JPH11114563A - Water treating device - Google Patents

Water treating device

Info

Publication number
JPH11114563A
JPH11114563A JP28591597A JP28591597A JPH11114563A JP H11114563 A JPH11114563 A JP H11114563A JP 28591597 A JP28591597 A JP 28591597A JP 28591597 A JP28591597 A JP 28591597A JP H11114563 A JPH11114563 A JP H11114563A
Authority
JP
Japan
Prior art keywords
membrane
permeated water
membrane separation
valve
flow path
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
JP28591597A
Other languages
Japanese (ja)
Inventor
Hajime Ito
肇 伊藤
Toshikazu Okumura
敏和 奥村
Kanji Tokushima
幹治 徳島
Koichi Okada
公一 岡田
Kazuyuki Honda
和之 本田
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP28591597A priority Critical patent/JPH11114563A/en
Publication of JPH11114563A publication Critical patent/JPH11114563A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To conveniently clean the face of the membrane of a membrane separator with a liq. chemical without suspending filtration. SOLUTION: The first and second membrane separators 14 and 15 are dipped in an aeration tank 12 and set. Permeated water pipes 21 and 24 communicated with the membrane-permeated water passages of the separators 14 and 15 through solenoid valves 22 and 25 are furnished, liq. chemical injection pipes 29 and 30 communicating with the membrane-permeated water passages of the separators 14 and 15 through solenoid valves 26 and 27 are provided, and the membrane separator to conduct filtration is switched to the membrane separator with the membrane to be cleaned and vice versa by opening or closing the solenoid valves 22, 25, 26 and 27.

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、浄化槽などの水処
理装置に関する。
[0001] The present invention relates to a water treatment apparatus such as a septic tank.

【0002】[0002]

【従来の技術】たとえば図2に示した浄化槽では、原水
1を脱窒槽2内に導入し、脱窒槽2内の活性汚泥混合液
3を硝化槽4へ移送しつつ、硝化槽4内の活性汚泥混合
液5の一部を脱窒槽2へ返送する状態において、脱窒槽
2内で嫌気条件下に脱窒処理し、硝化槽4内で、散気装
置6により散気する好気条件下に硝化処理するととも
に、硝化槽4内の活性汚泥混合液5を、吸引ポンプ7を
用いる吸引濾過方式(あるいは水位差を利用した重力濾
過方式)により膜分離装置8の膜エレメント8aで濾過
し、膜面を透過した透過水を透過水導出管8bを通じて
硝化槽4の外部へ導出している。そして、定期的にある
いは必要時に、次亜塩素酸ソーダ液などの薬液9を膜エ
レメント8aの透過水側に注入することにより、膜エレ
メント8aの膜面を薬液洗浄している。
2. Description of the Related Art In a septic tank shown in FIG. 2, for example, raw water 1 is introduced into a denitrification tank 2 and an activated sludge mixed solution 3 in the denitrification tank 2 is transferred to a nitrification tank 4 while an activated sludge mixture in the nitrification tank 4 is transferred. In a state in which a part of the sludge mixture 5 is returned to the denitrification tank 2, the denitrification treatment is performed in the denitrification tank 2 under anaerobic conditions, and in the nitrification tank 4, the air is diffused by the diffusion device 6 under aerobic conditions. At the same time as the nitrification treatment, the activated sludge mixed liquid 5 in the nitrification tank 4 is filtered by the membrane element 8a of the membrane separation device 8 by a suction filtration method using a suction pump 7 (or a gravity filtration method using a water level difference). The permeated water that has passed through the surface is led out of the nitrification tank 4 through the permeated water outlet pipe 8b. Then, periodically or when necessary, a chemical solution 9 such as sodium hypochlorite solution is injected into the permeated water side of the membrane element 8a to clean the membrane surface of the membrane element 8a.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記し
たような水処理装置では、薬液洗浄に必要な2〜3時間
は濾過処理を停止しなければならず、また薬液洗浄の終
了時に濾過処理を開始する操作を行うために管理者が拘
束されているのが現状である。
However, in the water treatment apparatus as described above, the filtration process must be stopped for a few hours required for cleaning the chemical solution, and the filtration process is started when the cleaning of the chemical solution is completed. At present, the administrator is bound to perform the operation of performing the operation.

【0004】本発明は上記問題を解決するもので、濾過
処理を停止することなく簡便に膜分離装置の膜面を薬液
洗浄できる水処理装置を提供することを目的とするもの
である。
An object of the present invention is to solve the above-mentioned problem, and an object of the present invention is to provide a water treatment apparatus capable of easily cleaning a membrane surface of a membrane separation apparatus with a chemical solution without stopping a filtration process.

【0005】[0005]

【課題を解決するための手段】上記問題を解決するため
に、本発明の請求項1記載の水処理装置は、処理槽の内
部に複数の膜分離装置を浸漬設置し、各膜分離装置の膜
透過水流路に弁装置を介して連通する透過水導出系を設
けるとともに、各膜分離装置の膜透過水流路に弁装置を
介して連通する薬液注入系を設けて、各弁装置の開閉操
作により、膜濾過工程を行う膜分離装置と膜洗浄工程を
行う膜分離装置とを切り替えるように構成したことを特
徴とする。ここで膜分離装置は一体的に操作できる単位
装置を意味し、複数の膜モジュールで構成された装置も
包含する。
In order to solve the above-mentioned problems, the water treatment apparatus according to the first aspect of the present invention is provided with a plurality of membrane separation devices immersed and installed in a treatment tank. Opening / closing operation of each valve device by providing a permeated water derivation system communicating with the membrane permeated water flow path via a valve device, and providing a chemical liquid injection system communicating with the membrane permeated water flow channel of each membrane separation device via a valve device. Thus, a membrane separation device that performs a membrane filtration process and a membrane separation device that performs a membrane cleaning process are switched. Here, the membrane separation device means a unit device that can be operated integrally, and also includes a device configured by a plurality of membrane modules.

【0006】請求項2記載の水処理装置は、弁装置とし
て電磁弁を配置し、各電磁弁に電気的に接続する制御装
置を設け、制御装置により各電磁弁を開閉制御して、一
つの膜分離装置の膜透過水流路に対する透過水導出系の
連通を遮断するとともに、この膜分離装置の膜透過水流
路に対する薬液注入系の流路を開放して薬液注入する膜
洗浄工程を、各膜分離装置に対して順次に行うように構
成したことを特徴とする。
According to a second aspect of the present invention, in the water treatment apparatus, an electromagnetic valve is disposed as a valve device, a control device electrically connected to each electromagnetic valve is provided, and each electromagnetic valve is controlled to open and close by the control device. The membrane washing step of shutting off the communication of the permeated water derivation system with the membrane permeated water flow path of the membrane separation device and opening the flow path of the drug solution injection system with respect to the membrane permeated water flow channel of the membrane separation device, and injecting the drug solution into each membrane, It is characterized in that it is configured to perform the operations sequentially on the separation device.

【0007】請求項1記載の構成によれば、各弁装置の
開閉操作により、膜濾過工程を行う膜分離装置と膜洗浄
工程を行う膜分離装置とを切り替えられるので、洗浄を
必要とする膜分離装置は膜洗浄工程を行いながら、その
他の膜分離装置は膜濾過工程を行うことができ、濾過処
理を停止することなく膜分離装置を薬液洗浄できる。
According to the first aspect of the present invention, the membrane separating apparatus for performing the membrane filtration step and the membrane separating apparatus for performing the membrane cleaning step can be switched by opening and closing the respective valve devices. While the separation apparatus performs the membrane washing step, the other membrane separation apparatuses can perform the membrane filtration step, and the membrane separation apparatus can be washed with a chemical solution without stopping the filtration process.

【0008】請求項2記載の構成によれば、制御装置に
より各電磁弁が開閉制御され、複数の膜分離装置が自動
的に順次に薬液洗浄される。
According to the second aspect of the present invention, the opening and closing of each solenoid valve is controlled by the control device, and the plurality of membrane separation devices are automatically and sequentially cleaned with the chemical solution.

【0009】[0009]

【発明の実施の形態】以下、本発明の実施の形態を図面
を参照しながら説明する。図1において、被処理水供給
管11が開口した曝気槽12の内部に、活性汚泥混合液
13に浸漬して第1膜分離装置14と第2膜分離装置1
5とが設置されている。
Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, an activated sludge mixture 13 is immersed in an aeration tank 12 in which a treated water supply pipe 11 is opened, and a first membrane separation device 14 and a second membrane separation device 1 are immersed.
5 are installed.

【0010】第1膜分離装置14および第2膜分離装置
15はそれぞれ、膜エレメント14a,15aを配列し
たものであり、各膜エレメント14a,15aの膜透過
水流路に連通した集水管14b,15bを有している。
第1膜分離装置14および第2膜分離装置15の下部に
はそれぞれ、電磁弁16,17を介してブロワ18に連
通した散気装置19,20が設けられている。
The first membrane separator 14 and the second membrane separator 15 are respectively arranged with membrane elements 14a and 15a, and water collecting pipes 14b and 15b communicating with the membrane permeated water flow paths of the respective membrane elements 14a and 15a. have.
Below the first membrane separator 14 and the second membrane separator 15 are provided diffusers 19 and 20 which communicate with a blower 18 via solenoid valves 16 and 17, respectively.

【0011】第1膜分離装置14の集水管14bには第
1透過水導出管21が連通しており、この第透過水導出
管21は電磁弁22と吸引ポンプ23とを介装し、槽外
で開口している。第2膜分離装置15の集水管15bに
は第2透過水導出管24が連通しており、この第2透過
水導出管24は電磁弁25を介装し、第1透過水導出管
21の電磁弁22と吸引ポンプ23との間の位置に連通
している。
A first permeated water outlet pipe 21 communicates with the water collecting pipe 14b of the first membrane separation device 14, and this first permeated water outlet pipe 21 is provided with a solenoid valve 22 and a suction pump 23, and is connected to a tank. Open outside. A second permeated water outlet pipe 24 communicates with the water collection pipe 15b of the second membrane separation device 15, and the second permeated water outlet pipe 24 is provided with an electromagnetic valve 25 and is connected to the first permeated water outlet pipe 21. It communicates with a position between the solenoid valve 22 and the suction pump 23.

【0012】第1透過水導出管21の電磁弁22より上
流側の位置と、第2透過水導出管24の電磁弁25より
上流側の位置にはそれぞれ、電磁弁26,27を介して
薬液タンク28に接続した薬液注入管29,30が連通
している。
The first permeated water outlet pipe 21 at a position upstream of the solenoid valve 22 and the second permeated water outlet pipe 24 at a position upstream of the solenoid valve 25 are connected to the chemical via electromagnetic valves 26 and 27, respectively. Chemical liquid injection pipes 29 and 30 connected to the tank 28 communicate with each other.

【0013】電磁弁22,25,26,27には、これ
ら電磁弁22,25,26,27を後述するごとく開閉
制御する制御装置31が電気的に接続している。上記し
た構成における作用を説明する。
The solenoid valves 22, 25, 26 and 27 are electrically connected to a control device 31 for controlling the opening and closing of the solenoid valves 22, 25, 26 and 27 as described later. The operation of the above configuration will be described.

【0014】被処理水は被処理水供給管11を通じて曝
気槽12の内部に供給されて、活性汚泥混合液13中に
混合され、被処理水中の汚濁物質は散気装置19,20
より散気される好気的条件下、活性汚泥の作用によって
酸化分解される。
The water to be treated is supplied to the inside of an aeration tank 12 through a water supply pipe 11 to be mixed with the activated sludge mixture 13, and pollutants in the water to be treated are diffused by diffusers 19, 20.
It is oxidatively decomposed by the action of activated sludge under more aerobically aerobic conditions.

【0015】このとき、制御装置31によって、電磁弁
25,26は閉塞されるとともに電磁弁22,27は開
放されており、これより、第1膜分離装置14の集水管
14bに連通した第1透過水導出管21が開放され、第
1薬液注入管29が閉塞された状態となっていて、吸引
ポンプ23より第1透過水導出管21を通じて各膜エレ
メント14aに作用する吸引圧によって膜面において濾
過が行われ、膜面を透過して透過水流路に流入した透過
水が集水管14b,第1透過水導出管21を通じて槽外
へ導出される。
At this time, the solenoid valves 25 and 26 are closed and the solenoid valves 22 and 27 are opened by the control device 31, so that the first valve communicating with the water collecting pipe 14 b of the first membrane separation device 14 is formed. The permeated water outlet pipe 21 is opened and the first chemical liquid injection pipe 29 is closed, and the suction pump 23 applies a suction pressure acting on each membrane element 14a through the first permeated water outlet pipe 21 so that the first chemical liquid injection pipe 29 is closed on the membrane surface. Filtration is performed, and the permeated water that has passed through the membrane surface and flowed into the permeated water flow path is led out of the tank through the water collecting pipe 14b and the first permeated water outlet pipe 21.

【0016】また、第2膜分離装置15の集水管15b
に連通した第2透過水導出管24が閉塞され、第2薬液
注入管30が開放された状態となっていて、薬液タンク
28内の次亜塩素酸ソーダなどの薬液が第2薬液注入管
30,第2透過水導出管24,集水管15bを通じて膜
エレメント15aの透過水流路に注入され、膜面を活性
汚泥混合液13側へ浸透していき、膜面が洗浄される。
薬液注入が終了した後も、第2薬液注入管30が開放さ
れ、第2透過水導出管24が閉塞された状態は保持さ
れ、薬液が次亜塩素酸ソーダの場合はその大部分が揮散
する。
The water collecting pipe 15b of the second membrane separation device 15
The second permeated water outlet pipe 24 communicating with the second liquid injection pipe 30 is closed and the second chemical liquid injection pipe 30 is in an open state, and the liquid chemical such as sodium hypochlorite in the chemical liquid tank 28 is filled with the second liquid injection pipe 30. , The second permeated water outlet pipe 24 and the water collecting pipe 15b are injected into the permeated water flow path of the membrane element 15a to permeate the membrane surface into the activated sludge mixture 13 side, and the membrane surface is washed.
Even after the chemical solution injection is completed, the state where the second chemical solution injection pipe 30 is opened and the second permeated water outlet pipe 24 is closed is maintained, and when the chemical solution is sodium hypochlorite, most of the chemical vaporizes. .

【0017】そして、定期メンテナンス時に、制御装置
31によって電磁弁25,26が開放されるとともに電
磁弁22,27が閉塞され、これにより上記と逆に、第
2膜分離装置15の集水管15bに連通した第2透過水
導出管24が開放され、第2薬液注入管30が閉塞され
た状態となって、膜エレメント15aの膜面において濾
過が行われ、透過水が槽外へ導出されるとともに、第1
膜分離装置14の集水管14bに連通した第1透過水導
出管21が閉塞され、第1薬液注入管29が開放された
状態となって、膜エレメント14aが薬液洗浄される。
At the time of the regular maintenance, the electromagnetic valves 25 and 26 are opened and the electromagnetic valves 22 and 27 are closed by the control device 31, whereby the water collecting pipe 15b of the second membrane separation device 15 is connected to the water collecting pipe 15b. The connected second permeated water outlet pipe 24 is opened, and the second chemical liquid injection pipe 30 is closed, so that filtration is performed on the membrane surface of the membrane element 15a, and the permeated water is drawn out of the tank. , First
The first permeated water outlet pipe 21 communicating with the water collection pipe 14b of the membrane separation device 14 is closed, and the first chemical liquid injection pipe 29 is opened, and the membrane element 14a is washed with the chemical liquid.

【0018】このようにして、第1膜分離装置14によ
り膜濾過しながら、第2膜分離装置15を膜洗浄できる
とともに、第1膜分離装置14が汚れてきたら自動的
に、第1膜分離装置14を膜洗浄しながら、第2膜分離
装置15により膜濾過する運転に切り替えられるので、
濾過処理を停止することなく各膜分離装置を薬液洗浄す
ることができ、透過流束を維持できる。
In this way, the second membrane separator 15 can be washed while the first membrane separator 14 filters the membrane, and when the first membrane separator 14 becomes contaminated, the first membrane separator 15 is automatically cleaned. Since the operation is switched to the operation of membrane filtration by the second membrane separation device 15 while the device 14 is being washed with a membrane,
Each membrane separation device can be washed with a chemical solution without stopping the filtration process, and the permeation flux can be maintained.

【0019】なお、上記においては活性汚泥処理を行う
曝気槽12を例に挙げて説明したが、上記した構成は、
前述したような脱窒槽とともに設けられる硝化槽や単な
る固液分離槽にも適用できる。第1および第2の膜分離
装置14,15は浸漬型(外圧型)であればいずれのタ
イプであってもよく、セラミック膜、有機膜等の種々の
膜を配した管状、平板状等の種々の形状の膜エレメント
が可能である。第1および第2の透過水導出管21,2
4は合することなく単独に設けてもよく、電磁弁22,
25と、電磁弁26,27とを切替弁に代えてもよい。
In the above description, the aeration tank 12 for performing the activated sludge treatment has been described as an example.
The present invention can be applied to a nitrification tank provided together with the above-described denitrification tank or a mere solid-liquid separation tank. The first and second membrane separation devices 14 and 15 may be of any type as long as they are of the immersion type (external pressure type), such as a tubular or flat plate having various membranes such as a ceramic membrane and an organic membrane. Various shapes of membrane elements are possible. First and second permeated water outlet pipes 21 and
4 may be provided independently without being combined.
25 and the solenoid valves 26 and 27 may be replaced by switching valves.

【0020】また、上記においては制御装置31を設け
て自動的に運転を切り替えるようにしたが、従来のよう
に薬液洗浄の終了時に膜濾過運転に切り替える必要がな
いので手動で切り替えるようにしても作業は容易であ
り、その場合は、各電磁弁を通常の開閉弁に代えればよ
い。散気装置は常時2台とも運転してもよいし、濾過を
行う膜分離装置の下部の散気装置のみ運転してもよく、
その場合は制御装置31によって各膜分離装置(すなわ
ち電磁弁)に連動させるのが好都合である。
In the above, the control device 31 is provided to automatically switch the operation. However, it is not necessary to switch to the membrane filtration operation at the end of the cleaning of the chemical solution as in the prior art. The work is easy, and in that case, each solenoid valve may be replaced with a normal on-off valve. The two diffusers may be operated at all times, or only the diffuser below the membrane separation device that performs the filtration may be operated,
In that case, it is convenient to link the respective membrane separation devices (that is, solenoid valves) by the control device 31.

【0021】[0021]

【発明の効果】以上のように、本発明によれば、弁装置
の開閉操作によって、膜濾過工程を行う膜分離装置と膜
洗浄工程を行う膜分離装置とを切り替え自在に構成した
ことにより、濾過処理を停止することなく膜分離装置を
薬液洗浄でき、管理も容易である。
As described above, according to the present invention, it is possible to switch between a membrane separation device for performing a membrane filtration process and a membrane separation device for performing a membrane cleaning process by opening and closing a valve device. The membrane separation device can be washed with a chemical solution without stopping the filtration process, and management is easy.

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

【図1】本発明の一実施形態における水処理装置として
の曝気槽の概略全体構成を示した縦断面図である。
FIG. 1 is a longitudinal sectional view showing a schematic overall configuration of an aeration tank as a water treatment apparatus according to an embodiment of the present invention.

【図2】従来の水処理装置としての浄化槽の概略全体構
成を示した縦断面図である。
FIG. 2 is a longitudinal sectional view showing a schematic overall configuration of a septic tank as a conventional water treatment apparatus.

【符号の説明】[Explanation of symbols]

12 曝気槽 14 第1膜分離装置 15 第2膜分離装置 21 第1透過水導出管 24 第2透過水導出管 22, 25 電磁弁 26, 27 電磁弁 28 薬液タンク 29 第1薬液注入管 30 第2薬液注入管 31 制御装置 12 Aeration tank 14 First membrane separator 15 Second membrane separator 21 First permeate outlet pipe 24 Second permeate outlet pipe 22, 25 Solenoid valve 26, 27 Solenoid valve 28 Chemical tank 29 First chemical inlet 30 2 Chemical injection tube 31 Controller

───────────────────────────────────────────────────── フロントページの続き (72)発明者 岡田 公一 兵庫県尼崎市浜一丁目1番1号 株式会社 クボタ技術開発研究所内 (72)発明者 本田 和之 滋賀県甲賀郡甲西町高松2番地の1 株式 会社クボタ滋賀工場内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Koichi Okada 1-1-1 Hama, Amagasaki-shi, Hyogo Inside Kubota Research Institute of Technology (72) Inventor Kazuyuki Honda 2 Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture 1 Kubota Shiga Plant

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 処理槽の内部に複数の膜分離装置を浸漬
設置し、各膜分離装置の膜透過水流路に弁装置を介して
連通する透過水導出系を設けるとともに、各膜分離装置
の膜透過水流路に弁装置を介して連通する薬液注入系を
設け、各弁装置の開閉操作により、膜濾過工程を行う膜
分離装置と膜洗浄工程を行う膜分離装置とを切り替える
ように構成したことを特徴とする水処理装置。
1. A plurality of membrane separation devices are immersed and installed in a treatment tank, and a permeated water discharge system is provided to communicate with a membrane permeated water flow path of each membrane separation device via a valve device. A chemical liquid injection system that communicates with the membrane permeated water flow path via a valve device is provided, and the opening and closing operation of each valve device switches between a membrane separation device that performs a membrane filtration process and a membrane separation device that performs a membrane cleaning process. A water treatment apparatus characterized by the above-mentioned.
【請求項2】 弁装置として電磁弁を配置し、各電磁弁
に電気的に接続する制御装置を設け、制御装置により各
電磁弁を開閉制御して、一つの膜分離装置の膜透過水流
路に対する透過水導出系の連通を遮断するとともに、こ
の膜分離装置の膜透過水流路に対する薬液注入系の流路
を開放して薬液注入する膜洗浄工程を、各膜分離装置に
対して順次に行うように構成したことを特徴とする請求
項1記載の水処理装置。
2. An electromagnetic valve is disposed as a valve device, a control device electrically connected to each electromagnetic valve is provided, and each electromagnetic valve is controlled to be opened and closed by the control device. The membrane washing step of shutting off the communication of the permeated water discharge system to the membrane separation apparatus and opening the flow path of the chemical liquid injection system to the membrane permeated water flow path of the membrane separation apparatus and injecting the chemical liquid is sequentially performed for each membrane separation apparatus. The water treatment apparatus according to claim 1, wherein the water treatment apparatus is configured as described above.
JP28591597A 1997-10-20 1997-10-20 Water treating device Pending JPH11114563A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28591597A JPH11114563A (en) 1997-10-20 1997-10-20 Water treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28591597A JPH11114563A (en) 1997-10-20 1997-10-20 Water treating device

Publications (1)

Publication Number Publication Date
JPH11114563A true JPH11114563A (en) 1999-04-27

Family

ID=17697670

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28591597A Pending JPH11114563A (en) 1997-10-20 1997-10-20 Water treating device

Country Status (1)

Country Link
JP (1) JPH11114563A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007152282A (en) * 2005-12-07 2007-06-21 Mitsubishi Rayon Eng Co Ltd Membrane separation active sludge treatment method
JP2013121586A (en) * 2011-11-08 2013-06-20 Toshiba Corp Method and device for membrane separation activated sludge treatment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007152282A (en) * 2005-12-07 2007-06-21 Mitsubishi Rayon Eng Co Ltd Membrane separation active sludge treatment method
JP2013121586A (en) * 2011-11-08 2013-06-20 Toshiba Corp Method and device for membrane separation activated sludge treatment

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