JP2002159946A - Anaerobic fermentation tank, anaerobic fermentation system and anaerobic fermentation method - Google Patents

Anaerobic fermentation tank, anaerobic fermentation system and anaerobic fermentation method

Info

Publication number
JP2002159946A
JP2002159946A JP2000360990A JP2000360990A JP2002159946A JP 2002159946 A JP2002159946 A JP 2002159946A JP 2000360990 A JP2000360990 A JP 2000360990A JP 2000360990 A JP2000360990 A JP 2000360990A JP 2002159946 A JP2002159946 A JP 2002159946A
Authority
JP
Japan
Prior art keywords
anaerobic
fermenter
anaerobic fermentation
fermentation
tank
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
Application number
JP2000360990A
Other languages
Japanese (ja)
Inventor
Takashi Kono
孝志 河野
Tomohiko Hirao
知彦 平尾
Shizuo Kataoka
静夫 片岡
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.)
Takuma Co Ltd
Original Assignee
Takuma 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 Takuma Co Ltd filed Critical Takuma Co Ltd
Priority to JP2000360990A priority Critical patent/JP2002159946A/en
Publication of JP2002159946A publication Critical patent/JP2002159946A/en
Pending 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

  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an anaerobic fermentation tank with which anaerobic fermentation gas dispersing no unpleasant odor in a surrounding environment can be obtained at a low treating cost and to provide an anaerobic fermentation system provided with the anaerobic fermentation tank and an anaerobic fermentation method. SOLUTION: The anaerobic fermentation tank 1 of a horizontal type in which anaerobic fermentation treatment can be executed by being hermetically sealed is provided with a fixed bed 4 which is inserted inside the fermentation tank 1 and can hold anaerobic bacteria and is capable of being connected with a feed pump 7 for feeding a material to be treated A from an entrance side to an exit 6 side in the fermentation tank 1. Further, the anaerobic fermentation system provided with the anaerobic fermentation tank and the anaerobic fermentation method are also provided.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は嫌気発酵槽と嫌気発
酵システム及び嫌気発酵方法に関し、詳しくは、生ゴミ
等を低コストで処理可能な嫌気発酵槽と、これを備えた
嫌気発酵システム及び嫌気発酵方法に関する。
The present invention relates to an anaerobic fermenter, an anaerobic fermentation system, and an anaerobic fermentation method. More specifically, the present invention relates to an anaerobic fermenter capable of treating garbage and the like at a low cost, an anaerobic fermentation system provided with the anaerobic fermenter, and an anaerobic fermenter. It relates to a fermentation method.

【0002】[0002]

【従来の技術】生ゴミ、蓄糞、汚泥などの処理システム
として、バクテリアを利用するいわゆる微生物利用技術
が行われていて、微生物の発酵作用により、堆肥(コン
ポスト)を得る方法、発生したメタン等のガスを燃料と
して用いるシステム等がある。これには、分子状酸素の
存在下で処理を行う好気性発酵と、分子状酸素を必要と
しない嫌気性発酵があり、処理速度が早い等の理由から
前者が多く採用されてきた。
2. Description of the Related Art As a system for treating garbage, feces, sludge, and the like, a so-called microbial utilization technology utilizing bacteria has been used. A method for obtaining compost (compost) by fermentation of microorganisms, generated methane, etc. There is a system using the same gas as fuel. These include aerobic fermentation in which treatment is performed in the presence of molecular oxygen, and anaerobic fermentation that does not require molecular oxygen, and the former has been often employed because of its high processing speed.

【0003】しかしながら、好気性発酵により好気性コ
ンポストを得る場合、常に酸素を送給する必要上、送風
時に臭気が飛散するという問題があり、環境上、好まし
いものではなく、改良の要請が強い。
[0003] However, when aerobic compost is obtained by aerobic fermentation, oxygen must be supplied constantly, and there is a problem that odors are scattered at the time of blowing, which is not environmentally preferable and demands for improvement are strong.

【0004】一方、密閉したシステムで処理して得られ
る嫌気性発酵ガスでは、そのような問題がなく、しかも
消化残渣もほとんど臭気を発しないため、最近、嫌気性
発酵システムが注目を集めるに至っている。
On the other hand, the anaerobic fermentation gas obtained by processing in a closed system does not have such a problem, and the digestion residue hardly emits an odor. I have.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、これま
での嫌気性発酵ガス回収システムは、嫌気性菌を槽内で
繁殖させるため、細かく破砕処理された副資材(剪定
枝、紙など)を必要とするなど、前処理および発酵処理
のために少なくない処理コストを要していた。しかも、
これまで縦型の発酵槽を用いていたので、処理を行うに
際して、内容物の上下方向移動あるいは攪拌に少なから
ぬ電力コストを要することになり、そのため被処理物の
粘度を低くするために、水分を補給して被処理物を10
%程度に希釈していた。このようにすると、排水処理す
べき排水量が多くなり、排水設備を大きくしたり、排水
処理に少なくない処理コストがかかっていた。
However, the conventional anaerobic fermentation gas recovery system requires a finely crushed auxiliary material (pruned branches, paper, etc.) in order to propagate the anaerobic bacteria in the tank. For example, the pretreatment and the fermentation treatment required a considerable processing cost. Moreover,
Until now, a vertical fermenter was used, so that when processing, a considerable amount of power cost was required for moving the contents in the vertical direction or stirring, and to reduce the viscosity of the object to be treated, And replenish 10
%. In this case, the amount of wastewater to be treated is increased, the size of the drainage equipment is increased, and the treatment cost of the wastewater treatment is not small.

【0006】そこで、本発明の目的は、周囲環境に不快
な臭気を飛散させることがない嫌気性発酵ガスを、低い
処理コストで得られる嫌気発酵槽、これを備えた嫌気発
酵システム及び嫌気発酵方法を提供することにある。
Accordingly, an object of the present invention is to provide an anaerobic fermentation tank capable of obtaining an anaerobic fermentation gas which does not disperse an unpleasant odor to the surrounding environment at a low processing cost, an anaerobic fermentation system provided with the anaerobic fermentation tank, and an anaerobic fermentation method. Is to provide.

【0007】[0007]

【課題を解決するための手段】上記目的は各請求項記載
の発明により達成される。すなわち、本発明に係る嫌気
発酵槽の特徴構成は、密封して嫌気発酵処理可能な横型
の発酵槽であって、この発酵槽内部に挿入されて嫌気性
菌を保持可能な固定床を備え、前記発酵槽内の入口側か
ら出口側に向けて被処理物を送給する送給手段と接続可
能になっていることにある。
The above object is achieved by the invention described in each claim. That is, the characteristic configuration of the anaerobic fermentation tank according to the present invention is a horizontal fermentation tank capable of performing anaerobic fermentation treatment in a sealed manner, including a fixed bed capable of holding anaerobic bacteria by being inserted inside the fermentation tank, The present invention is characterized in that it can be connected to a feeding means for feeding an object to be processed from an inlet side to an outlet side in the fermenter.

【0008】この構成によれば、従来技術のような、手
間のかかる前処理を必要とする副資材を処理の都度用い
る必要がないので、処理コストを低くすることができ、
しかも固定床に嫌気性菌を培養することにより、処理能
力を十分高く維持することができて、安価に嫌気性発酵
ガスが得られる。しかも、被処理物を槽内の横方向に押
し出すようにしているため、強力でエネルギーコストの
低い油圧式の押出し手段などを使用できるので、被処理
物をほとんど希釈する必要がなく、格別大規模な排水処
理設備を必要とせず、排水処理コストも低く押さえるこ
とができる。
According to this structure, it is not necessary to use a secondary material requiring a complicated pretreatment as in the prior art every time the treatment is performed, so that the processing cost can be reduced.
Moreover, by culturing the anaerobic bacteria on the fixed bed, the processing capacity can be maintained sufficiently high, and the anaerobic fermentation gas can be obtained at low cost. In addition, since the object to be processed is extruded in the horizontal direction in the tank, a powerful and low-energy hydraulic extruder can be used, so there is almost no need to dilute the object to be processed. No wastewater treatment equipment is required, and wastewater treatment costs can be kept low.

【0009】前記発酵槽に、投入された被処理物を緩速
度で攪拌可能な攪拌機構と、嫌気性菌の繁殖を促進可能
にする加熱手段とが設けられていることが好ましい。
It is preferable that the fermenter is provided with a stirring mechanism capable of agitating the thrown object at a slow speed and a heating means capable of promoting the propagation of anaerobic bacteria.

【0010】この構成によれば、嫌気性菌による分解処
理を一層高い効率で行うことかできると共に、加熱手段
により被処理物の粘度を低くして流動性を高めることが
できるので都合がよい。攪拌機構としては、嫌気発酵槽
内に攪拌棒などを配置して、これをゆっくり回転させる
方式などを採用することができる。又、加熱手段として
は、嫌気発酵槽の外側あるいは内側に温調可能なジャケ
ットを設けたり、ヒータ線を配設したり、種々の方式の
加熱手段を採用可能である。嫌気性菌の場合、加熱は5
0〜60℃程度が好ましい。
According to this structure, the decomposition treatment by the anaerobic bacterium can be performed with higher efficiency, and the viscosity of the object to be treated can be reduced by the heating means to improve the fluidity, which is convenient. As a stirring mechanism, a method of disposing a stirring rod or the like in an anaerobic fermenter and slowly rotating the stirring rod can be adopted. Further, as the heating means, a temperature-controllable jacket may be provided outside or inside the anaerobic fermenter, a heater wire may be provided, or various types of heating means may be employed. In the case of anaerobic bacteria, heating is 5
About 0 to 60 ° C. is preferable.

【0011】更に、本発明に係る嫌気発酵システムの特
徴構成は、請求項1又は2の嫌気発酵槽と、この嫌気発
酵槽へ被処理物を投入する投入手段と、投入された被処
理物を前記嫌気発酵槽内の入口側から出口側に向けて送
給する送給手段と、発酵処理された被処理物から排出す
るバイオガスを貯留する貯留槽と、この貯留槽からのバ
イオガスを取り出して燃焼する装置と、嫌気発酵された
被処理物を排出する回収手段と、を有することにある。
Further, the anaerobic fermentation system according to the present invention is characterized in that the anaerobic fermenter according to claim 1 or 2, an input means for inputting an object to the anaerobic fermenter, Feeding means for feeding from the inlet side to the outlet side in the anaerobic fermentation tank, a storage tank for storing biogas discharged from the fermented processed object, and taking out biogas from this storage tank And a recovery means for discharging the anaerobic fermented object.

【0012】この構成によれば、周囲環境に不快な臭気
を飛散させることのない嫌気性発酵ガスを、低い処理コ
ストで得られると共に、発酵処理により生じるバイオガ
スを燃料などに有効利用できる嫌気発酵システムを提供
することができる。
According to this configuration, an anaerobic fermentation gas which does not disperse an unpleasant odor to the surrounding environment can be obtained at a low processing cost, and an anaerobic fermentation gas in which biogas generated by the fermentation treatment can be effectively used as a fuel or the like. A system can be provided.

【0013】更に又、本発明に係る嫌気発酵方法の特徴
構成は、請求項1又は2の嫌気発酵槽に嫌気性菌を投入
し、この嫌気性菌を固定床で培養し、被処理物を前記嫌
気発酵槽内に投入し、投入された被処理物を押出しつつ
嫌気発酵させることにある。
Furthermore, a characteristic configuration of the anaerobic fermentation method according to the present invention is that an anaerobic bacterium is charged into the anaerobic fermenter according to claim 1 or 2, and the anaerobic bacterium is cultured on a fixed bed, and The anaerobic fermentation tank is charged into the anaerobic fermenter, and the anaerobic fermentation is performed while extruding the charged object.

【0014】この構成によれば、前処理を必要とする副
資材を処理の都度用いる必要がないので、処理コストを
低くすることができ、しかも固定床に嫌気性菌を培養す
ることにより、処理能力を十分高く維持することができ
て、安価に嫌気性発酵ガスが得られる嫌気発酵方法を提
供することができる。尚、嫌気発酵槽への嫌気性菌の投
入は、嫌気性菌を含む汚泥などを投入すればよく、嫌気
性菌のみを投入する必要は必ずしもない。
According to this configuration, it is not necessary to use the auxiliary material requiring the pretreatment every time the treatment is performed, so that the treatment cost can be reduced and the anaerobic bacterium is cultured on the fixed bed. It is possible to provide an anaerobic fermentation method capable of maintaining a sufficiently high capacity and inexpensively obtaining an anaerobic fermentation gas. The anaerobic bacteria may be introduced into the anaerobic fermenter only by introducing sludge containing anaerobic bacteria, and it is not always necessary to introduce only anaerobic bacteria.

【0015】前記嫌気発酵槽内で被処理物を嫌気発酵さ
せる際に、嫌気性菌の繁殖を促進可能に前記嫌気発酵槽
内を加熱すると共に、前記被処理物を緩速度で攪拌する
ことが好ましい。
In the anaerobic fermentation of the object to be treated in the anaerobic fermenter, the inside of the anaerobic fermenter is heated and the object is stirred at a slow speed so as to promote the propagation of anaerobic bacteria. preferable.

【0016】この構成によれば、嫌気性菌による分解処
理を一層高い効率で行うことかできて都合がよい。
According to this configuration, the decomposition treatment by the anaerobic bacteria can be performed with higher efficiency, which is convenient.

【0017】[0017]

【発明の実施の形態】本発明の実施の形態を、図面を参
照して詳細に説明する。図1は、本実施形態に係る嫌気
発酵槽1と、これに接続された被処理物貯留ホッパー8
と被処理物送給手段7などを備えた嫌気発酵システムの
概略全体構成を示す。
Embodiments of the present invention will be described in detail with reference to the drawings. FIG. 1 shows an anaerobic fermenter 1 according to the present embodiment and an object storage hopper 8 connected thereto.
FIG. 1 shows a schematic overall configuration of an anaerobic fermentation system including a processing object feeding unit 7 and the like.

【0018】生ゴミ、汚泥、畜糞などの被処理物Aは、
一旦ホッパー8に集められ、この内、所定量の被処理物
Aを混合室9に投入し、ここで十分混合される。次に、
混合室9に続くバルブ12を開放すると共に、嫌気発酵
槽1の入口側のバルブ13を閉鎖した状態で、被処理物
送給手段である送給ポンプ7に内蔵されて緩速度で押引
可能な油圧式プラグ7aを引いて吸引状態にすると、混
合された被処理物Aは嫌気発酵槽1の入口側に向けて送
り込まれる。その後、バルブ12を閉鎖すると共にバル
ブ13を開放して、送給ポンプ7のプラグ7aを逆に押
す方向に移動させると、被処理物Aは嫌気発酵槽1の入
口に向けて、徐々に押し出される。
The object A to be treated, such as garbage, sludge, animal dung,
Once collected in the hopper 8, a predetermined amount of the object to be treated A is put into the mixing chamber 9, and is sufficiently mixed therein. next,
The valve 12 connected to the mixing chamber 9 is opened, and the valve 13 on the inlet side of the anaerobic fermenter 1 is closed. When the appropriate hydraulic plug 7a is pulled to a suction state, the mixed object A is fed toward the inlet side of the anaerobic fermenter 1. Thereafter, when the valve 12 is closed and the valve 13 is opened, and the plug 7a of the feed pump 7 is moved in the direction in which the feed pump 7 is pushed in the reverse direction, the object A is gradually pushed out toward the inlet of the anaerobic fermenter 1. It is.

【0019】嫌気発酵槽1の入口側の開口部5から導入
された被処理物Aは、送給ポンプ7のプラグ7aの押し
動作により、ゆっくりと嫌気発酵槽1内の固定床4を経
由して出口6に向けて押されてゆく。
The object A introduced from the opening 5 on the inlet side of the anaerobic fermenter 1 slowly passes through the fixed bed 4 in the anaerobic fermenter 1 by the pressing operation of the plug 7a of the feed pump 7. And it is pushed toward exit 6.

【0020】この嫌気発酵槽1は、密封された横型円筒
状になっていて、内部に、軸2周りに回動可能な複数の
攪拌棒3からなる攪拌機構と、これら攪拌棒3の間に円
周方向に配置されている固定床4とが配設されている。
そして、嫌気発酵槽1の後端側には処理した被処理物A
を排出する出口6が形成されていて、更に出口6の下流
側には、供給ポンプ7と同様な機能を有し、内部に油圧
式プラグ15aを備えた排出戻しポンプ15が接続され
ていて、処理済みの被処理物を排出するようになってい
る。
The anaerobic fermenter 1 has a sealed horizontal cylindrical shape and includes therein a stirring mechanism including a plurality of stirring rods 3 rotatable around an axis 2. A fixed floor 4 arranged in the circumferential direction is provided.
Then, the treated object A is disposed on the rear end side of the anaerobic fermenter 1.
An outlet 6 for discharging water is formed, and a discharge return pump 15 having a function similar to that of the supply pump 7 and having a hydraulic plug 15a therein is connected downstream of the outlet 6. The processed object is discharged.

【0021】嫌気発酵槽1中に配置されている固定床4
の構造は、特に限定されるものではないが、例えば、ハ
ニカム形状をしていて、嫌気性菌が付着し繁殖しやすい
ようになっていることが好ましい。更に、嫌気発酵槽1
の外周には嫌気性菌が繁殖し易いように、例えば、槽内
を50〜60℃に加熱可能な温水ジャケット10が円周
状に配置されている。この温水ジャケットには、図示は
しないが、貯水槽より温度制御され所定温度に加熱され
た所定量の水を循環させるようにすることができる。
Fixed bed 4 arranged in anaerobic fermenter 1
The structure is not particularly limited, but is preferably, for example, in a honeycomb shape so that an anaerobic bacterium can be attached and easily propagated. Furthermore, anaerobic fermenter 1
For example, a warm water jacket 10 capable of heating the inside of the tank to 50 to 60 ° C. is circumferentially arranged on the outer periphery of the container so that anaerobic bacteria can easily propagate. Although not shown, a predetermined amount of water heated to a predetermined temperature controlled by a water storage tank can be circulated in the warm water jacket.

【0022】嫌気発酵槽1の入口側には、被処理物Aを
所定温度に保持する熱交換器Eが設けられていて、被処
理物Aを嫌気発酵させるに適した温度に保持しつつ、嫌
気発酵槽1に導入するようになっている。この熱交換器
Eは必ずしも必要ではないが、このように嫌気発酵槽1
に被処理物を導入する前に被処理物を所定温度に保持す
るようにすると、嫌気発酵槽1での嫌気性菌を一層活性
にできて好ましい。
At the inlet side of the anaerobic fermenter 1, a heat exchanger E for holding the object A at a predetermined temperature is provided, and while maintaining the object A at a temperature suitable for anaerobic fermentation, The anaerobic fermenter 1 is introduced. Although this heat exchanger E is not always necessary, the anaerobic fermenter 1
It is preferable to keep the object at a predetermined temperature before introducing the object into the anaerobic fermenter 1 because the anaerobic bacteria in the anaerobic fermenter 1 can be further activated.

【0023】嫌気発酵槽1の出口側上部には、槽内で発
生したメタン等のバイオガスを取り出す排出口11が設
けられていて、バイオガス貯留槽(図示略)に送給され
るようになっている。このように発生したバイオガス
は、発電用など各種燃料に利用される。もとより、温水
ジャケットに送給する温水を作成する燃料としても利用
できる。
At the upper part of the outlet side of the anaerobic fermentation tank 1, there is provided a discharge port 11 for taking out biogas such as methane generated in the tank, so as to be supplied to a biogas storage tank (not shown). Has become. The biogas generated in this way is used for various fuels such as for power generation. Of course, it can also be used as fuel to create hot water to be sent to the hot water jacket.

【0024】排出戻しポンプ15の吸引とそれに続く押
出動作により、嫌気発酵槽1の出口6から排出される処
理済みの被処理物は、脱水装置14を経て回収手段であ
る回収槽(図示略)に貯留され、肥料として利用され
る。
The treated object discharged from the outlet 6 of the anaerobic fermenter 1 by the suction of the discharge return pump 15 and the subsequent extruding operation passes through the dehydrator 14 and is a recovery tank (not shown) as a recovery means. And stored as fertilizer.

【0025】処理済みの被処理物Aの一部は、再度嫌気
発酵槽1に導入するようにしてもよい。このような処理
済みの被処理物Aには、嫌気性菌が多数繁殖して含まれ
ているので、これを嫌気発酵槽1に導入することによ
り、嫌気発酵を効率よく行わせることができて都合がよ
いからである。尚、図番16,17,18は処理済み被
処理物の排出量を制御可能なバルブである。
A part of the processed object A may be introduced again into the anaerobic fermenter 1. Since a large number of anaerobic bacteria are propagated and contained in the treated object A, the anaerobic fermentation can be efficiently performed by introducing the anaerobic bacteria into the anaerobic fermenter 1. This is because it is convenient. Reference numerals 16, 17, and 18 denote valves capable of controlling the discharge amount of the processed workpiece.

【0026】[0026]

【実施例】長さ18m、直径3mの円筒状の横型発酵槽
に、予め汚泥を槽内深さ1/4程度にまで投入してお
き、攪拌することにより、汚泥中に含まれている嫌気性
菌を固定床で培養してから、入口側より所定量の生ゴミ
を投入した。その後、攪拌しつつ被処理物をプラグで押
し込むことにより処理した。攪拌は、攪拌棒を約6分/
回程度の緩速度で回転させた。この場合、発酵槽の外周
に設けた温水ジャケットにより、発酵槽内部を約55℃
に加熱した。このようにして、約3t/日の処理をする
ことができた。これらの堆肥に、有機臭は認められなか
った。又、バイオガスは、約300m3 (Norma
l)/日得られた。
EXAMPLE Sludge was previously poured into a cylindrical horizontal fermentation tank having a length of 18 m and a diameter of 3 m to a depth of about 1/4 in the tank, and the mixture was stirred. After the bacterium was cultured on the fixed bed, a predetermined amount of garbage was introduced from the inlet side. Thereafter, the object was processed by pushing in the object with a plug while stirring. Stirring is performed with a stirring rod for about 6 minutes /
It was rotated at a slow speed of about once. In this case, the inside of the fermenter is heated to about 55 ° C. by a warm water jacket provided on the outer periphery of the fermenter.
Heated. In this way, about 3 t / day processing could be performed. No organic odor was found in these composts. Biogas is about 300 m 3 (Norma
l) / day.

【0027】〔別実施の形態〕 (1)嫌気発酵槽の形状は、円筒状だけでなく、半円筒
状(略かまぼこ形)などであってもよい。
[Another Embodiment] (1) The shape of the anaerobic fermenter is not limited to a cylindrical shape, but may be a semi-cylindrical shape (substantially kamaboko shape).

【0028】(2)被処理物は、生ゴミに以外に、鶏
糞、牛糞などの各種畜糞、更に、浄水場や下水処理場で
発生する汚泥、産業廃水処理汚泥、埋め立て廃水処理汚
泥、し尿処理汚泥など、水分を比較的多く含む汚れた泥
状物質を含めることができる。
(2) In addition to raw garbage, objects to be treated include various animal dung such as chicken dung and cow dung, sludge generated at water purification plants and sewage treatment plants, industrial wastewater treatment sludge, landfill wastewater treatment sludge, and human waste treatment. Dirty mud containing relatively high water content, such as sludge, can be included.

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

【図1】本発明に係る嫌気発酵システムの一実施形態を
表す概略構成図
FIG. 1 is a schematic configuration diagram showing an embodiment of an anaerobic fermentation system according to the present invention.

【符号の説明】[Explanation of symbols]

1 発酵槽 3 攪拌機構 4 固定床 7 被処理物送給手段 10 加熱手段 A 被処理物 DESCRIPTION OF SYMBOLS 1 Fermenter 3 Stirring mechanism 4 Fixed bed 7 Processing object feeding means 10 Heating means A Processing object

───────────────────────────────────────────────────── フロントページの続き (72)発明者 片岡 静夫 兵庫県尼崎市金楽寺町2丁目2番33号 株 式会社タクマ内 Fターム(参考) 4D004 AA02 AA03 BA03 BA04 CA15 CA18 CA22 CA48 CB04 CB28 CB31 CB42 CB43 CC08 DA02 DA06 DA13 4D059 AA01 AA03 AA07 BA17 BA41 BA48 BA56 BJ03 CB11 CC01 EB06 EB16  ────────────────────────────────────────────────── ─── Continuing from the front page (72) Inventor Shizuo Kataoka 2-33, Kinrakuji-cho, Amagasaki-shi, Hyogo F-term in Takuma Co., Ltd. (Reference) 4D004 AA02 AA03 BA03 BA04 CA15 CA18 CA22 CA48 CB04 CB28 CB31 CB42 CB43 CC08 DA02 DA06 DA13 4D059 AA01 AA03 AA07 BA17 BA41 BA48 BA56 BJ03 CB11 CC01 EB06 EB16

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 密封して嫌気発酵処理可能な横型の発酵
槽であって、この発酵槽内部に挿入されて嫌気性菌を保
持可能な固定床を備え、前記発酵槽内の入口側から出口
側に向けて被処理物を送給する送給手段と接続可能にな
っている嫌気発酵槽。
1. A horizontal fermenter capable of performing anaerobic fermentation treatment in a hermetically sealed manner, comprising a fixed bed inserted into the fermenter and capable of holding anaerobic bacteria. An anaerobic fermenter that can be connected to a feeding means that feeds the object toward the side.
【請求項2】 前記発酵槽に、投入された被処理物を緩
速度で攪拌可能な攪拌機構と、嫌気性菌の繁殖を促進可
能にする加熱手段とが設けられている請求項1の嫌気発
酵槽。
2. The anaerobic apparatus according to claim 1, wherein the fermenter is provided with a stirring mechanism capable of stirring the thrown object at a slow speed and a heating means capable of promoting the propagation of anaerobic bacteria. Fermenter.
【請求項3】 請求項1又は2の嫌気発酵槽と、この嫌
気発酵槽へ被処理物を投入する投入手段と、投入された
被処理物を前記嫌気発酵槽内の入口側から出口側に向け
て送給する送給手段と、発酵処理された被処理物から排
出するバイオガスを貯留する貯留槽と、この貯留槽から
のバイオガスを取り出して燃焼する装置と、嫌気発酵さ
れた被処理物を排出する回収手段と、を有する嫌気発酵
システム。
3. An anaerobic fermenter according to claim 1 or 2, an input means for inputting an object to be processed into the anaerobic fermenter, and the input object being supplied from the inlet side to the outlet side in the anaerobic fermenter. Feeding means for feeding toward the target, a storage tank for storing biogas discharged from the fermented processing target, a device for extracting and burning the biogas from the storage tank, and an anaerobic fermented processing target. An anaerobic fermentation system comprising: a collection unit that discharges a substance.
【請求項4】 請求項1又は2の嫌気発酵槽に嫌気性菌
を投入し、この嫌気性菌を固定床で培養し、被処理物を
前記嫌気発酵槽内に投入し、投入された被処理物を押出
しつつ嫌気発酵させる嫌気発酵方法。
4. An anaerobic bacterium is charged into the anaerobic fermenter according to claim 1 or 2, and the anaerobic bacterium is cultured on a fixed bed. Anaerobic fermentation method for anaerobic fermentation while extruding processed material.
【請求項5】 前記嫌気発酵槽内で被処理物を嫌気発酵
させる際に、嫌気性菌の繁殖を促進可能に前記嫌気発酵
槽内を加熱すると共に、前記被処理物を緩速度で攪拌す
る請求項4の嫌気発酵方法。
5. When anaerobic fermentation of an object in the anaerobic fermenter is performed, the anaerobic fermenter is heated and the object is stirred at a slow speed so as to promote the growth of anaerobic bacteria. An anaerobic fermentation method according to claim 4.
JP2000360990A 2000-11-28 2000-11-28 Anaerobic fermentation tank, anaerobic fermentation system and anaerobic fermentation method Pending JP2002159946A (en)

Priority Applications (1)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000360990A JP2002159946A (en) 2000-11-28 2000-11-28 Anaerobic fermentation tank, anaerobic fermentation system and anaerobic fermentation method

Publications (1)

Publication Number Publication Date
JP2002159946A true JP2002159946A (en) 2002-06-04

Family

ID=18832493

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2002159946A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014176784A (en) * 2013-03-13 2014-09-25 Zukosha:Kk Methane fermentation system
JP2021020152A (en) * 2019-07-26 2021-02-18 株式会社インターファーム Methane fermentation method of poultry manure, and production method of poultry manure fertilizer
CN114164085A (en) * 2021-12-01 2022-03-11 上海坚蚕环境科技有限公司 Anaerobic and aerobic combined fermentation process system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014176784A (en) * 2013-03-13 2014-09-25 Zukosha:Kk Methane fermentation system
JP2021020152A (en) * 2019-07-26 2021-02-18 株式会社インターファーム Methane fermentation method of poultry manure, and production method of poultry manure fertilizer
JP7180881B2 (en) 2019-07-26 2022-11-30 株式会社インターファーム Method for methane fermentation of poultry manure and method for producing poultry manure fertilizer
CN114164085A (en) * 2021-12-01 2022-03-11 上海坚蚕环境科技有限公司 Anaerobic and aerobic combined fermentation process system

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