JPS5840196A - Preparation of methane-fermenting sludge - Google Patents

Preparation of methane-fermenting sludge

Info

Publication number
JPS5840196A
JPS5840196A JP56127605A JP12760581A JPS5840196A JP S5840196 A JPS5840196 A JP S5840196A JP 56127605 A JP56127605 A JP 56127605A JP 12760581 A JP12760581 A JP 12760581A JP S5840196 A JPS5840196 A JP S5840196A
Authority
JP
Japan
Prior art keywords
methane
bacteria
sludge
weight
growth
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
Application number
JP56127605A
Other languages
Japanese (ja)
Other versions
JPS6246239B2 (en
Inventor
Yasuyuki Nukina
康之 貫名
Shunji Namikawa
俊次 並河
Toshiichi Tomioka
敏一 冨岡
Takehiko Yamamoto
山本 武彦
Susumu Oi
進 大井
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP56127605A priority Critical patent/JPS5840196A/en
Publication of JPS5840196A publication Critical patent/JPS5840196A/en
Publication of JPS6246239B2 publication Critical patent/JPS6246239B2/ja
Granted legal-status Critical Current

Links

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

Landscapes

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

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は高濃度のメタン発酵用スラツヂの製造法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a highly concentrated sludge for methane fermentation.

メタン発酵は第一次石油ショック以来微生物を用いてエ
ネルギーを生産する一手段として注目され、農林、水産
、畜産廃棄物、都市生活廃棄物や工場廃水等を原料とし
て実施されている。一般に使用するメタン発酵菌は自然
界から採取したものを原料に応じて馴養したのち用いる
。馴養スラッジのメタン発酵能力はさまざまで、種々の
条件によって変化しやすい。そのため通常、装置内で沈
降濃縮したものをポンプ等で発酵槽に輸送する。
Methane fermentation has attracted attention as a means of producing energy using microorganisms since the first oil crisis, and has been carried out using agricultural, forestry, fisheries, livestock waste, urban waste, industrial wastewater, etc. as raw materials. Generally, the methane-fermenting bacteria used are collected from nature and used after being acclimatized according to the raw material. The methane fermentation capacity of acclimatized sludge varies and is easily changed depending on various conditions. For this reason, the product that is sedimented and concentrated in the device is usually transported to a fermentation tank using a pump or the like.

メタン発酵はそれに先立って細微生物による高分子有機
化合物の低分子化、揮発生有機酸の生成蓄積が行われ、
そこに生じた有機酸からの脱水素。
Methane fermentation is preceded by microorganisms converting high-molecular organic compounds into low-molecular molecules, producing and accumulating volatile organic acids,
Dehydrogenation from the organic acids generated there.

脱炭酸をへて、水素と二酸化炭素からメタンが合成され
る過程を辿っている。メタン発酵を高能率で行わせるた
めには、前段階の酸生成過程に役立つ微生物群と、後段
階のメタン生成を行うメタン菌1群を精選し適度の菌数
に整える必要がある。
The process follows the synthesis of methane from hydrogen and carbon dioxide after decarboxylation. In order to perform methane fermentation with high efficiency, it is necessary to carefully select a group of microorganisms that are useful for the acid production process in the first stage, and a group of methane bacteria that perform methane production in the second stage, and to maintain an appropriate number of bacteria.

従来用いられてきた濃縮スラッジには、培養原料のC/
N比が不適当なためにメタン菌の好まない有機酸を多量
に生成したり、メタン生成能が低かったり、また濃縮ス
ラッジが粘調なため取得困難なものがまま見受けられた
The conventionally used concentrated sludge contains C/C, which is a culture raw material.
Due to an inappropriate N ratio, a large amount of organic acids that methane bacteria do not like are produced, the methane production ability is low, and the concentrated sludge is so viscous that it is difficult to obtain it.

本発明者は、これらの点に注目して研究した結果、本発
明に至ったもので、メタン菌を短期間で生育させ、かつ
酸生成菌とメタン菌の生育バランス調整が必要なことを
認めこの調整方法に関して工夫を重ねた結果、ベントナ
イトと磨砂をある比率で混合したもの或は同質無機物で
ある川底沈泥を添加して嫌気的培養を行って菌を増殖せ
しめる方法が上述菌群の調整を極めて有効に達成できる
ことを確認した。培養液には主炭素源としてセルロース
やヘミセルロースを、主窒素源としてはポリペプトン、
酵母エスキ等を用いる。更に好ましくは菌の生育を強)
ヒ促進するだめの物質を微量添加すれば菌の生育は大巾
に促進され本発明を完成するにいたった。ヘミセルロー
ス質としては大豆種皮(大豆油製造工程で排出される農
産廃棄物)を用い、それを酵素で軽度に分解して可溶化
し、それにセルロースや微量のグルコースを混合する。
As a result of research focusing on these points, the present inventors have arrived at the present invention, and have recognized that it is necessary to grow methane bacteria in a short period of time and to adjust the growth balance between acid-producing bacteria and methane bacteria. As a result of repeated efforts regarding this adjustment method, we have found that the above-mentioned bacterial group can be adjusted by adding a mixture of bentonite and polishing sand in a certain ratio or river bottom silt, which is a homogeneous inorganic substance, and performing anaerobic culture to grow the bacteria. It was confirmed that this can be achieved extremely effectively. The culture solution contains cellulose and hemicellulose as the main carbon source, and polypeptone and hemicellulose as the main nitrogen source.
Use yeast eski etc. More preferably, it enhances the growth of bacteria)
By adding a small amount of a substance that promotes bacterial growth, the growth of bacteria was greatly promoted, leading to the completion of the present invention. As the hemicellulose material, soybean seed coat (agricultural waste produced during the soybean oil manufacturing process) is used, which is slightly decomposed and solubilized with enzymes, and then cellulose and a small amount of glucose are mixed with it.

窒素源としてポリペプトン、酵母エキス、トリブチカー
ゼ等を加え、また生育促進物質として微量のグルタミン
、アスパラギンとイノシトールを添加して培地とする。
A medium is prepared by adding polypeptone, yeast extract, tributicase, etc. as a nitrogen source, and trace amounts of glutamine, asparagine, and inositol as growth promoting substances.

これに上記、ベントナイトと磨砂(1:9の混合比率)
混合物や、川底沈泥等を培養液1ρに600yを加え、
嫌気条件下でメタン発酵菌を温度+ pHを最適条件に
保ち乍ら迅速に生育させて、メタン菌数のおおいい沈滓
を調製し、メタンスラッヂとして提供するものである。
Add to this the above, bentonite and polishing sand (mixing ratio of 1:9)
Add 600y of mixture, river bottom silt, etc. to 1ρ of culture solution,
Methane-fermenting bacteria are grown rapidly under anaerobic conditions while keeping the temperature and pH at optimal conditions to prepare a sludge with a large number of methane bacteria, which is then provided as methane sludge.

本発明におけるメタン発酵菌の培養方法について詳述す
る。培養液に添加するヘミセルロース質は大豆種皮(大
豆油製造工程で排出される農産廃棄物)752を16の
水道水に懸濁して126°C216分間高圧殺菌し、放
冷したのち、酵素セルラーゼ(セ・ルロシンAC,上田
化学株式会社熟成種黒カビ生産)を0.1〜1%(対重
量比)添加し、pH3,5〜4.0附近、温度26〜5
0℃で酵素を作用させ、低分子ヘミセルロースを含む溶
液を得る。この溶液にセルロース粉末(P紙粉末、東洋
科学産業製品、1%対重量)、グルコース(0,3%対
重量)を加え、窒素源としてポリペプトン(第五栄養株
式会社製、0.06%対重量)、酵母エキス(DIFC
O製、0.06%対重量)とトリブチカーゼ(BBL製
、 o、ocs%対重量)をそれぞれ添加し、また生育
促進物質として、L−グルタミン(和光純薬工業株式会
社製、 0.005%対重喰λL−アスパラギン(和光
純薬工業株式会社製。
The method for culturing methane-fermenting bacteria in the present invention will be described in detail. The hemicellulose material to be added to the culture solution is made by suspending soybean seed coat (agricultural waste produced in the soybean oil manufacturing process) 752 in tap water, sterilizing it under high pressure at 126°C for 216 minutes, allowing it to cool, and adding the enzyme cellulase (cellulase).・Added 0.1 to 1% (weight ratio) of Lurosin AC (produced by Ueda Chemical Co., Ltd., matured black mold), pH around 3.5 to 4.0, temperature 26 to 5.
Enzyme is allowed to act at 0°C to obtain a solution containing low molecular weight hemicellulose. Cellulose powder (P paper powder, Toyo Kagaku Sangyo product, 1% by weight) and glucose (0.3% by weight) were added to this solution, and polypeptone (manufactured by Daigo Nutrition Co., Ltd., 0.06% by weight) was added as a nitrogen source. weight), yeast extract (DIFC
0.06% by weight (manufactured by Wako Pure Chemical Industries, Ltd.) and tributicase (manufactured by BBL, 0.06% by weight) and tributicase (manufactured by BBL, 0.06% by weight) and L-glutamine (manufactured by Wako Pure Chemical Industries, Ltd., 0.005% by weight) as a growth promoting substance. Anti-jukui λL-asparagine (manufactured by Wako Pure Chemical Industries, Ltd.).

0 、005%対重量)、イノシトール(キング化学株
式会社製、0.005%対重量)とL−システィン塩酸
塩(、fo光純薬工業株式会社製、0.005%対重制
を添加する。また生育に不可欠なビタミンB1.B2は
各0.0005%とビタミンB6は0.001%、ビタ
ミンには0.004%(各ビタミン共、和光純薬工業株
式会社製)を添加する(ビタミンB1=塩酸チアミン、
ビタミンB2=リボフラビン、ビタミンB6=塩酸ピリ
ドキシン、ビタミンに=ビタミンに1)。
0.005% by weight), inositol (manufactured by King Chemical Co., Ltd., 0.005% by weight) and L-cystine hydrochloride (manufactured by Hikari Pure Chemical Industries, Ltd., 0.005% by weight). In addition, 0.0005% each of vitamins B1 and B2, 0.001% of vitamin B6, and 0.004% of vitamins (all vitamins, manufactured by Wako Pure Chemical Industries, Ltd.) are added (vitamin B1 and B2, which are essential for growth). = Thiamine hydrochloride,
Vitamin B2 = riboflavin, vitamin B6 = pyridoxine hydrochloride, vitamin = vitamin 1).

本発明において、培養液に添加する各種有機化合物をま
とめて示すと、下記1〜4となる。
In the present invention, various organic compounds added to the culture solution are summarized as 1 to 4 below.

1 ヘミセルロース可溶化液(大豆種皮から取得)。1 Hemicellulose solubilized liquid (obtained from soybean seed coat).

セルロース粉末、グルコース 2 酵母エキス、トリブチカーゼ、ポリペ7’ト/3 
L−グルタミン、L−アスパラギン、イノシトール、L
−システィン塩酸塩 4 ビタミンB1.B2.B6.に 1の主たる炭素源供給物の培養液中濃度については、ヘ
ミセルロース可溶化液は上記記載の濃度にて酵素反応の
のち作製されたものを、使用にあたっては7乃至10部
に稀釈して用いる。ヘミセルロース可溶化液に由来する
培養液中の全糖分量は0.02チ(対重量)でよい。
Cellulose powder, glucose 2, yeast extract, tributicase, polypeptide 7'/3
L-glutamine, L-asparagine, inositol, L
-Cystine hydrochloride 4 Vitamin B1. B2. B6. Concerning the concentration of the main carbon source supplied in the culture medium in step 1, the hemicellulose solubilized solution is prepared after enzymatic reaction at the concentration described above, and is diluted to 7 to 10 parts before use. The total sugar content in the culture solution derived from the hemicellulose solubilized solution may be 0.02 h (relative to weight).

2.3.4はそれぞれ酸生成菌およびメタン菌に対して
発育強化の効果を示すもので、大計に加えれば異常に酸
生成菌の生育を増大するため、最終的にはメタン菌の含
有割合を低下させる効果をもたらす。添加はO,OS乃
至0.3%程度を上限とする。
2.3.4 each shows the effect of strengthening the growth of acid-producing bacteria and methane bacteria, and if added to the total, the growth of acid-producing bacteria will be abnormally increased, so ultimately the inclusion of methane bacteria will increase the growth of acid-producing bacteria. This has the effect of lowering the ratio. The upper limit of addition is O, OS or about 0.3%.

酸生成菌およびメタン菌を包括する無機物質であるベン
トナイトと磨砂の混合割合は1:9父は2:8で、培養
液への添加割合は20乃至60%(対容量)が好ましい
。無機物質としては沈泥θ11底の青粘土)や時には凝
灰質砂(火山灰由来)でもよい。しかし、培養液へ混合
した場合のpf(は6.0乃至7.Oi/i:保つ必要
がある。
The mixing ratio of bentonite, which is an inorganic substance containing acid-producing bacteria and methane bacteria, and polishing sand is 1:9 and 2:8, and the addition ratio to the culture solution is preferably 20 to 60% (by volume). The inorganic material may be silt θ11 bottom blue clay) or sometimes tuffaceous sand (derived from volcanic ash). However, the pf (pf) when mixed into the culture solution must be maintained at 6.0 to 7.Oi/i.

以上詳述した粘土または中和ベントナイト等の硅酸系微
粒粉末を含む培養液を嫌気状態とし、この場合大型注射
筒内にとじこめるか、又は簡便には大型容器中に入れて
静置することにより行なわれる。37℃に保温したもの
に種菌を接種して、3日乃至4日間生育させればその際
の城主ガスを採取して分析し、メタン生成を確認すると
同時に、その沈滓中のメタン菌数を平板稀釈嫌気培養法
(嫌気ガスパック使用、置換気体はs o % N2゜
10チH2、1oチC02(対容量)を含む)により生
育を確認し、響光(メタン菌の固有7ラピンF42゜由
来)検出により、その菌数が計測できる。
The culture solution containing the clay or silicic acid-based fine powder such as neutralized bentonite described in detail above is brought to an anaerobic state, and in this case, it can be kept in a large syringe, or more conveniently, it can be placed in a large container and allowed to stand still. It is done. Inoculate the inoculum into a container kept at 37℃ and let it grow for 3 to 4 days, then collect and analyze the castle gas to confirm methane production, and at the same time measure the number of methane bacteria in the sediment by diluting it on a plate. Growth was confirmed by the anaerobic culture method (anaerobic gas pack was used, replacement gas included s o % N2°, 10% H2, 10% CO2 (relative to volume)), and Kyokou (derived from 7 lapin F42°, which is unique to methane bacteria). Through detection, the number of bacteria can be measured.

ベントナイトと磨砂(1:9混合)混合物や沈泥捷たは
凝灰質砂102と培養液10me、殺菌水10meを加
えて嫌気的にメタン発酵菌を生育させる。接種メタン発
酵菌(酸生成菌とメタン菌)数は5 X 106/1m
eとして、37℃、4日間培養した場合の葭数例を第1
表に示した。
A mixture of bentonite and polishing sand (1:9 mixture), silt sludge or tuffaceous sand 102, 10 me of culture solution, and 10 me of sterilized water are added to grow methane-fermenting bacteria anaerobically. The number of inoculated methane fermenting bacteria (acid producing bacteria and methane bacteria) is 5 x 106/1m
As e, the number of reeds when cultured at 37℃ for 4 days is
Shown in the table.

第1表 ※(酸生成菌)+(メタン菌) メタン発酵菌生育ののち、自然放置して沈滓を滓部への
メタン発酵菌の存在2分布を調べた結果が第2表で、大
部分のメタン発酵菌は沈滓に包括されている。
Table 1 *(Acid-producing bacteria) + (Methane bacteria) After the methane fermentation bacteria have grown, the sludge is left to stand naturally and the sludge is examined for the presence of methane fermentation bacteria in the slag. Table 2 shows the results of examining the distribution of methane fermentation bacteria. Some of the methane-fermenting bacteria are contained in the sediment.

第2表 このように本発明によれば、メタン発酵菌を粘土または
中和ベントナイト等の硅酸系微粒粉末で抱括してスラッ
ヂ化したことにより、高濃度のメタン発酵用スラッヂを
得ることができた。
Table 2 As described above, according to the present invention, a highly concentrated sludge for methane fermentation can be obtained by enclosing methane-fermenting bacteria with clay or silicic acid-based fine powder such as neutralized bentonite to form a sludge. did it.

代理人の氏名 弁理士 中 尾 敏 男 ほか1名=5Name of agent: Patent attorney Toshio Nakao and 1 other person = 5

Claims (1)

【特許請求の範囲】[Claims] メタン発酵菌を粘土または中和ベントナイト等の硅酸系
微粒粉末で抱括してスラツヂ化したメタン発酵用スラソ
ヂの製造法。
A method for producing a sludge for methane fermentation in which methane-fermenting bacteria are encapsulated in clay or silicic acid-based fine powder such as neutralized bentonite.
JP56127605A 1981-08-13 1981-08-13 Preparation of methane-fermenting sludge Granted JPS5840196A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56127605A JPS5840196A (en) 1981-08-13 1981-08-13 Preparation of methane-fermenting sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56127605A JPS5840196A (en) 1981-08-13 1981-08-13 Preparation of methane-fermenting sludge

Publications (2)

Publication Number Publication Date
JPS5840196A true JPS5840196A (en) 1983-03-09
JPS6246239B2 JPS6246239B2 (en) 1987-10-01

Family

ID=14964215

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56127605A Granted JPS5840196A (en) 1981-08-13 1981-08-13 Preparation of methane-fermenting sludge

Country Status (1)

Country Link
JP (1) JPS5840196A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6031892A (en) * 1983-08-02 1985-02-18 Chiaki Kobayashi Filter material for purifying sewage

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0416047U (en) * 1990-05-30 1992-02-10
JPH04122247U (en) * 1991-04-18 1992-11-02 三菱自動車工業株式会社 Electric side mirror device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6031892A (en) * 1983-08-02 1985-02-18 Chiaki Kobayashi Filter material for purifying sewage

Also Published As

Publication number Publication date
JPS6246239B2 (en) 1987-10-01

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