JPS6225034B2 - - Google Patents
Info
- Publication number
- JPS6225034B2 JPS6225034B2 JP56127604A JP12760481A JPS6225034B2 JP S6225034 B2 JPS6225034 B2 JP S6225034B2 JP 56127604 A JP56127604 A JP 56127604A JP 12760481 A JP12760481 A JP 12760481A JP S6225034 B2 JPS6225034 B2 JP S6225034B2
- Authority
- JP
- Japan
- Prior art keywords
- methane
- oxygen
- days
- bacteria
- hydrogen
- 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
Links
Classifications
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Treatment Of Sludge (AREA)
Description
本発明はメタン生産効率が高く酸素の混入に強
いメタン発酵種菌の製造法に関する。
メタンは石油に替るエネルギーとして期待され
るものの1つであり、従来より発酵法によるメタ
ンガス製造に関しては多くの研究がある。最近の
優れた高速メタン発酵法として(昭和56年農芸化
学会、予稿集第82頁)0.5m3の液化発酵槽と1.5m3
のガス化発酵槽を用い全滞留日数8日、有機物負
荷15Kg/m3・日の条件下で連続発酵を行い、メタ
ン濃度70%の発酵ガスを有機物1Kg当たり300
を得ており、この装置より発生するメタンガス量
は15Kg/m3・日×(0.5+1.5)m3×300/Kg×70
%=6.3m3(CH4)である。
この例では8日×1.5m3/(0.5+1.5)m3=
6日となり、
液化ガス化2日、ガス化6日の日数を要してい
る。メタンガス生成反応が全発酵過程の律速段階
となつている。即ち、メタン生産菌のメタン生産
能が発酵過程の効率を支配する最重要因子となつ
ている。
又この例は連続発酵法であるから、定状運転中
のガス化槽中のメタン生産菌濃度は一定に保たれ
ている。しかし新しい基質の流入と同量の発酵終
了廃液がガス化発酵槽より流出するのであるか
ら、その流出分だけメタン生産菌は増殖している
こととなる。そのメタン生産菌の分裂時間は100
時間程度と考えられる。
したがつて、発酵過程でのメタン生産菌の増殖
は無視し得るほどにわずかで、生育定常期に於け
るメタン生産能が重要である。
さてメタン生産菌はバージエーのマニユアルに
記載されているように非常に厳密な絶対嫌気性菌
であつて、ごく微量の酸素が混入しても短時間内
に全菌は死滅する。この酸素に対して非常に敏感
で弱い特性は、メタン発酵種菌としてメタン生産
菌を保存し、大量培養し、運搬等の取り扱いを行
なう場合に著しい困難をもたらすもので、実用に
供されるメタン生産菌は、酸素に対しかなりの耐
性を有するものであることが望まれる。
以上の論拠により、本発明者らは生育定常期に
高いメタン生産能を有し、かつ混入酸素に対して
耐性を有するメタン生産菌の取得を目標として、
池沼沈泥及び嫌気性屎尿消化槽汚泥等よりメタン
生産菌の分離検索を行ない、上記の特性に合致し
た1株の中温(25〜40℃)メタン生産菌を取得し
た。これをメタノバクテリウム・エスピー・エス
テイー23(Methanobacterium SP・ST−23)と
呼ぶ。本菌は沈泥中の優占種として分離されたも
ので、沈泥1ml中には108〜109個が生存してい
る。
さて本菌の表の培地を用い35℃で液体培養すれ
ば、約7日間で生育定常期に達する。完全に生育
定常期に入つた生育15日目の培養物のメタン生産
能は、水素及び二酸化炭素を基質として、8.7×
10-8ml/個・日以上のメタン生産能を示した。な
お菌数の測定は平板培養法によつた。メタンガス
の分析はガスクロマトグラフ法によつた。このメ
タン発生能は、沈泥中の本菌の生存量の下限値
108/mlを算出根拠に採用し、先の文献例の槽容
量1.5m3に換算すると、13m3/日に相当し、実用
メタン発生能は非常に大である。
次に本菌の酸素に対する耐性について、110ml
容バイアルビンに50mlの培地をとり(気相60ml)
還元剤として硫化水素及びシステインを酸素の当
量として1ml加え、気相中に酸素(0〜12ml)を
加え、さらにH280%、CO220%の混合ガスを詰め
て1.5気圧として35℃で培養したところ、2mlま
での酸素の混合培養では3日後まで微量(0.05
ml/3日)のメタン生成を確認した。さらに14日
後、平板培養法により他菌の汚染を受けていない
こと及び、12mlまでの酸素の混入に対しても菌数
の減少は見られないことを確認した。60mlの気相
中12mlの酸素量は、大気中の酸素濃度と等しい量
であり、本菌は大気と同じ酸素分圧に耐えて生存
しえる。この点に関して、メタノバクテリウム・
モビレ(ジヤーナル・オブ・バクテリオロジー、
95巻、1943頁、1968年)は還元剤の当量以下の酸
素の存在で死滅するという。本菌の特性はこれら
の菌種からは大きく異なる。
本菌株は次のような菌学的性状を有する。
なお培養は培地に、H280%、CO220%の気相を
用いた。
(1) 光学顕微鏡的及び電子顕微鏡的所見
a直径0.3μm、長さ1.3〜3,3μmの丸い
末端を持つた直からやや曲つた桿菌。b著しい
不等分割を行い、時には球に近いものも存在す
る。c胞子は形成せず、d運動性無く、eベン
毛無く、fグラム陰性である。
(2) 寒天平板培養所見
a生育は悪く、b植菌4日後より微小な集落
が出現し、c14日間で最大径0.7〜1mmの集落と
なる。d若い集落は円形、全縁、白から淡黄緑
であり、e古くなると表面に浅く細かい方射状
のひだが入る。
3 生理学的性質
a中性(PH)付近にて生育する中温の嫌気性
菌、b水素及び二酸化炭素、又は蟻酸、若しく
は酢酸を資化して生育する。c酸素に対しては
1/5気圧までの分圧に耐えて生存し、1/30気圧
までの分圧に耐えて有意量のメタンを生産す
る。dペプトン及びアミノ酸による生育促進み
られず、eコエンザイム・エム(CoM)によ
る生育促進みられず、fイーストエキストラク
トによりわずかに生育促進が認められる。g沈
泥抽出液には生育促進効果がみとめられない
が、ある種の細菌との混合培養により著しく生
育促進をうける。
(4) その他
本菌破砕物可溶性画分は近紫外線の照射によ
り青緑色の蛍光を発す。
本菌株の属する分類学的地位をバージエイ
ズ・アニユアル・オブ・デターミネイテイブ・
バクテリオロジー第8版により求めると、メタ
ンを生産する桿菌という点からメタノバクテリ
ウム属に属するとするのが適当である。本菌株
は酢酸からメタンをつくる点で
Methanobacterium soehngeniiと類似するが、
このMethanobacterium soehngeniiは純粋分離
できないという点で生活型が本菌株と明白に相
違する。さらにメタノバクテリウム・フオルミ
シカムやメタノバクテリウム・モビレに近いと
考えられるが、いずれの種も酢酸の資化性を有
しない点をはじめとして既述の様々の相違点を
有し、本菌株はメタノバクテリウム属の新種と
するのが妥当と考えられる。そこで本菌の分離
源である沈泥の産出地の名称をとり、メタノバ
クテリウム・カドメンシス
(Methanobacterium kademensis)の新種名を
与えた。
本菌は工業技術院微生物工業技術研究所に
「微生物受託番号、微工研条寄第44号(FERM
BP−44)」のもとに微生物保管を委託した。
本菌の培養は例えば下記の表に示す組成の培
地により行なうことができる。硫化ソーダを増
量すればさらに酸素の影響を受けにくくなる
が、多量の硫化ソーダは本菌の生育を阻害する
ので実際的には表の量からその3倍程度の量が
適当である。培養の基質としては、水素及び二
酸化炭素、蟻酸、酢酸のいずれも利用できる
が、水素及び二酸化炭素、又は蟻酸を使用する
のが適当である。酢酸は熱力学的にも明らかな
様にきわめてゆつくりとしか利用されない。蟻
酸と水素の組合わせも可能であるが、この場合
高分圧の水素は生育に対し阻害的に働く。水素
及び二酸化炭素を基質とした場合、基質組成は
メタン生産の理論式より水素80%、二酸化炭素
20%が適当である。しかし培養の初期にはチツ
素ガス等で水素、二酸化炭素の混合ガスを希釈
して用いた方が生育がよい。培養温度は中温
域、35゜〜40℃が適当である。培地PHは中性付
近が適当であるが、気相の二酸化炭素濃度によ
り変化するし、蟻酸を使用する場合は、蟻酸の
利用減少に従い、培地PHは上昇するので、培地
組成に大きな緩衝能を持たせるか、又は培養期
間中常時中和を行なうかしなければならない。
又表のビタミン類に代えてイーストエキストラ
クト等のビタミン源を用いてもさしつかえな
い。生育には約7日間を要する。
この様にして培養して得られた菌体は、遠心分
離法、共沈法等公知の方法で集菌するか、あるい
はそのまま、他のメタン発酵系を構成する微生物
と混合しメタン発酵種菌として用いることができ
る。
The present invention relates to a method for producing a methane-fermenting starter that has high methane production efficiency and is resistant to oxygen contamination. Methane is one of the promising energy alternatives to petroleum, and there has been much research into producing methane gas through fermentation methods. As a recent excellent high-speed methane fermentation method (1982, Society of Agricultural Chemistry, Proceedings, p. 82), a liquefaction fermentation tank of 0.5 m 3 and a 1.5 m 3
Continuous fermentation was carried out using a gasification fermenter with a total residence time of 8 days and an organic matter load of 15 kg/m 3 days. Fermentation gas with a methane concentration of 70% was
The amount of methane gas generated by this device is 15Kg/ m3・day×(0.5+1.5) m3 ×300/Kg×70
%=6.3m 3 (CH 4 ). In this example, 8 days x 1.5 m 3 / (0.5 + 1.5) m 3 =
6 days, 2 days for liquefaction and 6 days for gasification. The methane gas production reaction is the rate-limiting step in the entire fermentation process. That is, the methane-producing ability of methane-producing bacteria is the most important factor governing the efficiency of the fermentation process. Furthermore, since this example is a continuous fermentation method, the concentration of methane-producing bacteria in the gasification tank is kept constant during steady-state operation. However, since the same amount of fermentation waste liquid flows out from the gasification fermenter as the new substrate flows in, the methane-producing bacteria proliferate by the amount that flows out. The division time of the methane-producing bacteria is 100
It is thought to be about an hour. Therefore, the growth of methane-producing bacteria during the fermentation process is negligible, and the methane-producing ability during the stationary growth phase is important. Now, as described in Bergier's manual, methane-producing bacteria are extremely strict anaerobic bacteria, and even if a very small amount of oxygen is mixed in, all the bacteria will die within a short period of time. This extremely sensitive and weak characteristic to oxygen causes significant difficulties when preserving methane-producing bacteria as seed bacteria for methane fermentation, culturing them in large quantities, and handling them such as transporting them. It is desired that the bacteria have considerable resistance to oxygen. Based on the above reasoning, the present inventors aimed to obtain methane-producing bacteria that have high methane-producing ability during the stationary growth phase and are resistant to mixed oxygen.
We isolated and searched for methane-producing bacteria from pond silt, anaerobic human waste digester sludge, etc., and obtained one strain of mesophilic (25-40°C) methane-producing bacteria that met the above characteristics. This is called Methanobacterium SP/ST-23. This bacterium was isolated as a dominant species in silt, with 10 8 to 10 9 living in 1 ml of silt. If this bacterium is cultured in liquid at 35°C using the medium listed above, it will reach the stationary growth phase in about 7 days. The methane production capacity of the culture on the 15th day of growth, which has completely entered the stationary growth phase, is 8.7× using hydrogen and carbon dioxide as substrates.
It showed a methane production capacity of more than 10 -8 ml/piece/day. The number of bacteria was measured by the plate culture method. Methane gas was analyzed by gas chromatography. This methane generating ability is the lower limit of the survival amount of this bacterium in silt.
Using 10 8 /ml as the calculation basis and converting it to the tank capacity of 1.5 m 3 in the previous literature example, it corresponds to 13 m 3 /day, and the practical methane generation capacity is extremely large. Next, regarding the resistance of this bacteria to oxygen, 110ml
Transfer 50ml of medium to a vial (gas phase: 60ml)
Add 1 ml of hydrogen sulfide and cysteine as a reducing agent as equivalent to oxygen, add oxygen (0 to 12 ml) to the gas phase, and fill with a mixed gas of 80% H 2 and 20% CO 2 at 1.5 atm at 35°C. When cultured, a trace amount (0.05
ml/3 days) of methane production was confirmed. Furthermore, after 14 days, it was confirmed by the plate culture method that there was no contamination with other bacteria, and that there was no decrease in the number of bacteria even when up to 12 ml of oxygen was mixed in. The amount of oxygen of 12 ml in 60 ml of gas phase is equivalent to the oxygen concentration in the atmosphere, and this bacterium can withstand the same oxygen partial pressure as the atmosphere and survive. In this regard, Methanobacterium
Mobile (Journal of Bacteriology,
95, p. 1943, 1968) is said to die in the presence of less than the equivalent amount of oxygen as the reducing agent. The characteristics of this bacterium differ greatly from those of these bacterial species. This strain has the following mycological properties. For culture, a gas phase containing 80% H 2 and 20% CO 2 was used as a medium. (1) Light microscopic and electron microscopic findings a Straight to slightly curved rod with a rounded end, 0.3 μm in diameter and 1.3 to 3.3 μm in length. bIt has markedly unequal divisions, sometimes close to spheres. c No spores are formed, d no motility, e no hairs, f gram negative. (2) Agar plate culture findings a. Growth is poor, b. Small colonies appear 4 days after inoculation, c. Colonies with a maximum diameter of 0.7 to 1 mm in 14 days. d Young colonies are circular, with entire edges, and white to pale yellow-green in color; e As they get older, shallow, fine, radial folds appear on the surface. 3 Physiological properties a. A mesophilic anaerobic bacterium that grows near neutral pH. b. Grows by assimilating hydrogen and carbon dioxide, or formic acid or acetic acid. c For oxygen
It can withstand partial pressures up to 1/5 atmosphere and survive, and can withstand partial pressures up to 1/30 atmosphere and produce significant amounts of methane. d No growth promotion was observed by peptone and amino acids, e no growth promotion was observed by coenzyme M (CoM), and f slight growth promotion was observed by yeast extract. Although no growth-promoting effect is observed in the silt extract, growth is significantly promoted by mixed culture with certain types of bacteria. (4) Others The soluble fraction of crushed bacteria emits blue-green fluorescence when irradiated with near ultraviolet light. The taxonomic status of this strain was determined by Verges Annual of Determinative.
According to the 8th edition of Bacteriology, it is appropriate that it belongs to the genus Methanobacterium because it is a rod that produces methane. This strain produces methane from acetic acid.
Similar to Methanobacterium soehngenii,
The life style of Methanobacterium soehngenii is clearly different from this strain in that it cannot be isolated in its pure form. Furthermore, although it is thought to be close to Methanobacterium formicicum and Methanobacterium mobilee, both species have various differences as mentioned above, including the fact that they do not have the ability to assimilate acetic acid. It is considered appropriate to classify it as a new species of the genus Bacterium. Therefore, the new species name, Methanobacterium kademensis, was given after the name of the place where the silt from which this bacterium was isolated was produced. This bacterium was submitted to the Institute of Microbial Technology, Agency of Industrial Science and Technology with the microbial accession number No. 44 (FERM).
The storage of microorganisms was outsourced under the BP-44). Cultivation of this bacterium can be carried out, for example, in a medium having the composition shown in the table below. Increasing the amount of soda sulfide will make it even less susceptible to the effects of oxygen, but since a large amount of sodium sulfide inhibits the growth of this bacterium, the appropriate amount is about three times the amount shown in the table. As a culture substrate, any of hydrogen and carbon dioxide, formic acid, and acetic acid can be used, and it is appropriate to use hydrogen and carbon dioxide or formic acid. As is clear from thermodynamics, acetic acid is only used very slowly. A combination of formic acid and hydrogen is also possible, but in this case high partial pressure of hydrogen acts as an inhibitor to growth. When hydrogen and carbon dioxide are used as substrates, the substrate composition is 80% hydrogen and carbon dioxide according to the theoretical formula for methane production.
20% is appropriate. However, in the early stages of culture, growth is better if a mixed gas of hydrogen and carbon dioxide is diluted with nitrogen gas or the like. The appropriate culture temperature is a medium temperature range, 35° to 40°C. The appropriate medium pH is around neutrality, but it changes depending on the carbon dioxide concentration in the gas phase, and if formic acid is used, the medium pH will increase as the use of formic acid decreases, so a large buffering capacity should be added to the medium composition. Either the cells must be allowed to remain in the culture, or they must be constantly neutralized during the culture period.
Also, vitamin sources such as yeast extract may be used in place of the vitamins listed in the table. It takes about 7 days to grow. The microbial cells cultured in this way can be collected using known methods such as centrifugation or coprecipitation, or they can be mixed with other microorganisms constituting a methane fermentation system as a methane fermentation starter. Can be used.
【表】
次にこの種菌製造の実施例を挙げて本発明の方
法を具体的に説明するが、これは本発明方法を限
定するものでない。
表の組成の液体培地を700ml容バイアルビンに
500mlとり、120℃、10分間のオートクレーブ滅菌
を行なう。ただしビタミン類及び炭酸ナトリウ
ム、硫化ソーダ、システイン塩酸は別に除菌過
を行ない、滅菌後の液体培地に合わせる。ブチル
ゴム栓にて密栓し、アルミキヤツプでおさえ、注
射針を通じて気相を水素80%、二酸化炭素20%の
混合ガスで置き代え、さらに1.5atmとなるまで
混合ガスを詰める。本菌の液体培養を1パーセン
トの割合で注射器を用いて植菌し、35℃で静置培
養する。この間2日に1度混合ガスを追加する。
10日後、660nmで測定した濁度は0.01となり平板
培養法により計数した菌濃度は106/mlとなり、
8000×G10分間の遠沈により200mgの湿菌体を得
た。
また液体培地に蟻酸トリウム又は酢酸ナトリウ
ム又はプロピオン酸ナトリウム又は酪酸ナトリウ
ム又はメタノール又はエタノールを除菌過して
0.1%になるよう添加する点、気相をN2ガスで置
換する点の2点以外の条件を前に述べた実施例と
同一として本菌を培養し、30日培養後の培地濁り
の増加をもつて定性的に生育の有無を判断した。
結果はギ酸ナトリウム添加のものと酢酸ナトリウ
ム添加のものに生育が見られ、他にはなかつた。
従つて、本菌は蟻酸、酢酸を基質として有効に生
産することができる。
このように本発明によれば、メタノバクテリウ
ム属に属し、生育定常期に高いメタン生産能を有
する、酸素耐性を示す菌株を用い、水素及び二酸
化炭素、又は蟻酸、若しくは酢酸の三つのグルー
プから選ばれた少くとも一つを基質とし、少くと
もチツ素源、無機塩、還元剤を添加した培地を用
い、中温域にて嫌気的に培養してメタン生産菌菌
体を取得したものであり、メタン生産効率が高く
酸素の混入に強いメタン発酵種菌が得られるもの
である。[Table] Next, the method of the present invention will be specifically explained with reference to Examples of the production of this seed culture, but this is not intended to limit the method of the present invention. Put the liquid medium with the composition shown in the table into a 700ml vial.
Take 500ml and sterilize in an autoclave at 120℃ for 10 minutes. However, vitamins, sodium carbonate, sodium sulfide, and cysteine hydrochloric acid should be sterilized separately and added to the sterilized liquid medium. Seal the tube with a butyl rubber stopper, cover with an aluminum cap, replace the gas phase with a mixed gas of 80% hydrogen and 20% carbon dioxide through the syringe needle, and fill with the mixed gas until the concentration reaches 1.5 atm. Inoculate a liquid culture of this bacterium at a rate of 1% using a syringe, and culture it statically at 35°C. During this time, add mixed gas once every two days.
After 10 days, the turbidity measured at 660 nm was 0.01, and the bacterial concentration counted by plate culture was 10 6 /ml.
200 mg of wet bacterial cells were obtained by centrifugation at 8000×G for 10 minutes. In addition, sterilize the liquid medium by adding thorium formate, sodium acetate, sodium propionate, sodium butyrate, methanol or ethanol.
This bacterium was cultured under the same conditions as in the previous example, except for the addition of 0.1% gas and the replacement of the gas phase with N 2 gas, and an increase in medium turbidity after 30 days of culture. The presence or absence of growth was determined qualitatively.
As a result, growth was observed in the plants added with sodium formate and those added with sodium acetate, but not in the others.
Therefore, this bacterium can effectively produce formic acid and acetic acid as substrates. As described above, according to the present invention, a strain belonging to the genus Methanobacterium and having high methane production ability during the stationary growth phase and exhibiting oxygen tolerance is used to produce hydrogen and carbon dioxide, or from the three groups of formic acid or acetic acid. Methane-producing bacterial cells are obtained by culturing anaerobically in a mesotemperature range using at least one of the selected substrates and a medium to which at least a nitrogen source, an inorganic salt, and a reducing agent are added. , it is possible to obtain a methane-fermenting starter that has high methane production efficiency and is resistant to oxygen contamination.
Claims (1)
高いメタン生産能を有し、かつ酸素耐性を示す菌
株を用い、水素及び二酸化炭素、又は蟻酸、若し
くは酢酸の三つのグループから選ばれた少くとも
一つを基質とし、かつ少くともチツ素源、無機
塩、還元剤を添加した培地を用い、中温域にて嫌
気的に培養してメタン生産菌菌体を取得するメタ
ン発酵種菌の製造法。1 Using a strain that belongs to the genus Methanobacterium and has a high methane production ability during the stationary growth phase and is resistant to oxygen, at least one of the following three groups is used: hydrogen and carbon dioxide, or formic acid or acetic acid. A method for producing a methane-fermenting inoculum, which comprises culturing anaerobically in a meso-temperature range to obtain methane-producing microorganisms using a medium containing a methane as a substrate and at least a chisel source, an inorganic salt, and a reducing agent.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56127604A JPS5840090A (en) | 1981-08-13 | 1981-08-13 | Preparation of seed of methane fermentation bacterium |
| US06/407,273 US4540666A (en) | 1981-08-13 | 1982-08-10 | Methane fermentation |
| PH27696A PH15950A (en) | 1981-08-13 | 1982-08-10 | Methane fermentation |
| GB08223382A GB2107735B (en) | 1981-08-13 | 1982-08-13 | Methane fermentation |
| DE3230197A DE3230197C2 (en) | 1981-08-13 | 1982-08-13 | Methane fermentation process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56127604A JPS5840090A (en) | 1981-08-13 | 1981-08-13 | Preparation of seed of methane fermentation bacterium |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5840090A JPS5840090A (en) | 1983-03-08 |
| JPS6225034B2 true JPS6225034B2 (en) | 1987-06-01 |
Family
ID=14964188
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56127604A Granted JPS5840090A (en) | 1981-08-13 | 1981-08-13 | Preparation of seed of methane fermentation bacterium |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5840090A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59176514A (en) * | 1983-03-24 | 1984-10-05 | Mitsubishi Electric Corp | Combustion control circuit |
| US4921799A (en) * | 1986-03-14 | 1990-05-01 | Kabushiki Kaisha Kobe Seiko Sho | Fermentation method |
| JPS62236489A (en) * | 1986-03-14 | 1987-10-16 | Kobe Steel Ltd | Production of methane |
| CN110747149B (en) * | 2019-12-03 | 2021-03-05 | 中国科学院烟台海岸带研究所 | Salt-tolerant methanogenic archaea and application thereof |
-
1981
- 1981-08-13 JP JP56127604A patent/JPS5840090A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5840090A (en) | 1983-03-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| McInerney et al. | Anaerobic bacterium that degrades fatty acids in syntrophic association with methanogens | |
| Oude Elferink et al. | Desulforhabdus amnigenus gen. nov. sp. nov., a sulfate reducer isolated from anaerobic granular sludge | |
| Tanner | Cultivation of bacteria and fungi | |
| Bryant et al. | Methanobacillus omelianskii, a symbiotic association of two species of bacteria | |
| Min et al. | Isolation and characterization of a thermophilic sulfate-reducing bacterium Desulfotomaculum thermoacetoxidans sp. nov. | |
| Samain et al. | Isolation and characterization of Desuljobulbus elongatus sp. nov. from a mesophilic industrial digester | |
| US4540666A (en) | Methane fermentation | |
| JPH0775588A (en) | Microbial hydrogen production method | |
| Finster et al. | Desulfuromonas acetexigens sp. nov., a dissimilatory sulfur-reducing eubacterium from anoxic freshwater sediments | |
| CN101705199B (en) | A kind of methanogenic composite bacterial agent and preparation method thereof | |
| CN111909867A (en) | Heterotrophic nitrification-aerobic denitrification bacterium and culture method and application thereof | |
| Esnault et al. | Characterization of Desulfovibrio giganteus sp. nov., a sulfate-reducing bacterium isolated from a brackish coastal lagoon | |
| Klasson et al. | Kinetics of light limited growth and biological hydrogen production from carbon monoxide and water by Rhodospirillum rubrum | |
| Magalhães et al. | Metabolic versatility of anaerobic sludge towards platform chemical production from waste glycerol | |
| JPS6225034B2 (en) | ||
| CN102041274A (en) | Method for producing hydrogen by fermenting special anaerobic clostridium butyricum | |
| CN105217799A (en) | A kind of industrial fermentation method of molten algae streptomycete active substance | |
| Boopathy | Isolation and characterization of a methanogenic bacterium from swine manure | |
| Singh et al. | Isolation of non-sulphur photosynthetic bacterial strains efficient in hydrogen production at elevated temperatures | |
| JP2611835B2 (en) | Anaerobic digestion | |
| CN100355878C (en) | Alkane-degrading functional bacteria, its cultivation method and application | |
| Bharati et al. | Degradation of cellulose by mixed cultures of fermentative bacteria and anaerobic sulfur bacteria | |
| JPS6230840B2 (en) | ||
| Drapoi et al. | Hydrogen production from cellulosic materials by natural microbial association from soil enriched by Clostridium and Bacillus microorganisms | |
| JP2849122B2 (en) | Low temperature resistant Methanosarcina methanogen NY-927 |