JPH0523700A - Methane fermenter - Google Patents

Methane fermenter

Info

Publication number
JPH0523700A
JPH0523700A JP3205731A JP20573191A JPH0523700A JP H0523700 A JPH0523700 A JP H0523700A JP 3205731 A JP3205731 A JP 3205731A JP 20573191 A JP20573191 A JP 20573191A JP H0523700 A JPH0523700 A JP H0523700A
Authority
JP
Japan
Prior art keywords
tank
liquid
fermentation tank
section
methane
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
JP3205731A
Other languages
Japanese (ja)
Other versions
JPH0775716B2 (en
Inventor
Hidehiko Takahata
英彦 高畑
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.)
Nippon Beet Sugar Manufacturing Co Ltd
Original Assignee
Nippon Beet Sugar 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 Nippon Beet Sugar Manufacturing Co Ltd filed Critical Nippon Beet Sugar Manufacturing Co Ltd
Priority to JP20573191A priority Critical patent/JPH0775716B2/en
Publication of JPH0523700A publication Critical patent/JPH0523700A/en
Publication of JPH0775716B2 publication Critical patent/JPH0775716B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

PURPOSE:To provide a methane fermenter easy to operate which is used to treat a waste liq. rich in org. components such as livestock waste liq., industrial waste liq. and night soil. CONSTITUTION:A methane fermenter 1 is divided into plural sections 6, 7, 8 and 9, pipes 20, 21 and 22 are provided to transfer a liq. to be treated from the working level position of the succeeding section in the flow direction F of the liq. to the position of the preceding section close to the bottom face, and a rotary gate valve 13 for discharging sludge is furnished to the collecting parts of the sections 6, 7, 8 and 9.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は,畜産廃液、工場廃
液、屎尿廃液等の有機成分の高い廃液を処理するメタン
発酵槽に係り、特に一つの発酵槽を隔壁で複数の区分に
分割した構造のメタン発酵槽に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a methane fermentation tank for treating waste liquid having a high organic content such as a livestock waste liquid, a factory waste liquid, and a human waste liquid, and particularly a structure in which one fermentation tank is divided into a plurality of sections by partition walls. Of the methane fermenter.

【0002】[0002]

【従来の技術】メタン発酵などのように嫌気性細菌を利
用して廃液中の有機成分を分解処理する廃液の嫌気性処
理方法は、活性汚泥処理法のようにエアレションのため
の動力を必要としないこと、汚泥の生成量が少ないこと
から運転費が廉価であり、加えて有機物の生分解により
可利用バイオガスが生ずること、などの利点を有するこ
とから、近年畜産廃液、工場廃液、屎尿廃液等の処理に
多く採用されている。特開昭60−78700号公報に
は排出管を介して順次配列される発酵槽を槽底に接しな
いバッフルで二つの帯域に分割し、各槽に流入する被処
理液をバッフルの下方を回動させて流動させ、各帯域を
液体−固体混合物を実質上静止状態又は非攪乱状態に置
いて処理するメタン発酵槽が開示されている。
2. Description of the Related Art An anaerobic treatment method for waste liquid, which decomposes organic components in the waste liquid by utilizing anaerobic bacteria such as methane fermentation, requires power for aeration like the activated sludge treatment method. In addition, the operating cost is low because it does not produce sludge and the biodegradation of organic matter produces usable biogas.In addition, in recent years, livestock effluent, factory effluent, and human waste effluent have been obtained. It is often used for processing such as. In JP-A-60-78700, a fermentation tank sequentially arranged through a discharge pipe is divided into two zones by a baffle that does not contact the tank bottom, and a liquid to be treated flowing into each tank is passed under the baffle. Disclosed is a methane fermentor which is moved to flow and each zone treated with a liquid-solid mixture in a substantially static or undisturbed state.

【0003】[0003]

【発明が解決しようとする課題】上記、特開昭60−7
8700号公報に開示するメタン発酵槽は、発酵槽内を
槽下底に接しないバッフルにより二つの帯域に分割した
ことにより、各槽に流入する被処理液が各帯域に形成す
る液体−固体混合物の層を確実に通過するように仕向け
るが、このシステムのメタン発酵槽にあっては、液体−
固体混合物の層を静止状態又は非攪乱状態に維持するこ
とが必須条件とされている。かように、液体−固体混合
物の層を静止状態又は非攪乱状態特に非攪乱状態に維持
しながら運転することは実際に困難で、例えば流入する
被処理液が気泡を抱く場合には容易に静止状態が破られ
ることになる。このため、この種処理装置の、より運転
の容易な設備の開発が望まれている。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
In the methane fermentation tank disclosed in Japanese Patent No. 8700, a liquid-solid mixture formed in each zone by a liquid to be treated flowing into each tank by dividing the inside of the fermentation tank into two zones by a baffle that does not contact the bottom of the vessel. To ensure that it passes through the layer of
It is a prerequisite that the layer of solid mixture is kept static or undisturbed. As described above, it is actually difficult to operate the liquid-solid mixture layer while maintaining a static state or an undisturbed state, in particular, an undisturbed state, for example, when the inflowing liquid to be treated contains bubbles, it is easily stopped. The state will be broken. For this reason, it is desired to develop a facility of this kind of processing device that is easier to operate.

【0004】[0004]

【課題を解決するための手段】この発明は、上記事情か
らなされたもので、酸発酵槽を前処理槽として別に設け
る循環装置を持つメタン発酵槽において、発酵槽を複数
の隔壁により複数の区分に分割し、被処理液の流れ方向
後方区分の上部から前方区分の下部に向けて移送管を配
設したことを特徴とするものであり、さらに、前記複数
の隔壁の集合部に回転式ゲ−トバルブを配したことを特
徴とするものであり、この回転式ゲ−トバルブを外円筒
と、これに回転自在に嵌入する内円筒から構成し、外円
筒の下部筒壁には前記複数の区分の個数に対応する開口
を設け、内円筒の筒壁下部には上記外円筒の下部筒壁の
開口に連通する1個の開口を設けた特徴ある構造とする
ことにより、運転の容易なメタン発酵槽を完成したもの
である。以下、図面の実施例により、この発明を詳細に
説明する。
The present invention has been made in view of the above circumstances, and in a methane fermentation tank having a circulation device separately provided as an acid fermentation tank as a pretreatment tank, the fermentation tank is divided into a plurality of sections by a plurality of partition walls. And a transfer pipe is arranged from the upper part of the rear section to the lower part of the front section in the flow direction of the liquid to be treated, and the rotary gate is further provided at the collecting portion of the plurality of partition walls. -A rotary valve is arranged, and the rotary gate valve is composed of an outer cylinder and an inner cylinder rotatably fitted therein, and the lower cylinder wall of the outer cylinder has the plurality of sections. A methane fermentation that is easy to operate by providing openings corresponding to the number of the above, and one opening communicating with the opening of the lower cylinder wall of the outer cylinder at the bottom of the cylinder wall of the inner cylinder. The tank is completed. Hereinafter, the present invention will be described in detail with reference to the embodiments of the drawings.

【0005】[0005]

【実施例】図に示す例は、直線部が円筒形で、底面が中
心部に向けて傾斜する円形型メタン発酵槽の場合である
が、この例に制限されない。図1は、この発明のメタン
発酵槽の説明を容易とするために、天板部の記載を省略
して要部を示す平面図であり、図2は図1のA−A線断
面図である。図において、1は槽本体で、円筒形側壁2
と傾斜状底面3からなり、傾斜状底面3のセンタ−下部
にはピット4がある。5a、5b、5cおよび5dはそ
れぞれ隔壁で、槽1の内部空間を縦方向の4個の区分
6、7、8および9に分割する(但し4個の区分に分割
する例)。隔壁5a、5b、5cおよび5dの外側部1
0と底部11は、それぞれ槽1の円筒形側壁2と傾斜状
底面3に固着し、内側部12のそれぞれは、槽1の中央
部に固定する回転式ゲ−トバルブ13に固着して、前記
区分6、7、8および9を互いに連通しない独立区分と
する。
EXAMPLE The example shown in the drawing is a case of a circular methane fermentation tank in which the linear portion is cylindrical and the bottom surface is inclined toward the center, but the invention is not limited to this example. FIG. 1 is a plan view showing an essential part of the methane fermentation tank of the present invention with the description of the top plate omitted, for ease of explanation, and FIG. 2 is a sectional view taken along line AA of FIG. is there. In the figure, 1 is a tank body, and a cylindrical side wall 2
And a pit 4 at the lower center of the sloping bottom surface 3. 5a, 5b, 5c and 5d are partition walls, respectively, which divide the internal space of the tank 1 into four vertical sections 6, 7, 8 and 9 (however, an example of dividing into four sections). Outer part 1 of partition walls 5a, 5b, 5c and 5d
0 and the bottom 11 are fixed to the cylindrical side wall 2 and the inclined bottom surface 3 of the tank 1, respectively, and the inner portions 12 are fixed to the rotary gate valve 13 fixed to the central portion of the tank 1, respectively. The sections 6, 7, 8 and 9 are independent sections that do not communicate with each other.

【0006】回転式ゲ−トバルブ13は、図4に示すよ
うに、外円筒14と、これに回転自在に嵌入する内円筒
15からなり、外円筒14の下方筒壁には前記区分6、
7、8および9のそれぞれに対応する位置に開口16が
あり、内円筒15の下方筒壁には1個の開口17が設け
られていて、内円筒15の開口17が外円筒14の開口
16のいずれかに一致するとき互いに連通し、この場
合、開口の連通に関与しない外円筒14の他の開口16
は内円筒15の円筒壁により閉塞される。また、外円筒
14と内円筒15の軸方向の下部は互いに開口されてい
て、内円筒15の開口17と外円筒14の開口16が連
通口となるとき、この連通口を介して、連通口が対応す
る区分からピット4に向けて流路が形成し、内円筒15
の開口17が外円筒14の開口16のいずれとも連通し
ないときには、このピット4に向けて流路形成が遮断さ
れる。15aは、内円筒15の回転操作用バ−を示す。
As shown in FIG. 4, the rotary gate valve 13 is composed of an outer cylinder 14 and an inner cylinder 15 which is rotatably fitted therein.
There is an opening 16 at a position corresponding to each of 7, 8 and 9, and one opening 17 is provided in the lower cylinder wall of the inner cylinder 15, and the opening 17 of the inner cylinder 15 is the opening 16 of the outer cylinder 14. The other openings 16 of the outer cylinder 14 which are in communication with each other when they match any of the
Is closed by the cylindrical wall of the inner cylinder 15. Also, the lower portions of the outer cylinder 14 and the inner cylinder 15 in the axial direction are opened to each other, and when the opening 17 of the inner cylinder 15 and the opening 16 of the outer cylinder 14 serve as a communication port, the communication port is communicated through this communication port. A flow path is formed from the corresponding section to the pit 4, and the inner cylinder 15
When the opening 17 is not communicated with any of the openings 16 of the outer cylinder 14, the flow passage formation is blocked toward the pit 4. Reference numeral 15a indicates a bar for rotating the inner cylinder 15.

【0007】18は、別に設ける酸発酵槽19からの酸
発酵液を槽1に導入する導入管で、入液側18aを槽1
内作業液面Lよりも高くし、出液側18bを槽1の中心
部底面に近接するように傾斜状にして槽1の区分6に設
けられる。20、21および22は移送管で、流入側2
0a、21aよび22aを、図3の部分図に示すよう
に、隔壁5a(5b、5c)の外側部10に被処理液の
流れ方向Fに張り出る移送棚23(24、25)の開口
23a(24a、25a)にそれぞれ固着し、流出側2
0b(21b、22b)はそれぞれ槽1の底面3中心部
に近接するように傾斜状にとして設ける 26は排出管で、前記独立区分の最終区分(例では区分
6)の槽1の作業液面L位置の開口部(図示しない)に
一側を接続し、他側を作業液面Lより低位置として固−
液分離槽27に接続する。
Reference numeral 18 is an introduction pipe for introducing the acid fermentation liquor from a separately provided acid fermentation liquor 19 into the liquor 1, and the liquor side 18a is placed in the liquor 1
It is provided in the section 6 of the tank 1 so as to be higher than the inner working liquid level L, and the liquid outlet side 18 b is inclined so as to be close to the bottom surface of the central portion of the tank 1. Transfer pipes 20, 21 and 22 are provided on the inflow side 2
As shown in the partial view of FIG. 3, the openings 0a, 21a and 22a of the transfer rack 23 (24, 25) projecting in the outer direction 10 of the partition wall 5a (5b, 5c) in the flow direction F of the liquid to be treated 23a. (24a, 25a) respectively fixed to the outflow side 2
Reference numeral 0b (21b, 22b) is provided as an inclined shape so as to be close to the center of the bottom surface 3 of the tank 1, and 26 is a discharge pipe, which is the working liquid level of the tank 1 in the final section of the independent section (section 6 in the example). One side is connected to the opening (not shown) at the L position, and the other side is fixed at a position lower than the working liquid level L.
It is connected to the liquid separation tank 27.

【0008】28、29、30および31は揚液壁で、
それぞれ隔壁5d−5a間、5a−5b間、5b−5c
間、および5c−5d間に跨り、前記回転式ゲ−トバル
ブ13を取り囲むようにして設けられる。図の例では、
この揚液壁を円弧形とするが、これに制限されない。3
2は揚液機能を有する翼で、前記回転式ゲ−トバルブ1
3と揚液壁28、29、30および31のそれぞれとの
間に形成する揚液路33の下方部に位置して回転軸34
に固定する。
28, 29, 30 and 31 are pumping walls,
Between partitions 5d-5a, between 5a-5b, 5b-5c, respectively
It is provided so as to surround the rotary gate valve 13 and to extend between 5c-5d. In the example shown,
The pumping wall has an arc shape, but is not limited thereto. Three
Reference numeral 2 denotes a blade having a pumping function, which is the rotary gate valve 1
3 and the pumping walls 28, 29, 30 and 31, respectively, and a rotary shaft 34 located below the pumping passage 33 formed between
Fixed to.

【0009】35は主排出ラインで一側をピット4に接
続し、他側を図示しないスラリ−タンク等の受槽に接続
する。36は固−液分離槽27内に設ける固−液分離装
置で、固−液分離槽27と固−液分離装置36との間に
ポンプを介する供給ライン37を設ける。38は固−液
分離装置36で分離した処理液を受ける受体で、主排出
ライン35との間に放出ライン39を設ける。40は固
−液分離槽27のオ−バ−フロ−・ラインで、放出ライ
ン39に接続する。41、42はそれぞれ酸発酵槽19
および固−液分離槽27の下部を主排出ライン35に接
続するラインである。43は図示しない原液槽の原液を
酸発酵槽19に供給する供給管を示す。44、45、4
6、47および48は仕切弁示す。
A main discharge line 35 has one side connected to the pit 4 and the other side connected to a receiving tank such as a slurry tank (not shown). Reference numeral 36 denotes a solid-liquid separation device provided in the solid-liquid separation tank 27, and a supply line 37 via a pump is provided between the solid-liquid separation tank 27 and the solid-liquid separation device 36. Reference numeral 38 is a receiver for receiving the treatment liquid separated by the solid-liquid separation device 36, and a discharge line 39 is provided between it and the main discharge line 35. An overflow line 40 of the solid-liquid separation tank 27 is connected to the discharge line 39. 41 and 42 are acid fermenters 19 respectively
And a line connecting the lower part of the solid-liquid separation tank 27 to the main discharge line 35. Reference numeral 43 denotes a supply pipe for supplying a stock solution from a stock solution tank (not shown) to the acid fermentation tank 19. 44, 45, 4
6, 47 and 48 are gate valves.

【0010】この発明のメタン発酵槽は、上記のように
構成されていて、導入管18の酸発酵液取出しレベルを
メタン発酵槽1の作業レベルよりも高位に位置させ、メ
タン発酵を終えた処理液を固−液分離槽27に取出す排
出管26の固−液分離槽27側のレベルを、メタン発酵
槽1の作業レベルよりも低位に位置させることにより、
この処理系における液の流動は無動力的になされ、図示
しない原液槽から原液が供給管43により酸発酵槽19
に供給されると、まず原液中の有機質成分は酢酸やプロ
ピオン酸のような簡単な酸に発酵分解される。次いで、
上記酸発酵を受けた被処理液は、出液側18bを槽1の
区分6の底面に近接するようにして設けた導入管18に
より、区分6の底面に強制的に導入される。
The methane fermenter of the present invention is constructed as described above, and the processing for finishing the methane fermentation is performed by setting the acid fermentation liquor withdrawal level of the introduction pipe 18 higher than the working level of the methane fermenter 1. By positioning the level of the discharge pipe 26 for extracting the liquid into the solid-liquid separation tank 27 on the solid-liquid separation tank 27 side to be lower than the working level of the methane fermentation tank 1,
The flow of the liquid in this processing system is made non-powerless, and the raw liquid is supplied from a raw liquid tank (not shown) through the supply pipe 43 to the acid fermentation tank 19.
First, the organic components in the stock solution are fermented and decomposed into simple acids such as acetic acid and propionic acid. Then
The liquid to be treated that has undergone the acid fermentation is forcibly introduced to the bottom surface of the section 6 by the introduction pipe 18 provided so that the liquid outlet side 18b is close to the bottom surface of the section 6 of the tank 1.

【0011】この場合、区分6の底面に近接して、下層
域に揚液路33を設け、その下方部に揚液機能を有する
翼32を回転させて、循環流を形成する(ただし、循環
流の作用が上層部に及ばないように考慮されている)の
で、区分6の下方部に導入された酸発酵液は直ちにこの
循環流に巻き込まれ、揚液路33を循環する間にメタン
発酵菌によりメタン発酵分解をうけることになることか
ら、区分6の下方部に導入された酸発酵液が区分6の表
層部にある既に処理を終えた液へ直接混合することはな
く、区分6の表層部の液は未処理液を含まない処理液と
なる。
In this case, a pumping channel 33 is provided in the lower region in the vicinity of the bottom surface of the section 6, and a blade 32 having a pumping function is rotated below the pumping channel 33 to form a circulation flow (however, circulation is required). Since it is taken into consideration that the effect of the flow does not reach the upper part), the acid fermentation liquor introduced into the lower part of the section 6 is immediately entrained in this circulation flow, and the methane fermentation is performed while circulating the pumping line 33. Since the bacteria undergo methane fermentation decomposition, the acid fermentation liquor introduced in the lower part of Category 6 does not directly mix with the already-treated solution in the surface layer of Category 6, The liquid in the surface layer portion is a treated liquid that does not include the untreated liquid.

【0012】区分6で第1次の処理を終えた表層部の処
理液は、隔壁5aに設けた移送棚23から区分7の底面
近接域に向けて設ける移送管20により区分7の底面近
接域に強制移送され、前記区分6と同様に設ける揚液路
33と翼32が形成する循環流の作用を受けて前記同様
に揚液路33を循環する間に第2次のメタン発酵を受け
る。以下、同様のプロセスで区分8、区分9において第
3次、第4次のメタン発酵を経て十分に処理を終えた処
理液は、区分9の作業液面位置に設けた開口に取り付け
た排出管26により固−液分離槽27に排出される。
The treatment liquid in the surface layer portion which has been subjected to the first treatment in the section 6 is transferred from the transfer rack 23 provided on the partition wall 5a to the bottom area in the bottom section of the section 7 by the transfer pipe 20. And is subjected to the secondary methane fermentation while circulating through the pumping channel 33 in the same manner as described above under the action of the circulation flow formed by the pumping channel 33 and the blade 32 provided similarly to the section 6. Hereinafter, in the same process, the treated liquid that has been sufficiently treated through the third and fourth methane fermentations in Sections 8 and 9 is the discharge pipe attached to the opening provided in the working liquid level position in Section 9. It is discharged to the solid-liquid separation tank 27 by 26.

【0013】固−液分離槽27に排出された最終処理液
は、汚泥等の固形物の混合状況に応じて仕切弁45を閉
じ、供給ライン37を介して最終処理液を固−液分離装
置36に供給して固−液分離を行ない、分離液は受体3
8、排出ライン39を経て主排出ライン35に合流放出
させる。分離した固形物は図示しない適宜手段で系外に
取り出す。一方、汚泥等の混合のない処理液はオ−バ−
フロ−・ラインを経て主排出ライン35に合流放出させ
る。
For the final treatment liquid discharged to the solid-liquid separation tank 27, the sluice valve 45 is closed according to the mixing condition of solid matters such as sludge, and the final treatment liquid is passed through the supply line 37 to separate the final treatment liquid. 36 to carry out solid-liquid separation, and the separated liquid is the receiver 3
8. The combined discharge is carried out to the main discharge line 35 through the discharge line 39. The separated solid matter is taken out of the system by an appropriate means (not shown). On the other hand, the treatment liquid without mixing sludge is over-heated.
The combined discharge is made to the main discharge line 35 through the flow line.

【0014】この発明のメタン発酵槽においては各区分
が集合する中心部に回転式ゲ−トバルブ13を設け、内
円筒15の筒壁下方の1個の開口17と外円筒14の筒
壁下方の開口16(区分の個数、位置に対応する)を回
転一致させるだけのきわめて簡単な操作で、所望の区分
の排泥をさせることができるばかりではなく、任意の区
分の沈降汚泥を取り出し、これを仕切弁45、46およ
び48を閉じ、仕切弁44、47を開けることにより、
酸発酵槽19に供給される原液に接触させてメタン発酵
菌の活性化をはかることなどの操作をきわめて簡単に行
なうことがができる。
In the methane fermentation tank of the present invention, a rotary gate valve 13 is provided at the center where each section is gathered, and one opening 17 below the cylinder wall of the inner cylinder 15 and below the cylinder wall of the outer cylinder 14 is provided. Not only can the sludge of a desired section be discharged by an extremely simple operation of simply rotating and matching the openings 16 (corresponding to the number and position of sections), but the settled sludge of an arbitrary section can be taken out and By closing the gate valves 45, 46 and 48 and opening the gate valves 44, 47,
Operations such as activation of the methane-fermenting bacteria by contact with the stock solution supplied to the acid fermentation tank 19 can be performed very easily.

【0015】[0015]

【発明の効果】この発明のメタン発酵槽によるときは、
メタン発酵槽を複数の区分に分割して多段化したことに
より、装置をコンパクトにすることができ、分割された
複数の区分のそれぞれに流入する被処理液を、その性状
に適した菌相により効果的に発酵処理し、次区分への被
処理液の移送は、当該区分の表層部の処理液を当該前方
区分の底面の近接部に確実に流入せしめて、直ちにメタ
ン発酵菌層と循環接触させるので効率的なメタン発酵、
分解を可能とする。さらに、各区分の排泥を回転式ゲ−
トバルブにより行なうので、所望の区分の排泥操作をき
わめて容易とする。以上多くの利点を有するこの発明の
メタン発酵槽は、各種の有機性廃液のメタン発酵処理装
置として用いて、きわめて有益である。
When the methane fermenter of the present invention is used,
By dividing the methane fermentation tank into multiple sections and making it multi-stage, the device can be made compact, and the liquid to be treated that flows into each of the divided sections can be treated with a flora suitable for its properties. Fermentation is effectively carried out, and the liquid to be treated is transferred to the next section by making sure that the treated solution in the surface layer of the relevant section flows into the vicinity of the bottom of the front section, and immediately in circulation contact with the methane-fermenting bacterial layer. Efficient methane fermentation,
Allows disassembly. In addition, the sludge from each section is
Since it is carried out by a valve, the sludge operation in the desired section can be made extremely easy. The methane fermentation tank of the present invention having many advantages as described above is extremely useful as a methane fermentation treatment apparatus for various organic waste liquids.

【0016】[0016]

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

【図1】この発明のメタン発酵槽の天板部を省略した平
面図である。
FIG. 1 is a plan view of a methane fermentation tank of the present invention in which a top plate portion is omitted.

【図2】図1のA−A線視断面図である。FIG. 2 is a sectional view taken along line AA of FIG.

【図3】この発明を構成する移送管の取付けおよび配置
状態を説明する部分斜視図である。
FIG. 3 is a partial perspective view illustrating a mounting and arrangement state of a transfer pipe that constitutes the present invention.

【図4】この発明を構成する回転式ゲ−トバルブの構造
を説明する分解斜視図である。
FIG. 4 is an exploded perspective view illustrating the structure of the rotary gate valve that constitutes the present invention.

【符合の説明】 1 槽本体 2 円筒形側壁 3 傾斜状底面 4 ピット 5a、5b、5c、5d 隔壁 6、7、8、9 区分 13 回転式ゲ−トバルブ 14 外円筒 15 内円筒 16、17 開口 20、21、22 移送管 23、24、25 移送棚 32 翼 33 揚液路 35 主排出ライン[Explanation of sign] 1 tank body 2 cylindrical side wall 3 inclined bottom 4 pits 5a, 5b, 5c, 5d Partition walls 6, 7, 8, 9 categories 13 rotary gate valve 14 outer cylinder 15 Inner cylinder 16,17 opening 20, 21, 22 transfer pipe 23, 24, 25 Transfer rack 32 wings 33 Pumping channel 35 Main discharge line

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 酸発酵槽を前処理槽として別に設ける循
環装置を持つメタン発酵槽において、発酵槽を複数の隔
壁により複数の区分に分割し、被処理液の流れ方向後方
区分の上部から前方区分の下部に向けて移送管を配設し
たことを特徴とするメタン発酵槽。
1. A methane fermentation tank having a circulation device separately provided as an acid fermentation tank as a pretreatment tank, wherein the fermentation tank is divided into a plurality of sections by a plurality of partition walls, and the flow direction of the liquid to be treated is from the upper part to the front of the rear section. A methane fermenter characterized in that a transfer pipe is arranged toward the bottom of the section.
【請求項2】 酸発酵槽を前処理槽として別に設ける循
環装置を持つメタン発酵槽において、発酵槽を複数の隔
壁により複数の区分に分割し、被処理液の流れ方向後方
区分の上部から前方区分の下部に向けて移送管を配設
し、前記複数の隔壁の集合部に回転式ゲ−トバルブを配
したことを特徴とするメタン発酵槽。
2. A methane fermentation tank having a circulation device separately provided as an acid fermentation tank as a pretreatment tank, wherein the fermentation tank is divided into a plurality of sections by a plurality of partition walls, and the direction of flow of the liquid to be treated is from the top to the front of the rear section. A methane fermentation tank characterized in that a transfer pipe is arranged toward the lower part of the section, and a rotary gate valve is arranged at an assembly portion of the plurality of partition walls.
【請求項3】 回転式ゲ−トバルブが外円筒と、これに
回転自在に嵌入する内円筒からなり、外円筒の下部筒壁
には前記複数の区分の個数に対応する開口があり、内円
筒の筒壁下部には上記外円筒の下部筒壁の開口に連通す
る1個の開口が設けられている構造を特徴とする請求項
2記載のメタン発酵槽。
3. A rotary gate valve comprises an outer cylinder and an inner cylinder rotatably fitted therein, and the lower cylinder wall of the outer cylinder has openings corresponding to the number of the plurality of sections. 3. The methane fermentation tank according to claim 2, wherein the lower part of the cylinder wall is provided with one opening communicating with the opening of the lower cylinder wall of the outer cylinder.
JP20573191A 1991-07-23 1991-07-23 Methane fermentation tank Expired - Fee Related JPH0775716B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20573191A JPH0775716B2 (en) 1991-07-23 1991-07-23 Methane fermentation tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20573191A JPH0775716B2 (en) 1991-07-23 1991-07-23 Methane fermentation tank

Publications (2)

Publication Number Publication Date
JPH0523700A true JPH0523700A (en) 1993-02-02
JPH0775716B2 JPH0775716B2 (en) 1995-08-16

Family

ID=16511739

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20573191A Expired - Fee Related JPH0775716B2 (en) 1991-07-23 1991-07-23 Methane fermentation tank

Country Status (1)

Country Link
JP (1) JPH0775716B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7277551B2 (en) 2003-09-02 2007-10-02 Sony Corporation Sound reproducing apparatus and sound reproducing method
JP2015182002A (en) * 2014-03-24 2015-10-22 株式会社神鋼環境ソリューション Digestion tank, and method of discharging sludge in digestion tank

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5712897A (en) * 1980-06-26 1982-01-22 Tatemi Sonoda Automatic cycling methane gas-collecting apparatus

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5712897A (en) * 1980-06-26 1982-01-22 Tatemi Sonoda Automatic cycling methane gas-collecting apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7277551B2 (en) 2003-09-02 2007-10-02 Sony Corporation Sound reproducing apparatus and sound reproducing method
JP2015182002A (en) * 2014-03-24 2015-10-22 株式会社神鋼環境ソリューション Digestion tank, and method of discharging sludge in digestion tank

Also Published As

Publication number Publication date
JPH0775716B2 (en) 1995-08-16

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