JPH03114594A - Apparatus for treating effluent water - Google Patents

Apparatus for treating effluent water

Info

Publication number
JPH03114594A
JPH03114594A JP1251647A JP25164789A JPH03114594A JP H03114594 A JPH03114594 A JP H03114594A JP 1251647 A JP1251647 A JP 1251647A JP 25164789 A JP25164789 A JP 25164789A JP H03114594 A JPH03114594 A JP H03114594A
Authority
JP
Japan
Prior art keywords
gas
reaction tank
layer
pipe
connecting pipes
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
JP1251647A
Other languages
Japanese (ja)
Inventor
Yoshiaki Arai
喜明 新井
Nobuyuki Wada
信行 和田
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 Corp
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Corp
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 Corp, Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Corp
Priority to JP1251647A priority Critical patent/JPH03114594A/en
Publication of JPH03114594A publication Critical patent/JPH03114594A/en
Pending legal-status Critical Current

Links

Classifications

    • Y02W10/12

Landscapes

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

Abstract

PURPOSE:To smoothly perform treatment reaction by effectively utilizing the whole of the interior of a reaction tank and improving the contact with anaerobic bacteria by a method wherein the interior of the reaction tank is partitioned into a plurality of beds and Venturi tube like connection pipes are formed to the respective beds and barrier plates are arranged above the respective connection pipes. CONSTITUTION:Effluent water (a) to be treated is introduced into a reaction tank 1 at low flow velocity from a effluent water inflow port 9. The flow velocity of the effluent water increases when the effluent water passes through connection pipes 2-1 to 2-4 and the effluent water (a) is sprayed to barrier plates 3-1 to 3-4 by the force thereof and turblent flow is generated in respective beds T1-T4 and the contact with anaerobic bacteria becomes well. As a result, treatment reaction is smoothly performed. At the same time, the sedimentation of the suspended components in the effluent water is accurately advanced. As the treatment advanced, water is discharged from a treated water discharge port 6 as treated water (d) and the suspended components are withdrawn from a drain 10 as sludge (b). The generated gas C is collected by a gas collection pipe 4 and gas collection ports 8-1 to 8-3 and guided to gas piping 7 to be stored in the storage part outside the tank.

Description

【発明の詳細な説明】 A、産業上の利用分野 本発明は、下水処理等に用いる排水処理装置に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION A. Field of Industrial Application The present invention relates to a wastewater treatment device used for sewage treatment and the like.

B 発明の概要 本発明は、下水等を嫌気性処理法によって処理する排水
処理装置において、 反応タンクの内部を複数層に区画し、各層底部にベンチ
ュリ管状の連結管を形成して、最下層の連結管につなが
る排水流入口から最上層の処理水排出口に至る1本の流
通路とするとともに、各連結管の上方に乱流を生じさせ
るための邪魔板を配置することにより、 反応タンクの内部全体を有効に利用し、かつ処理すべき
排水と嫌気性微生物との接触を良好にして、処理反応の
円滑化を図るようにしたものである。
B. Summary of the Invention The present invention provides a wastewater treatment device for treating sewage, etc. by an anaerobic treatment method, in which the inside of a reaction tank is divided into multiple layers, a venturi-like connecting pipe is formed at the bottom of each layer, and the bottom layer is By creating a single flow path from the wastewater inlet connected to the connecting pipe to the treated water outlet on the top layer, and by placing baffles above each connecting pipe to create turbulent flow, the reaction tank The entire interior is used effectively and the wastewater to be treated is brought into good contact with anaerobic microorganisms, thereby facilitating the treatment reaction.

C0従来の技術 近年、嫌気性処理法は、曝気を必要とせず、また、余剰
汚泥の発生も少ないことから、高濃度有機性排水のみな
らず、下水のような低濃度有機性排水に対してもその適
用の範囲が広がろうとしており、多くの研究が活発に行
われている。
C0 Conventional technology In recent years, anaerobic treatment methods have become popular not only for high-concentration organic wastewater but also for low-concentration organic wastewater such as sewage, as they do not require aeration and generate little surplus sludge. The scope of its application is about to expand, and much research is being actively conducted.

下水を嫌気的に処理する場合には、有機物濃度が低いた
めに処理によって発生したメタンのみによって嫌気性処
理に最適な温度条件である35℃程度の温度に反応タン
クを加温することが不可能であったり、低温では嫌気性
細菌の活性が非常に低いために長時間の水理学的滞留時
間を必要とする、といった問題点があるが、嫌気性固定
床、嫌気性流動床、嫌気性汚泥床等を採用し、反応タン
ク内の嫌気性微生物の濃度を高く維持することによって
、比較的短い水理学的滞留時間(HRT)でも、下水の
処理が可能となってきた。
When treating sewage anaerobically, it is impossible to heat the reaction tank to a temperature of around 35°C, which is the optimal temperature condition for anaerobic treatment, using only the methane generated during treatment due to the low concentration of organic matter. anaerobic fixed bed, anaerobic fluidized bed, anaerobic sludge. By adopting a floor or the like and maintaining a high concentration of anaerobic microorganisms in the reaction tank, it has become possible to treat sewage even with a relatively short hydraulic retention time (HRT).

D 発明が解決しようとする課題 しかし、嫌気性固定床等を採用しただけでは、反応タン
ク内全体を有効に利用しているとは言えず、撹拌機によ
りタンク内を撹拌して排水と微生物が良く接触するよう
にしたり、短絡流を防ぐために流入口を数個設置し、排
水を均等に流入させるなど、タンク内全体を有効に利用
できる装置の開発が望まれている。
D Problems to be Solved by the Invention However, simply adopting an anaerobic fixed bed, etc. does not effectively utilize the entire interior of the reaction tank. It is desired to develop a device that can make effective use of the entire inside of the tank, such as by ensuring good contact and installing several inlets to prevent short-circuit flow so that the wastewater flows in evenly.

本発明の目的は、反応タンク内全体を有効に利用できる
排水処理装置を提供することにある。
An object of the present invention is to provide a wastewater treatment device that can effectively utilize the entire inside of a reaction tank.

E0課題を解決するための手段 本発明は、内部を複数層に区画された反応タンクと、こ
の反応タンクの各層の底部にベンチュリ管状に形成され
た複数の連結管と、最下層の連結管につながるように配
設された排水流入口及びドレーンと、最上層の側面上部
に設けられた処理水排出口と、前記各連結管の上方に配
置された複数の乱流発生用邪魔板と、前記反応タンクの
最上層に設置されたガス捕集管と、最上層以外の層の側
面上部に設けられたガス捕集口と、前記ガス捕集管及び
捕集口に接続され、捕集された発生ガスを貯留部に導く
ガス配管とを備えたことを特徴とするものである。
Means for Solving the E0 Problem The present invention provides a reaction tank whose interior is divided into multiple layers, a plurality of connecting pipes formed in the shape of a Venturi tube at the bottom of each layer of this reaction tank, and a connecting pipe in the lowest layer. A waste water inlet and a drain arranged so as to be connected to each other, a treated water outlet provided at the upper side of the uppermost layer, a plurality of baffles for generating turbulent flow arranged above each of the connecting pipes, A gas collection pipe installed on the top layer of the reaction tank, a gas collection port provided on the upper side of the layer other than the top layer, and a gas collection port connected to the gas collection pipe and collection port to collect the gas. The device is characterized in that it includes a gas pipe that guides the generated gas to the storage section.

また、本発明は、内部を複数層に区画された反応タンク
と、この反応タンクの各層の底部にベンチュリ管状に形
成された複数の連結管と、これら各連結管に個々につな
がるように配設された複数の排水流入口及びドレーンと
、最上層の側面上部に設けられた処理水排出口と、前記
各連結管の上方に配置された複数の乱流発生用邪魔板と
、前記反応タンクの最上層に設置されたガス捕集管と、
最上層以外の層の側面上部に設けられたガス捕集口と、
前記ガス捕集管及び捕集口に接続され、捕集された発生
ガスを貯留部に導くガス配管と、前記各ドレーンを結ぶ
循環管と、この循環管に挿設され、引き抜き汚泥の一部
を種汚泥として返送する循環ポンプとを備えたことを特
徴とするものである。
The present invention also provides a reaction tank whose interior is divided into multiple layers, a plurality of connecting pipes formed in the shape of a Venturi tube at the bottom of each layer of the reaction tank, and a plurality of connecting pipes arranged to be individually connected to each of these connecting pipes. a plurality of waste water inlets and drains, a treated water outlet provided on the upper side of the top layer, a plurality of baffles for generating turbulent flow arranged above each of the connecting pipes, and a plurality of baffles for generating turbulence arranged above each of the connecting pipes; A gas collection pipe installed on the top layer,
A gas collection port provided at the upper side of the layer other than the top layer;
A gas pipe that is connected to the gas collection pipe and the collection port and leads the collected generated gas to the storage part, a circulation pipe that connects each of the drains, and a part of the drawn sludge that is inserted into the circulation pipe. The sludge is characterized by being equipped with a circulation pump that returns the sludge as seed sludge.

F3作用 処理すべき排水は小さな流速で反応タンク内に導入され
る。排水の流速は連結管を通過する時に増大し、その勢
いで排水が邪魔板に吹き付けられると、各層に乱流が生
じ、嫌気性微生物との接触が良好になる。この結果、処
理反応が円滑に行われる。同時に、排水中のSS(浮遊
物)成分の沈降が適確に進む。処理が進行すると、水は
最上層の処理水排出口から処理水として排出され、SS
成分は汚泥としてドレーンから引き抜かれる。発生ガス
は、ガス捕集管及び捕集口に捕集され、ガン に ス配管に導かれてタンク外の貯留部に貯留される。
F3 action The wastewater to be treated is introduced into the reaction tank at a small flow rate. The flow velocity of wastewater increases as it passes through the connecting pipe, and when the wastewater is blown against the baffle plate by this force, turbulent flow occurs in each layer, improving contact with anaerobic microorganisms. As a result, the processing reaction is carried out smoothly. At the same time, the sedimentation of SS (suspended solids) components in the wastewater progresses appropriately. As the treatment progresses, water is discharged as treated water from the treated water outlet in the top layer, and the water is discharged as treated water from the SS.
The components are extracted from the drain as sludge. The generated gas is collected in a gas collection pipe and a collection port, guided to a gas pipe to the gun, and stored in a storage section outside the tank.

また、排水の併給が行われた場合は、処理反応が促進さ
れる。この場合、汚泥の返送があると、微生物量が高濃
度となり、処理効率が高くなるとともに、撹拌効果が向
上する。
Furthermore, when wastewater is co-supplied, the treatment reaction is accelerated. In this case, if the sludge is returned, the amount of microorganisms becomes high in concentration, treatment efficiency increases, and the stirring effect improves.

G、実施例 以下、本発明を図面に示す実施例に基づいて詳細に説明
する。
G. Examples Hereinafter, the present invention will be explained in detail based on examples shown in the drawings.

第1図は本発明の一実施例を示すもので、反応タンクI
の内部を複数層、例えばT1〜T4の4層に区画し、各
層の底部中央に連結管2−1〜24を形成している。連
結管2−1〜2−4はベンチュリ管のように管径を細く
しており、各層の上方には排水を吹き付けて乱流を生じ
させるための邪魔板3−f〜3−4を配置している。
FIG. 1 shows an embodiment of the present invention, in which a reaction tank I
The interior is divided into multiple layers, for example, four layers T1 to T4, and connecting pipes 2-1 to 24 are formed at the center of the bottom of each layer. Connecting pipes 2-1 to 2-4 have narrow pipe diameters like venturi pipes, and baffle plates 3-f to 3-4 are arranged above each layer to spray wastewater and create turbulent flow. are doing.

前記反応タンク1の最上層T4には、ガス捕集管4を配
置するとともに、内側面上部に処理水収集樋5を配設し
、この樋の部分に処理水排出口6を設けている。前記ガ
ス捕集管4は、タンクlの外のガス配管7に接続してい
る。また、他の層TI−T3の内側面上部にガス捕集口
8−1〜8−3を設け、これらを前記ガス配管7に接続
している。捕集ガスは貯留するようにしている。
A gas collection pipe 4 is disposed in the uppermost layer T4 of the reaction tank 1, and a treated water collection gutter 5 is disposed at the upper part of the inner surface, and a treated water outlet 6 is provided in this gutter. The gas collection pipe 4 is connected to a gas pipe 7 outside the tank l. Furthermore, gas collection ports 8-1 to 8-3 are provided at the upper part of the inner surface of the other layer TI-T3, and these are connected to the gas pipe 7. The collected gas is stored.

一方、前記反応タンクIの最下層TIの連結管2−1に
は、排水流入口9とドレーンIOを設け、これらにバル
ブ11.12を付設している。
On the other hand, the connecting pipe 2-1 of the lowermost layer TI of the reaction tank I is provided with a waste water inlet 9 and a drain IO, and valves 11 and 12 are attached to these.

排水処理時には、排水&が排水流入口9からタンクl内
に導入される。この時の排水aの流速は小さくする。排
水λは連結管2−1〜2−4を通過する時に流速が増大
し、その勢いで邪魔板31〜3−4に吹き付けられる。
During wastewater treatment, wastewater & is introduced into the tank l from the wastewater inlet 9. At this time, the flow rate of the waste water a is made small. The flow velocity of the wastewater λ increases when it passes through the connecting pipes 2-1 to 2-4, and the momentum causes it to be blown onto the baffle plates 31 to 3-4.

このため、各層TI−T4で乱流が生じ、タンク内の嫌
気性微生物との接触が良好となる。各層で処理されて最
上層T4に達すると、処理水収集樋5に入り、排出口6
から処理水dとして排出される。
Therefore, turbulent flow occurs in each layer TI-T4, which improves contact with anaerobic microorganisms in the tank. After being treated in each layer and reaching the top layer T4, it enters the treated water collection trough 5 and the discharge port 6.
is discharged as treated water d.

一方、排水が反応タンク1内の各層を小さな流速で通過
する時、排水中のSS(浮遊物)分が容易に沈降し、最
下層TIの連結管2−1につなhるドレーン10から引
き抜き汚泥すとして排出される。
On the other hand, when the waste water passes through each layer in the reaction tank 1 at a small flow rate, the SS (suspended solids) in the waste water easily settles and flows from the drain 10 connected to the connecting pipe 2-1 of the lowest layer TI. It is extracted and discharged as sludge.

また、処理過程で発生したガス(メタンガス香は、TI
−T3ではガス捕集口8−1〜8−3力ら捕集され、最
上層T 4のガス捕集管4で集められたガスと共にガス
配管7を流れ、発生ガスCとしてタンク外で貯留される
In addition, the gas (methane gas scent) generated during the treatment process is
- In T3, the gas is collected from the gas collection ports 8-1 to 8-3, flows through the gas pipe 7 together with the gas collected in the gas collection pipe 4 in the uppermost layer T4, and is stored as generated gas C outside the tank. be done.

第2図は本発明の他の実施例を示すもので、前記実施例
と同様に反応タンク1の内部を11〜14層に区画し、
連結管2−1〜2−4を形成して1本の流通路としてい
るが、本実施例では最下層TI以外のT2〜T4層にも
排水と汚泥を直接供給できるようにしている。
FIG. 2 shows another embodiment of the present invention, in which the interior of the reaction tank 1 is divided into 11 to 14 layers as in the previous embodiment.
Although the connecting pipes 2-1 to 2-4 are formed to form one flow path, in this embodiment, wastewater and sludge can be directly supplied to the T2 to T4 layers other than the lowest layer TI.

即ち、TI−T4層の連結管2−1〜2−4に連通ずる
ように排水流入口9−1〜9−4とドレーン10−1〜
10−4を設け、排水流入口91〜9−4はバルブll
−1−11−4を介して共通の排水供給管13に、ドレ
ーン10−1〜l0−4はバルブ12−1〜I2−4を
汚泥循環管14にそれぞれ接続している。そして、汚泥
循環管14には、引き抜き汚泥の一部を循環汚泥eとし
てT2〜T4層に供給するため、循環ポンプ15とバル
ブ16を挿設している。
That is, the drain inlets 9-1 to 9-4 and the drains 10-1 to 10-4 are connected to the connecting pipes 2-1 to 2-4 of the TI-T4 layer.
10-4 is provided, and the drainage inlets 91 to 9-4 are valve ll.
The drains 10-1 to 10-4 connect the valves 12-1 to I2-4 to the sludge circulation pipe 14, respectively, through -1-11-4 to the common waste water supply pipe 13. A circulation pump 15 and a valve 16 are inserted into the sludge circulation pipe 14 in order to supply a portion of the drawn sludge as circulation sludge e to the T2 to T4 layers.

このような構成とすると、上層のT2〜T4層には排水
&が併給されることになり、処理反応の促進が図れる。
With such a configuration, waste water & is fed to the upper T2 to T4 layers, thereby promoting the treatment reaction.

この場合も、各層に乱流が生じ、タンク内の嫌気性微生
物が沈澱することなく、排水と良好に接触する。
In this case as well, turbulent flow occurs in each layer, allowing the anaerobic microorganisms in the tank to make good contact with the waste water without settling.

H0発明の効果 以りのように本発明によれば、反応タンクの内部を複数
層に区画し、各層にベンチュリ管状の連結管を形成して
連通させ、小さな流速で排水を通流させるようにしたの
で、反応タンクの内部全体を有効に利用することができ
る。しかも、排水中のSS成分の除去能力を高め、かつ
短絡流を防止することができる。また、各連結管の上方
に邪魔板を配置して乱流を生じさせるようにしたので、
簡単な構造でタンク内の撹拌を行うことができ、嫌気性
微生物との接触が良好となって処理反応の円滑化が図れ
る。更に、最下層以外にも排水を直接供給したり、引き
抜き汚泥の一部を種汚泥として返送することにより、微
生物量の高濃度化によって処理効率を高めることができ
るとともに、汚泥返送流量の調節によって撹拌効果の一
層の向上が期待できる。
According to the present invention, the interior of the reaction tank is divided into a plurality of layers, and a Venturi-shaped connecting pipe is formed in each layer to communicate with each other, so that wastewater flows at a small flow rate. Therefore, the entire interior of the reaction tank can be used effectively. In addition, it is possible to enhance the ability to remove SS components from wastewater and prevent short circuit currents. Additionally, baffle plates were placed above each connecting pipe to create turbulent flow.
With a simple structure, it is possible to stir the inside of the tank, which improves contact with anaerobic microorganisms and facilitates treatment reactions. Furthermore, by directly supplying wastewater to areas other than the lowest layer, and by returning a portion of the extracted sludge as seed sludge, treatment efficiency can be increased by increasing the concentration of microorganisms, and by adjusting the sludge return flow rate. Further improvement of the stirring effect can be expected.

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

第1図は本発明に係る排水処理装置の一実施例を示す構
成説明図、第2図は本発明の他の実施例を示す構成説明
図である。 1・・・反応タンク、2−1〜2−4・・・連結管、3
−I〜3−4・・・邪魔板、4・・・ガス捕集管、5・
・・処理水収集機、6・・・処理水排出口、7・・・ガ
ス配管、8−1〜8−3・・・ガス捕集口、9.9−1
〜94・・・排水流入口、10.10−1〜10−4・
・・ドレーン、11.11−1〜11−4.12.12
−1〜12−4.16・・・バルブ、15・・・循環ポ
ンプ。 1・・反応タンク 2−1〜2−4・・・連結管 3−1〜3−4 ・邪魔板 4・・ガス捕集管 5・・・処理水収集機 6・・処理水排出口 ア・・ガス配管 8−1〜8−3・・・ガス捕集口 9・・非水流入口 10・・ドーレン 1112・バルブ a・・排水 b・・引抜き汚泥 C・発生ガス d・処理水 第1図 ソ U
FIG. 1 is a structural explanatory diagram showing one embodiment of a wastewater treatment apparatus according to the present invention, and FIG. 2 is a structural explanatory diagram showing another embodiment of the present invention. 1... Reaction tank, 2-1 to 2-4... Connecting pipe, 3
-I~3-4... Baffle plate, 4... Gas collection tube, 5.
... Treated water collector, 6... Treated water outlet, 7... Gas piping, 8-1 to 8-3... Gas collection port, 9.9-1
~94...Drainage inlet, 10.10-1~10-4.
...Drain, 11.11-1 to 11-4.12.12
-1 to 12-4.16...Valve, 15...Circulation pump. 1...Reaction tanks 2-1 to 2-4...Connecting pipes 3-1 to 3-4 -Baffle plate 4...Gas collection pipe 5...Treated water collector 6...Treated water outlet a ... Gas piping 8-1 to 8-3 ... Gas collection port 9 ... Non-water inlet 10 ... Drain 1112 - Valve a - Drainage b - Pulled sludge C - Generated gas d - Treated water No. 1 Figure so U

Claims (2)

【特許請求の範囲】[Claims] (1)内部を複数層に区画された反応タンクと、この反
応タンクの各層の底部にベンチュリ管状に形成された複
数の連結管と、最下層の連結管につながるように配設さ
れた排水流入口及びドレーンと、最上層の側面上部に設
けられた処理水排出口と、前記各連結管の上方に配置さ
れた複数の乱流発生用邪魔板と、前記反応タンクの最上
層に設置されたガス捕集管と、最上層以外の層の側面上
部に設けられたガス捕集口と、前記ガス捕集管及び捕集
口に接続され、捕集された発生ガスを貯留部に導くガス
配管とを備えたことを特徴とする排水処理装置。
(1) A reaction tank whose interior is divided into multiple layers, a plurality of connecting pipes formed in the shape of a Venturi tube at the bottom of each layer of this reaction tank, and a drainage stream arranged to connect to the connecting pipes in the lowest layer. an inlet and a drain, a treated water outlet provided at the upper side of the top layer, a plurality of baffles for generating turbulence placed above each of the connecting pipes, and a plurality of baffles installed in the top layer of the reaction tank. A gas collection pipe, a gas collection port provided on the upper side of the layer other than the top layer, and a gas pipe connected to the gas collection pipe and collection port to guide the collected generated gas to the storage section. A wastewater treatment device characterized by comprising:
(2)内部を複数層に区画された反応タンクと、この反
応タンクの各層の底部にベンチュリ管状に形成された複
数の連結管と、これら各連結管に個々につながるように
配設された複数の排水流入口及びドレーンと、最上層の
側面上部に設けられた処理水排出口と、前記各連結管の
上方に配置された複数の乱流発生用邪魔板と、前記反応
タンクの最上層に設置されたガス捕集管と、最上層以外
の層の側面上部に設けられたガス捕集口と、前記ガス捕
集管及び捕集口に接続され、捕集された発生ガスを貯留
部に導くガス配管と、前記各ドレーンを結ぶ循環管と、
この循環管に挿設され、引き抜き汚泥の一部を種汚泥と
して返送する循環ポンプとを備えたことを特徴とする排
水処理装置。
(2) A reaction tank whose interior is divided into multiple layers, a plurality of connecting pipes formed in the shape of a Venturi tube at the bottom of each layer of this reaction tank, and a plurality of connecting pipes arranged to be individually connected to each of these connecting pipes. a waste water inlet and a drain, a treated water outlet provided on the upper side of the top layer, a plurality of baffles for generating turbulence placed above each of the connecting pipes, and a drain in the top layer of the reaction tank. The installed gas collection pipe, the gas collection port provided on the upper side of the layer other than the top layer, and the gas collection pipe and collection port are connected to each other, and the collected generated gas is transferred to the storage section. a gas pipe to guide the gas, and a circulation pipe connecting each of the drains;
A wastewater treatment device characterized by comprising a circulation pump inserted into the circulation pipe and returning a portion of the drawn sludge as seed sludge.
JP1251647A 1989-09-27 1989-09-27 Apparatus for treating effluent water Pending JPH03114594A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1251647A JPH03114594A (en) 1989-09-27 1989-09-27 Apparatus for treating effluent water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1251647A JPH03114594A (en) 1989-09-27 1989-09-27 Apparatus for treating effluent water

Publications (1)

Publication Number Publication Date
JPH03114594A true JPH03114594A (en) 1991-05-15

Family

ID=17225934

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1251647A Pending JPH03114594A (en) 1989-09-27 1989-09-27 Apparatus for treating effluent water

Country Status (1)

Country Link
JP (1) JPH03114594A (en)

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Publication number Priority date Publication date Assignee Title
JP2002079291A (en) * 2000-09-08 2002-03-19 Ebara Corp Anaerobic treatment method and apparatus
JP2009522096A (en) * 2006-01-05 2009-06-11 バイオタン システムズ インターナショナル ビー.ブイ. Method and reactor for anaerobic wastewater purification
JP2010533581A (en) * 2007-07-20 2010-10-28 エコデイズ・カンパニー・リミテッド Aerobic and anaerobic digestion apparatus and method with plug flow reactor
WO2012042581A1 (en) * 2010-09-27 2012-04-05 株式会社エイブル Apparatus for methane fermentation treatment
CN102616929A (en) * 2012-03-21 2012-08-01 天津科技大学 High-concentration waste water anaerobic fermentation device capable of realizing gas by-pass split-flow
CN104944574A (en) * 2015-05-22 2015-09-30 深圳市清研环境科技有限公司 Vertical multi-zone self-airlift circular current anaerobic bioreactor and application method thereof
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002079291A (en) * 2000-09-08 2002-03-19 Ebara Corp Anaerobic treatment method and apparatus
JP2009522096A (en) * 2006-01-05 2009-06-11 バイオタン システムズ インターナショナル ビー.ブイ. Method and reactor for anaerobic wastewater purification
JP2010533581A (en) * 2007-07-20 2010-10-28 エコデイズ・カンパニー・リミテッド Aerobic and anaerobic digestion apparatus and method with plug flow reactor
WO2012042581A1 (en) * 2010-09-27 2012-04-05 株式会社エイブル Apparatus for methane fermentation treatment
CN103153882A (en) * 2010-09-27 2013-06-12 株式会社爱博 Apparatus for methane fermentation treatment
JP5560343B2 (en) * 2010-09-27 2014-07-23 株式会社エイブル Methane fermentation treatment equipment
CN102616929A (en) * 2012-03-21 2012-08-01 天津科技大学 High-concentration waste water anaerobic fermentation device capable of realizing gas by-pass split-flow
CN104944574A (en) * 2015-05-22 2015-09-30 深圳市清研环境科技有限公司 Vertical multi-zone self-airlift circular current anaerobic bioreactor and application method thereof
CN107162178A (en) * 2017-07-03 2017-09-15 江苏奥尼斯环保科技有限公司 A kind of full mixing MBBR aerobic reactors
CN107162178B (en) * 2017-07-03 2020-08-07 江苏奥尼斯环保科技有限公司 Full-mixing MBBR reactor
JP2021122806A (en) * 2020-02-07 2021-08-30 水ing株式会社 Anaerobic treatment apparatus and anaerobic treatment method

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