が0:100〜10:
90である特許請求の範囲第2項記載の水素生産方
法。 4 暗微好気条件下の培養を、気相中に0.30容量
%を越えない酸素を存在させて開始し、微量酸素
を含む窒素雰囲気下に行なう特許請求の範囲第1
項記載の水素生産方法。 5 対数増殖期のラン藻を用いる特許請求の範囲
第1項記載の水素生産方法。 6 対数増殖期中期のラン藻を用いる特許請求の
範囲第5項記載の水素生産方法。 7 ラン藻がシネココツクス属(Synechoccus
sp.)である特許請求の範囲第1項、第5項また
は第6項記載の水素生産方法。 8 各サイクルでの培養温度が15〜60℃である特
許請求の範囲第1項記載の水素生産方法。 9 各サイクルでの培養温度が40〜55℃である特
許請求の範囲第8項記載の水素生産方法。 10 暗微好気条件下の培養を、攪拌または振盪
しながら行なう特許請求の範囲第1項記載の水素
生産方法。 11 明暗サイクルが昼夜サイクルである特許請
求の範囲第1項記載の水素生産方法。[Scope of Claims] 1. A method consisting of alternately repeating a cycle of culturing cyanobacteria capable of hydrogen generation in water under light aerobic conditions and a cycle of culturing them in water under dark microaerobic conditions. Hydrogen production by cyanobacteria using a light-dark cycle characterized by photosynthesis during cultivation under atmospheric conditions and decomposition of substances accumulated through photosynthesis during cultivation under dark microaerobic conditions to generate hydrogen. Method. 2. The hydrogen production method according to claim 1, wherein a mixed gas of air and carbon dioxide is aerated into the water during cultivation under light and aerobic conditions. 3 The volume ratio of carbon dioxide and air is 0:100 to 10:
90. The hydrogen production method according to claim 2, wherein the hydrogen production method is 90. 4.Culture under dark microaerobic conditions is initiated in the presence of not more than 0.30% by volume of oxygen in the gas phase, and is carried out in a nitrogen atmosphere containing a trace amount of oxygen.Claim 1
Hydrogen production method described in section. 5. The hydrogen production method according to claim 1, using cyanobacteria in the logarithmic growth phase. 6. The hydrogen production method according to claim 5, using cyanobacteria in the mid-logarithmic growth phase. 7 Cyanobacteria are of the genus Synechoccus (Synechoccus).
sp.), the hydrogen production method according to claim 1, 5 or 6. 8. The hydrogen production method according to claim 1, wherein the culture temperature in each cycle is 15 to 60°C. 9. The hydrogen production method according to claim 8, wherein the culture temperature in each cycle is 40 to 55°C. 10. The hydrogen production method according to claim 1, wherein the culture is carried out under dark microaerobic conditions with stirring or shaking. 11. The hydrogen production method according to claim 1, wherein the light/dark cycle is a day/night cycle.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57017132A JPS58134993A (en) | 1982-02-04 | 1982-02-04 | Production of hydrogen by cyanophyta using light and dark cycle |
| US06/424,767 US4532210A (en) | 1981-10-08 | 1982-09-27 | Process for producing hydrogen by alga in alternating light/dark cycle and environmental aerobic/microaerobic conditions |
| CA000412568A CA1194438A (en) | 1981-10-08 | 1982-09-30 | Process for producing hydrogen by alga in alternating light/dark cycle |
| AU89120/82A AU557378B2 (en) | 1981-10-08 | 1982-10-05 | Production of hydrogen by alga |
| DE8282109224T DE3269659D1 (en) | 1981-10-08 | 1982-10-06 | Process for producing hydrogen by alga in alternating light/dark cycle |
| EP82109224A EP0077014B1 (en) | 1981-10-08 | 1982-10-06 | Process for producing hydrogen by alga in alternating light/dark cycle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57017132A JPS58134993A (en) | 1982-02-04 | 1982-02-04 | Production of hydrogen by cyanophyta using light and dark cycle |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58134993A JPS58134993A (en) | 1983-08-11 |
| JPH0412955B2 true JPH0412955B2 (en) | 1992-03-06 |
Family
ID=11935501
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57017132A Granted JPS58134993A (en) | 1981-10-08 | 1982-02-04 | Production of hydrogen by cyanophyta using light and dark cycle |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58134993A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS591479B2 (en) * | 1981-09-30 | 1984-01-12 | 工業技術院長 | Cultivation method for photosynthetic microorganisms with photohydrogen production ability |
-
1982
- 1982-02-04 JP JP57017132A patent/JPS58134993A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58134993A (en) | 1983-08-11 |
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