JPH0679720B2 - Methane fermentation method and apparatus - Google Patents

Methane fermentation method and apparatus

Info

Publication number
JPH0679720B2
JPH0679720B2 JP61086335A JP8633586A JPH0679720B2 JP H0679720 B2 JPH0679720 B2 JP H0679720B2 JP 61086335 A JP61086335 A JP 61086335A JP 8633586 A JP8633586 A JP 8633586A JP H0679720 B2 JPH0679720 B2 JP H0679720B2
Authority
JP
Japan
Prior art keywords
medium
tank
methane
methane fermentation
inoculum
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
Application number
JP61086335A
Other languages
Japanese (ja)
Other versions
JPS62244500A (en
Inventor
旭 松永
弘志 島崎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Electric Manufacturing Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Electric Manufacturing Co Ltd
Priority to JP61086335A priority Critical patent/JPH0679720B2/en
Publication of JPS62244500A publication Critical patent/JPS62244500A/en
Publication of JPH0679720B2 publication Critical patent/JPH0679720B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 A.産業上の利用分野 本発明は、有機性基質をメタン菌によりメタン発酵処理
する場合において問題となる脂肪酸濃度上昇を抑えるこ
とのできるメタン発酵方法及びその装置に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION A. Field of Industrial Application The present invention relates to a methane fermentation method and apparatus capable of suppressing an increase in fatty acid concentration, which is a problem when an organic substrate is subjected to methane fermentation treatment with methane bacteria. Is.

B.発明の概要 本発明は、有機性基質をメタン菌によりメタン発酵処理
する場合において、 メタン発酵の中間生成物である脂肪酸、特にプロピオン
酸の分解能が高い脂肪酸分解菌群をメタン菌群と共に培
養し、培養した種菌をメタン発酵タンクに補充供給する
ことによつて、 いわゆる酸敗現象を抑えて、メタン発酵の高効率化を図
ろうとするものである。
B. Summary of the Invention The present invention is a method for culturing an organic substrate with methane bacteria, in which a fatty acid-decomposing bacteria group, which has a high ability to decompose fatty acids, especially propionic acid, which is an intermediate product of methane fermentation, is cultivated together with the methane bacteria group. By supplementing and supplying the cultured inoculum to the methane fermentation tank, the so-called rancid phenomenon is suppressed and the efficiency of methane fermentation is increased.

C.従来の技術 メタン発酵システムにおいては、メタン菌などの嫌気性
微生物を含む種菌に対して、適量の有機性基質を与える
とメタン発酵の中間生成物である脂肪酸の濃度が上昇
し、これによりpHが低下してメタンガスの発生が阻害さ
れる。この現象は酸敗現象といわれ、メタン発酵システ
ムが信頼性に欠ける要因になつている。従来において
は、酸敗が起きた場合、基質の投入を控えてガス発生の
回復を持つか、あるいは種菌を入れかえる方法が行なわ
れていた。
C. Conventional Technology In a methane fermentation system, when an appropriate amount of organic substrate is given to an inoculum containing anaerobic microorganisms such as methane bacteria, the concentration of fatty acid, which is an intermediate product of methane fermentation, increases, which causes The pH is lowered and the generation of methane gas is hindered. This phenomenon is called rancidity, which causes the methane fermentation system to lack reliability. Conventionally, when rancidity occurs, a method of refraining from inputting a substrate and recovering gas generation or replacing the inoculum is used.

D.発明が解決しようとする問題点 上述の方法では、ガス発生が回復するまでに長時間を要
することが多く、また種菌を入れかえる方法については
多大な労力と経費を必要とするという問題もある。
D. Problems to be Solved by the Invention In the above method, it often takes a long time for the gas generation to be recovered, and there is a problem that the method for replacing the inoculum requires a great deal of labor and cost. .

本発明は、酸敗現象を防止でき、酸敗が起きた場合にも
短時間のうちにガス発生能を回復させることのできるメ
タン発酵方法及びその装置を提供することを目的とす
る。
It is an object of the present invention to provide a methane fermentation method and an apparatus thereof capable of preventing the rancidity phenomenon and recovering the gas generating ability in a short time even when rancidity occurs.

E.問題点を解決するための手段及び作用 先ず本発明の着眼点について述べると、一般にメタン発
酵システムにおいて高負荷運転を行つている場合、ある
いは発酵温度が低い場合には、脂肪酸濃度が上昇する
が、この脂肪酸の構成比についてはプロピオン酸及び酢
酸の構成比が高い。このうち酢酸はメタン菌の直接の基
質となるので、メタン菌を大量培養して酸敗状態の発酵
タンクに補充することによつて、メタンガス生成が行わ
れ、酢酸の濃度か低下する。
E. Means and Actions for Solving Problems First, the focus of the present invention will be described. Generally, when high load operation is performed in a methane fermentation system or when the fermentation temperature is low, the fatty acid concentration increases. However, regarding the composition ratio of this fatty acid, the composition ratio of propionic acid and acetic acid is high. Of these, acetic acid serves as a direct substrate for methane bacteria, so by mass-culturing the methane bacteria and replenishing them in a fermented tank in a rancid state, methane gas is produced and the concentration of acetic acid decreases.

一方プロピオン酸については、従来微生物処理により分
解するといつたことはあまり注目されていない。その理
由は、プロピオン酸メタン菌の直接の基質ではなく、嫌
気状態でプロピオン酸を分解する菌により(1)式のよ
うに分解されること、 CH3CH2COOH+2H2O→CH3COOH+CO2+3H2…(1) しかも、この分解反応は熱力学的には不利な反応であ
り、生成物である水素が系外に除去されないと反応が進
行しないこと、そしてプロピオン酸の分解活性の高い菌
体数が少ないことにある。
On the other hand, propionic acid has not received much attention when it is decomposed by conventional microbial treatment. The reason for this is that it is not a direct substrate of methane propionate, but is decomposed by a bacterium that decomposes propionic acid in an anaerobic state as in formula (1): CH 3 CH 2 COOH + 2H 2 O → CH 3 COOH + CO 2 + 3H 2 (1) Moreover, this decomposition reaction is a thermodynamically unfavorable reaction, and the reaction does not proceed unless hydrogen, which is a product, is removed to the outside of the system. There is a small number.

ここに本発明者は、プロピオン酸分解菌を培養してメタ
ン発酵タンク内に補充供給し、その培養においてはメタ
ン菌を混合し、このメタン菌により水素を消費させてメ
タンガスを生成し、これにより培養用培地内のプロピオ
ン酸の分解反応を促進すると共にプロピオン酸分解菌を
増殖させるという点に着眼して次のような発明をするに
至つた。
Here, the present inventor cultivates a propionic acid-degrading bacterium and replenishes and supplies it into a methane fermentation tank. In the culturing, methane bacterium is mixed, and hydrogen is consumed by the methane bacterium to generate methane gas. The present invention has been made in view of the point of promoting the decomposition reaction of propionic acid in the culture medium and proliferating the propionic acid-decomposing bacteria.

本発明方法は、プロピオン酸分解菌群を含む脂肪酸分解
菌群とメタン菌群とを主たる微生物とする種菌、及びプ
ロピオン酸分解菌選択培養用培地を混合して種菌を培養
し、これにより増殖した種菌を前記メタン発酵タンク内
に補充供給するようにしたものである。
The method of the present invention comprises inoculating the inoculum having a fatty acid-decomposing bacterium group including a propionic acid-decomposing bacterium group and a methane bacterium group as a main microorganism, and culturing the inoculum by mixing a medium for selective culture of propionic acid-decomposing bacteria, and thereby proliferating. The seed bacteria are replenished and supplied into the methane fermentation tank.

本発明装置は、プロピオン酸分解菌選択培養用培地を調
整するための培地調整タンクと、このタンク内の培地成
分を混合する第1の混合手段と、前記培地をバブリング
して脱酸素を行う不活性ガスの散気手段と、プロピオン
酸分解菌群を含む脂肪酸分解菌群とメタン菌群とを主た
る微生物とする種菌、及び前記培地調整タンクよりの培
地を収容する種菌培養タンクと、この種菌培養タンク内
で前記培地と種菌とを混合する第2の混合手段と、前記
種菌培養タンクにて発生したガスを収容するガスホルダ
ーと、有機性基質をメタン菌群によりメタン発酵処理す
るためのメタン発酵タンクと、前記培地調整タンク及び
種菌培養タンク間に設けられた培地供給ポンプと、前記
種菌培養タンク及びメタン発酵タンク間に設けられた種
菌供給ポンプとを備えて成るものである。
The apparatus of the present invention comprises a medium adjusting tank for adjusting a medium for selective culture of propionic acid-degrading bacteria, a first mixing means for mixing medium components in the tank, and a deoxidizing unit for bubbling the medium for deoxidation. A means for diffusing active gas, an inoculum having a fatty acid-decomposing bacteria group including a propionic acid-decomposing bacteria group and a methane bacteria group as main microorganisms, and an inoculum culture tank containing a medium from the medium adjusting tank, and this inoculum culture Second mixing means for mixing the medium and the inoculum in the tank, a gas holder for accommodating the gas generated in the inoculum culture tank, and a methane fermentation for methane fermentation treatment of an organic substrate with a methane bacteria group. A tank, a medium supply pump provided between the medium adjustment tank and the seed culture tank, and a seed supply pump provided between the seed culture tank and the methane fermentation tank. One in which Ete made.

F.実施例 第1図は本発明の実施例に係る装置を示す構成図であ
る。1は培地調整タンク、2は第1の混合手段としての
メカニカルスターラ、3は不活性ガスの散気手段、4は
ガスボンベである。前記タンク1は、プロピオン酸及び
酪酸を含むプロピオン酸分解菌選択培養用培地を調整す
るためのものであり、この中にて培地成分の溶解及び混
合が行われ、ガスボンベ4から散気手段3を介して送ら
れた不活性ガスによりバブリングされて培地の脱酸素が
行われる。この不活性ガスは、例えば窒素ガス及び二酸
化炭素ガスを体積比80:20の割合で混合したものが用い
られる。前記培地の調整に関しては、装置の説明の後に
述べる。第1図中5は培地供給ポンプ、6は種菌培養タ
ンク、7は第2の混合手段としてのメカニカルスター
ラ、8はガスホルダーである。前記培地調整タンクで調
整された培地は、前記ポンプ5を介して種菌培養タンク
6に供給され、ここでメカニカルスターラ7により培地
と種菌とが混合される。この種菌は、プロピオン酸分解
菌群を含む嫌気性脂肪酸分解菌群とメタン菌群とを主た
る微生物とするものである。そして培地中のプロピオン
酸及び酪酸は嫌気性脂肪酸分解菌群及びメタン菌群によ
つて分解され、これにより発生したメタンガスはガルホ
ルダー8に貯留される。プロピオン酸の分解反応の生成
物である水素は、メタン菌群によつて、同時に生成され
た酢酸,二酸化炭素と反応して系外に除去される。これ
によりメタンガスが生成されるが、水素が系外に除去さ
れることからプロピオン酸分解反応は進行し、この結果
プロピオン酸分解菌の増殖が促進される。また培地中の
基質の一部は菌の増殖のための栄養源になる。9は種菌
供給ポンプ、10はメタン発酵タンクであり、種菌培養タ
ンク6にて増殖した種菌の一部は、種菌供給ポンプ9を
介してメタン発酵タンク10に間欠的に送られる。メタン
発酵タンク10ではメタン発酵が行われており、その中間
生成物であるプロピオン酸は、メタン発酵タンク10内の
プロピオン酸分解菌群及び新たに補充されたプロピオン
酸分解菌群によつて分解される。中間生成物の脂肪酸の
うちプロピオン酸の構成比率が高いことから、これが分
解されることにより酸敗現象を未然に防止できるし、ま
た酸敗現象が起こつている場合でもそれを解消すること
ができる。
F. Embodiment FIG. 1 is a block diagram showing an apparatus according to an embodiment of the present invention. Reference numeral 1 is a culture medium adjustment tank, 2 is a mechanical stirrer as a first mixing means, 3 is an inert gas diffusing means, and 4 is a gas cylinder. The tank 1 is for adjusting a culture medium for selective culture of propionic acid-degrading bacteria containing propionic acid and butyric acid, in which the medium components are dissolved and mixed, and the gas cylinder 4 drives the aeration means 3 Bubbling is carried out by the inert gas sent through the medium to deoxidize the medium. As this inert gas, for example, a mixture of nitrogen gas and carbon dioxide gas in a volume ratio of 80:20 is used. The adjustment of the medium will be described after the explanation of the apparatus. In FIG. 1, 5 is a medium supply pump, 6 is a seed culture tank, 7 is a mechanical stirrer as a second mixing means, and 8 is a gas holder. The medium adjusted by the medium adjusting tank is supplied to the seed culture tank 6 via the pump 5, and the medium and the seed are mixed by the mechanical stirrer 7 there. This inoculum is mainly composed of an anaerobic fatty acid-decomposing bacteria group including a propionic acid-decomposing bacteria group and a methane bacteria group. Then, propionic acid and butyric acid in the medium are decomposed by the anaerobic fatty acid decomposing bacteria group and the methane bacteria group, and the methane gas generated by this is stored in the gal holder 8. Hydrogen, which is a product of the decomposition reaction of propionic acid, is removed to the outside of the system by reacting with acetic acid and carbon dioxide that are simultaneously produced by the methane bacteria group. As a result, methane gas is produced, but hydrogen is removed to the outside of the system, so that the propionic acid-decomposing reaction proceeds, and as a result, the growth of the propionic acid-decomposing bacteria is promoted. Moreover, a part of the substrate in the medium serves as a nutrient source for the growth of the fungus. 9 is a seed feed pump, 10 is a methane fermentation tank, and a part of the seed grown in the seed culture tank 6 is intermittently sent to the methane fermentation tank 10 via the seed feed pump 9. Methane fermentation is carried out in the methane fermentation tank 10, and its intermediate product, propionic acid, is decomposed by the propionic acid-decomposing bacteria group and the newly supplemented propionic acid-decomposing bacteria group in the methane fermentation tank 10. It Since the proportion of propionic acid in the fatty acid as an intermediate product is high, decomposition of the fatty acid can prevent the rancidity phenomenon in advance, and even if the rancidity phenomenon occurs, it can be eliminated.

次に前記培地調整タンク1における培地の調整に関して
述べると、先ず水にK2HPO4をK2HPO4の濃度が6g/lになる
よう溶解して得たミネラル1と、表1〜表3に夫々成分
を示すミネラル2,トレースミネラル及びトレースビタミ
ンを予め用意する。
Now be described with respect to adjustment of the medium in said medium adjustment tank 1, first mineral 1 of K 2 HPO 4 concentration of K 2H PO 4 was obtained by dissolving so as to be 6 g / l in water, Table 1 to Table 3 Prepare minerals 2, trace minerals and trace vitamins showing the respective ingredients in advance.

そして培地調整タンク1内にて、水にミネラル1,ミネラ
ル2,トレースミネラルを加え、FeSO4・7H2O,NaHCO3
レザズリンを溶解する。次にプロピオン酸と酪酸とを加
え、KOH溶液でpH7.4に調整する。オートクレーブで滅菌
後室温まで冷却し、散気手段3により不活性ガスをバブ
リングしながら表3のトレースビタミン,システイン塩
酸塩,硫化ソーダを過滅菌して加える。レザズリンの
色が消失して溶存酸素が無くなつたことを確認してから
前記不活性ガスをバブリングしたまま、培地供給ポンプ
5によつて培地を種菌培養タンク6に供給する。ここで
培地と種菌とが適当な温度で保温され、メカニカルスタ
ーラ7によつて間欠的に攪拌される。培養に適した温度
は30℃付近であるが、室温でも培養可能である。表4に
培地1の組成を示す。
Then, in the culture medium adjustment tank 1, mineral 1, mineral 2, trace mineral are added to the water, and FeSO 4 · 7H 2 O, NaHCO 3 ,
Dissolve resazurin. Next, propionic acid and butyric acid are added, and the pH is adjusted to 7.4 with a KOH solution. After sterilization in an autoclave, the mixture is cooled to room temperature, and while traces of an inert gas are bubbled by an air diffuser 3, trace vitamins, cysteine hydrochloride and sodium sulfide in Table 3 are oversterilized and added. After confirming that the color of resazurin has disappeared and dissolved oxygen has disappeared, the culture medium supply pump 5 supplies the culture medium to the inoculum culture tank 6 while bubbling the inert gas. Here, the medium and the inoculum are kept warm at an appropriate temperature and intermittently stirred by the mechanical stirrer 7. The temperature suitable for culturing is around 30 ° C, but culturing is possible at room temperature. Table 4 shows the composition of medium 1.

なお培地成分として、酪酸は必ずしも不要不可欠の成分
ではなく、例えば表4においてプロピオン酸及び酪酸を
各々2.5mlづつ加える代りにプロピオン酸を5ml加えるよ
うにしてもよいが、酪酸を添加すれば初期のガス発生速
度が大きいので、より培養に適している。
As a medium component, butyric acid is not always an indispensable component. For example, in Table 4, 5 ml of propionic acid may be added instead of 2.5 ml each of propionic acid and butyric acid. Since the gas generation rate is high, it is more suitable for culture.

G.発明の効果 プロピオン酸分解菌選択培養用培地で培養した嫌気性脂
肪酸分解菌群とメタン菌群を主たる構成微生物とする種
菌を混合培養し、増殖した種菌をメタン発酵タンクに補
充することにより、メタン発酵タンク内の嫌気性脂肪酸
分解菌群とりわけ本来菌体数が少ないプロピオン酸分解
菌の菌体数を増加し、高負荷時難分解性で蓄積しやすい
プロピオン酸を分解する能力を高めることができる。
G. Effects of the Invention By culturing the anaerobic fatty acid-decomposing bacteria group and the inoculum that mainly consists of the methane bacteria group, which have been cultivated in a selective culture medium for propionic acid-decomposing bacteria, by culturing them in a mixed manner, and supplementing the methane fermentation tank with the grown inoculum. , Increase the number of anaerobic fatty acid degrading bacteria in methane fermentation tanks, especially propionic acid-degrading bacteria that originally have a low number of bacteria, and enhance the ability to decompose propionic acid, which is difficult to decompose at high load and easily accumulates. You can

また同時にプロピオン酸(および酪酸)の嫌気性脂肪酸
分解菌による分解生成物である酢酸、CO2,H2などから
メタンを生成するメタン菌の菌体数も増加するので、プ
ロピオン酸,酪酸,酢酸などをガス化する能力が高くな
り、脂肪酸の濃度が低下してpHが上昇する。pHが中性か
ら弱アルカリ性域になれば、メタン菌に対しては最適pH
となりメタン発酵を活発に行うことができるる。
At the same time, the number of methane bacteria that produce methane from acetic acid, CO 2 , and H 2 , which are the decomposition products of propionic acid (and butyric acid) by anaerobic fatty acid-degrading bacteria, also increases. The ability to gasify such substances becomes higher, the concentration of fatty acids decreases, and the pH rises. Optimum pH for methane bacteria when the pH changes from neutral to weakly alkaline
Next, methane fermentation can be actively carried out.

したがつて本発明によれば、メタン発酵を高効率化し、
酸敗を防止する効果がある。またすでに酸敗が起きてい
るメタン発酵システムにおいて酸敗を解消し、すみやか
にガス発生能を回復させる効果がある。
Therefore, according to the present invention, the efficiency of methane fermentation is improved,
It has the effect of preventing rancidity. It also has the effect of eliminating rancidity in a methane fermentation system where rancidity has already occurred and promptly recovering the gas generating ability.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の実施例の装置を示す構成図である。 1……培地調整タンク、3……散気手段、5……培地供
給ポンプ、6……種菌培養タンク、9……種菌供給ポン
プ、10……メタン発酵タンク。
FIG. 1 is a block diagram showing an apparatus according to an embodiment of the present invention. 1 ... medium adjusting tank, 3 ... aeration means, 5 ... medium supply pump, 6 ... inoculum culture tank, 9 ... inoculum supply pump, 10 ... methane fermentation tank.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】メタン発酵タンク内で有機性基質をメタン
菌群によりメタン発酵処理する方法において、 プロピオン酸分解菌群を含む嫌気性脂肪酸分解菌群とメ
タン菌群とを主たる微生物とする種菌、及びプロピオン
酸分解菌選択培養用培地を混合して種菌を培養し、これ
により増殖した種菌を前記メタン発酵タンク内に補充供
給することを特徴とするメタン発酵方法。
1. A method for subjecting an organic substrate to a methane fermentation treatment of an organic substrate in a methane fermentation tank, wherein an inoculum mainly composed of an anaerobic fatty acid-decomposing bacteria group including a propionic acid-decomposing bacteria group and a methane bacteria group, And a medium for selective culture of propionic acid-degrading bacteria, the inoculum is cultivated, and the inoculum grown thereby is supplementarily supplied to the methane fermentation tank.
【請求項2】プロピオン酸分解菌選択培養用培地を調整
するための培地調整タンクと、このタンク内の培地成分
を混合する第1の混合手段と、前記培地をバブリングし
て脱酸素を行う不活性ガスの散気手段と、プロピオン酸
分解菌群を含む嫌気性脂肪酸分解菌群とメタン菌群とを
主たる微生物とする種菌、及び前記培地調整タンクより
の培地を収容する種菌培養タンクと、この種菌培養タン
ク内で前記培地と種菌とを混合する第2の混合手段と、
前記種菌培養タンクにて発生したガスを収容するガスホ
ルダーと、有機性基質をメタン菌群によりメタン発酵処
理するためのメタン発酵タンクと、前記培地調整タンク
及び種菌培養タンク間に設けられた培地供給ポンプと、
前記種菌培養タンク及びメタン発酵タンク間に設けられ
た種菌供給ポンプとを備えて成ることを特徴とするメタ
ン発酵装置。
2. A medium adjusting tank for adjusting a medium for selective culture of propionic acid-degrading bacteria, a first mixing means for mixing medium components in the tank, and a device for deoxidizing the medium by bubbling the medium. Aeration means for active gas, inoculum mainly composed of anaerobic fatty acid-decomposing bacteria group including propionic acid-decomposing bacteria group and methane bacteria group, and a seed culture tank containing a medium from the medium adjusting tank, and Second mixing means for mixing the medium and the inoculum in the inoculum culture tank;
A gas holder for containing gas generated in the seed culture tank, a methane fermentation tank for methane fermentation treatment of an organic substrate with a methane bacteria group, and a medium supply provided between the medium adjustment tank and the seed culture tank A pump,
A methane fermentation apparatus comprising a seed culture feed pump provided between the seed culture tank and the methane fermentation tank.
JP61086335A 1986-04-15 1986-04-15 Methane fermentation method and apparatus Expired - Lifetime JPH0679720B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61086335A JPH0679720B2 (en) 1986-04-15 1986-04-15 Methane fermentation method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61086335A JPH0679720B2 (en) 1986-04-15 1986-04-15 Methane fermentation method and apparatus

Publications (2)

Publication Number Publication Date
JPS62244500A JPS62244500A (en) 1987-10-24
JPH0679720B2 true JPH0679720B2 (en) 1994-10-12

Family

ID=13883972

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61086335A Expired - Lifetime JPH0679720B2 (en) 1986-04-15 1986-04-15 Methane fermentation method and apparatus

Country Status (1)

Country Link
JP (1) JPH0679720B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109111065A (en) * 2018-08-07 2019-01-01 上海久树环境科技有限公司 A kind of riverbed ecology synthesis restorative procedure

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62279896A (en) * 1986-05-30 1987-12-04 Kobe Steel Ltd Methane fermentation method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109111065A (en) * 2018-08-07 2019-01-01 上海久树环境科技有限公司 A kind of riverbed ecology synthesis restorative procedure

Also Published As

Publication number Publication date
JPS62244500A (en) 1987-10-24

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