JPH1133582A - Sewage treatment apparatus - Google Patents

Sewage treatment apparatus

Info

Publication number
JPH1133582A
JPH1133582A JP19848197A JP19848197A JPH1133582A JP H1133582 A JPH1133582 A JP H1133582A JP 19848197 A JP19848197 A JP 19848197A JP 19848197 A JP19848197 A JP 19848197A JP H1133582 A JPH1133582 A JP H1133582A
Authority
JP
Japan
Prior art keywords
air
chemical
aerobic treatment
treatment tank
diffuser
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.)
Withdrawn
Application number
JP19848197A
Other languages
Japanese (ja)
Inventor
Kenichi Minami
健一 巳波
Akihiro Ueda
明弘 上田
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP19848197A priority Critical patent/JPH1133582A/en
Publication of JPH1133582A publication Critical patent/JPH1133582A/en
Withdrawn legal-status Critical Current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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Activated Sludge Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To exclude the contaminant bonded to the periphery of an air diffuser by washing the same with a chemical soln. to facilitate maintenance by arranging the air sending pipe connecting an air supply source and the air diffuser to an aerobic treatment bed and arranging a chemical soln. cylinder at a position higher than the liquid surface in the aerobic treatment tank. SOLUTION: A sewage treatment apparatus is equipped with an aerobic treatment tank 1 and the air diffuser 2 having air jet holes 3 formed thereto arranged to the bottom part thereof is connected to an air supply source 4 by an air sending pipe 5 and a chemical soln. injection pipe 7 is suspended from the chemical soln. cylinder 6 arranged on the aerobic treatment tank 1. After purifying treatment filtering sewage by the membrane module 9, a three-way cock 8 is changed over and the chemical soln. in the chemical soln. cylinder 6 is stored in the air sending pipe under the three-way cock 8 from the chemical soln. injection pipe 7. Subsequently, when the three-way cock 8 is again changed over in such a state that the air sending pipe 5 is filled with the chemical soln., the chemical soln. in the air sending pipe 5 is ejected from the air jet holes 3 along with air and the contaminant bonded to the periphery thereof is dissolved and removed.

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、汚水を好気性処理
するための汚水処理装置に関する。
The present invention relates to a sewage treatment apparatus for aerobically treating sewage.

【0002】[0002]

【従来の技術】汚水を処理する方法には、細菌などの生
物による汚濁物質分解作用を利用した生物学的処理方法
があり、生物学的処理方法にも酸素を嫌う嫌気性菌によ
って分解する嫌気性処理と、酸素を必要とする好気性菌
による好気性処理の2種類がある。これらのうち、好気
性処理においては、好気性処理槽内に散気装置を設置
し、散気装置に穿設された多数個の小さいエア噴出孔か
ら好気性処理槽内へ気泡状のエアを吹き込んで曝気する
という操作を行う。
2. Description of the Related Art As a method for treating sewage, there is a biological treatment method utilizing an action of decomposing pollutants by organisms such as bacteria. The biological treatment method also includes an anaerobic bacterium which is decomposed by anaerobic bacteria which dislike oxygen. There are two types of treatment: aerobic treatment and aerobic treatment by aerobic bacteria requiring oxygen. Among these, in the aerobic treatment, an air diffuser is installed in the aerobic treatment tank, and bubble air is supplied into the aerobic treatment tank from a number of small air ejection holes formed in the diffuser. An operation of blowing and aerating is performed.

【0003】図3はこのような好気性処理を行うための
従来の汚水処理装置の例である。この汚水処理装置は、
好気性処理槽aの底部に散気装置bが設置されており、
散気装置bは送気管eでブロワーdと連結されている。
そして散気装置bの上面には複数個のエア噴出孔cが穿
設されている。
FIG. 3 shows an example of a conventional sewage treatment apparatus for performing such aerobic treatment. This sewage treatment device,
A diffuser b is installed at the bottom of the aerobic treatment tank a,
The air diffuser b is connected to the blower d by an air supply pipe e.
A plurality of air ejection holes c are formed on the upper surface of the air diffuser b.

【0004】また、好気性処理槽aの外には、薬液(次
亜塩素酸ナトリウム等の洗浄剤)が入った薬液筒f、薬
液の送液ポンプpが設置され、送液ポンプpの先端には
薬液注入管hが連結され、薬液注入管hは好気性処理さ
れた汚水から汚泥等を分離させるための膜モジュールi
の内面に接続されている。
[0004] Outside the aerobic treatment tank a, a chemical solution tube f containing a chemical solution (a cleaning agent such as sodium hypochlorite) and a chemical solution sending pump p are installed. Is connected to a chemical solution injection pipe h, and the chemical solution injection pipe h is a membrane module i for separating sludge and the like from aerobic treated wastewater.
Is connected to the inner surface of the

【0005】また、好気性処理された後の処理水から固
形分を分離するために、散気装置bの上に膜モジュール
iが設けられ、膜モジュールiの内部より吸引ポンプで
吸引して処理水を濾過する膜濾過浄化方式が行われるよ
うになっている。
[0005] Further, in order to separate solids from the treated water after the aerobic treatment, a membrane module i is provided on the air diffuser b. A membrane filtration purification system for filtering water is performed.

【0006】そして、ブロワーdから散気装置bへエア
を送るラインと、薬液筒f内の薬液を膜モジュールiへ
送るラインとは別の系統とされている。
The line for sending air from the blower d to the diffuser b and the line for sending the chemical in the chemical cylinder f to the membrane module i are different systems.

【0007】しかるに、図3に示す汚水処理装置におい
て、メンテナンスを行うために散気装置bへのエアの供
給を停止するような場合、エア噴出孔cから汚水が逆流
して目詰まりを起こし、散気装置bが正常に機能しなく
なることがある。
However, in the sewage treatment apparatus shown in FIG. 3, when the supply of air to the air diffuser b is stopped for maintenance, the sewage flows backward from the air ejection hole c to cause clogging. The air diffuser b may not function properly.

【0008】また、膜モジュールiのような膜濾過浄化
方式を備えた汚水処理装置でも、活性汚泥濃度を高くし
て運転するために汚水の粘度が高くなり、エア噴出孔c
から常時エアを噴出させていても、エア噴出孔cに付着
する汚泥によって目詰まりを起こすことがある。このよ
うな場合、散気装置bを数カ月乃至1年毎に好気性処理
槽aから引き上げ、ブラシなどでエア噴出孔cを清掃す
ることが一般に行われている。
Further, even in a sewage treatment apparatus equipped with a membrane filtration and purification system such as a membrane module i, the viscosity of the sewage increases because the activated sludge is operated at a high concentration.
Even when air is constantly ejected from the air, clogging may occur due to sludge adhering to the air ejection holes c. In such a case, it is common practice to pull up the air diffuser b from the aerobic treatment tank a every several months to one year and clean the air ejection holes c with a brush or the like.

【0009】しかし、そのためにはメンテナンスの度毎
に散気装置bを好気性処理槽aから引き上げなければな
らず、特に図3に示すような膜濾過浄化方式の場合、膜
モジュールiの下部に散気装置bが配置されることが多
いために、散気装置bを取り外して引き上げるのに著し
く困難を伴う。
However, for that purpose, the air diffuser b must be pulled out of the aerobic treatment tank a every time maintenance is performed. In particular, in the case of the membrane filtration and purification system as shown in FIG. Since the air diffuser b is often arranged, it is extremely difficult to remove and pull up the air diffuser b.

【0010】また、エア噴出孔cの目詰まりをブラシで
こするという作業は、手間がかかる上不衛生であり、作
業者に嫌がられている。更にエア噴出孔cの孔径に合わ
せたブラシを備えておかねばならないという不便さもあ
る。
Further, the work of rubbing the clogged air ejection holes c with a brush is troublesome and unsanitary, and is disliked by workers. Further, there is another inconvenience that a brush corresponding to the diameter of the air ejection hole c must be provided.

【0011】更に、膜濾過浄化方式においても、膜濾過
を長期間続けると膜の目詰まりが発生する。膜の目詰ま
りに対しては、膜を薬液により洗浄する薬液洗浄が有効
とされていて、例えば特公平6−65371号公報に
は、一時的に膜濾過を停止し、膜内に濾過された透過液
の流動方向と逆方向に薬液を流して膜内部より洗浄す
る、いわゆる逆洗と呼ばれる方法が示されている。(図
3に示す汚水処理装置はこの逆洗を行うことのできるも
のである。)
Further, also in the membrane filtration purification system, membrane clogging occurs when membrane filtration is continued for a long period of time. For clogging of the membrane, chemical cleaning for cleaning the membrane with a chemical is effective. For example, in Japanese Patent Publication No. 6-65371, membrane filtration is temporarily stopped and the membrane is filtered. A method called backwashing, in which a chemical solution is caused to flow in a direction opposite to the flow direction of the permeate to wash the inside of the membrane, is shown. (The sewage treatment apparatus shown in FIG. 3 can perform this backwashing.)

【0012】しかしながら、膜は透過抵抗が大きい上、
水深による水圧が作用するので、深い位置にある膜の内
部に薬液を流し込んで逆洗するためには、図3中に示す
ように、薬液筒fの出口に送液ポンプpを設け、送液ポ
ンプpにより薬液に1kgf/cm2 以上の圧力をかけ
て注入する必要がある。そのために設備費、運転費、メ
ンテナンス費等が高価につくという問題がある。
However, the membrane has high transmission resistance and
Since the water pressure due to the water depth acts, in order to pour the chemical solution into the inside of the membrane at a deep position for backwashing, as shown in FIG. It is necessary to inject the drug solution by applying a pressure of 1 kgf / cm 2 or more by the pump p. Therefore, there is a problem that equipment costs, operation costs, maintenance costs, and the like are expensive.

【0013】[0013]

【発明が解決しようとする課題】本発明は、上記のよう
な従来技術の問題点を解消し、メンテナンスの度毎に散
気装置を引き上げてエア噴出孔の目詰まりを清掃する必
要のない汚水処理装置を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems of the prior art, and eliminates the need for cleaning the clogging of the air ejection holes by pulling up the air diffuser every time maintenance is performed. It is an object to provide a processing device.

【0014】また、好気性処理した汚水を膜濾過浄化方
式により濾過する場合においても、膜モジュールを引き
上げる必要がなく、しかも膜モジュールを逆洗するため
の送液ポンプなど、特別の設備を必要としない汚水処理
装置を提供することを目的とする。
[0014] Further, even when the aerobic treated wastewater is filtered by the membrane filtration and purification method, there is no need to pull up the membrane module, and special equipment such as a liquid feed pump for backwashing the membrane module is required. It is an object of the present invention to provide a wastewater treatment device that does not use wastewater.

【0015】[0015]

【課題を解決するための手段】上記の目的を達成するた
め、本発明は、好気性処理槽を備えた汚水処理装置であ
って、エア供給源と散気装置とを連結する送気管と、好
気性処理槽内の液面より高い位置に置かれた薬液筒に連
結される薬液注入管とが連結されていることを特徴とす
る。
According to the present invention, there is provided a sewage treatment apparatus having an aerobic treatment tank, comprising: an air supply pipe connecting an air supply source and a diffuser; It is characterized in that it is connected to a chemical liquid injection pipe connected to a chemical liquid cylinder placed at a position higher than the liquid level in the aerobic treatment tank.

【0016】また、送気管と薬液注入管とが切替弁を介
して連結されていることを特徴とする。
Further, the invention is characterized in that the air supply pipe and the chemical injection pipe are connected via a switching valve.

【0017】本発明において、送気管、薬液注入管、切
替弁等の材質は特に限定されるものではないが、汚水及
び薬液によって変質や劣化を生じしにくい材質が望まし
く、ポリ塩化ビニル、ポリエチレン、ポリプロピレン、
ABS樹脂、FRP等の汎用の合成樹脂、ステンレス
鋼、真鍮等の金属材料などが挙げられる。なお、薬液と
しては、例えば次亜塩素酸ナトリウム等の洗浄剤が通常
に用いられる。
In the present invention, the materials of the air supply pipe, the chemical liquid injection pipe, the switching valve, and the like are not particularly limited, but are preferably materials that are not easily deteriorated or deteriorated by sewage and a chemical liquid. polypropylene,
Examples include general-purpose synthetic resins such as ABS resin and FRP, and metal materials such as stainless steel and brass. As the chemical, a cleaning agent such as sodium hypochlorite is usually used.

【0018】また、切替弁としては手動、電動、空気動
等の三方コックが好適に用いられ、その設置位置は好気
性処理槽内の最高液面よりも高いことが好ましい。
A three-way cock of a manual, electric, pneumatic or the like is suitably used as the switching valve, and its installation position is preferably higher than the highest liquid level in the aerobic treatment tank.

【0019】(作用)請求項1記載の本発明は、メンテ
ナンスの際エアの供給を止め、代わって薬液筒の下のコ
ックを開けて、薬液筒と好気性処理槽の液面の高低差に
より、薬液を薬液注入管を通じて送気管に自然流下させ
る。次いで再び薬液筒の下のコックを閉じ、送気管への
エアの供給を開始すると、送気管内の薬液がエア圧によ
って散気装置のエア噴出孔から押し出される。
(Operation) According to the first aspect of the present invention, the supply of air is stopped at the time of maintenance, and a cock below the chemical liquid cylinder is opened in place of the chemical liquid cylinder, and the level difference between the chemical liquid cylinder and the aerobic treatment tank is changed. Then, the chemical is allowed to flow naturally into the air supply pipe through the chemical injection pipe. Next, the cock below the liquid medicine cylinder is closed again, and when the supply of air to the air supply pipe is started, the liquid medicine in the air supply pipe is pushed out from the air ejection hole of the air diffuser by the air pressure.

【0020】その結果、散気装置のエア噴出孔のまわり
に付着して目詰まりを起こしていた汚泥などの汚濁物質
が薬液により洗浄されて取り除かれるとともに、膜モジ
ュールの外面に付着している汚泥などの汚濁物質が膜モ
ジュールの外面から薬液により洗浄され、取り除かれ
る。
As a result, contaminants such as sludge that has adhered and clogged around the air ejection holes of the air diffuser are removed by washing with a chemical solution, and the sludge adhering to the outer surface of the membrane module is removed. Contaminants such as are washed and removed from the outer surface of the membrane module with a chemical solution.

【0021】また、請求項2記載の本発明は、切替弁を
切り替えることにより、薬液とエアの切り替えを一動作
で簡単に行うことができ、且つ自動化が容易である。
According to the second aspect of the present invention, by switching the switching valve, the switching between the chemical solution and the air can be easily performed by one operation, and automation is easy.

【0022】[0022]

【発明の実施の形態】以下、本発明の実施の形態につき
図面を参照しながら具体的に説明する。図1は本発明汚
水処理装置の実施の形態を示す模式図で、曝気により好
気性処理を行っている状態、図2は曝気を中止して薬液
による洗浄を行っている状態を示す。
Embodiments of the present invention will be specifically described below with reference to the drawings. FIG. 1 is a schematic view showing an embodiment of the sewage treatment apparatus of the present invention, in which aerobic treatment is performed by aeration, and FIG. 2 shows a state in which aeration is stopped and cleaning with a chemical solution is performed.

【0023】汚水処理装置は好気性処理槽1を備え、好
気性処理槽1の底部には散気装置2が設置されている。
散気装置2には、例えばその上面に複数個のエア噴出孔
3が穿設されていて、送気管5により好気性処理槽1の
外に設置されたブロア(エア供給源)4と連結されてい
る。
The sewage treatment apparatus has an aerobic treatment tank 1, and an air diffuser 2 is installed at the bottom of the aerobic treatment tank 1.
The air diffuser 2 has, for example, a plurality of air ejection holes 3 formed on an upper surface thereof, and is connected to a blower (air supply source) 4 installed outside the aerobic treatment tank 1 by an air supply pipe 5. ing.

【0024】好気性処理槽1の上には、次亜塩素酸ナト
リウム等の洗浄剤が入った薬液筒6が設置され、薬液筒
6からは薬液注入管7が垂設されていて、送気管5と薬
液注入管7とは三方コック8を介して連結されている。
三方コック8は好気性処理槽1の最高液面HLより高い
位置に設置されていて、図示しないアクチュエータによ
り駆動される構造とされている。
On the aerobic treatment tank 1, a chemical solution tube 6 containing a cleaning agent such as sodium hypochlorite is installed, and from the solution solution tube 6, a chemical solution injection pipe 7 is vertically installed. 5 and the chemical injection pipe 7 are connected via a three-way cock 8.
The three-way cock 8 is installed at a position higher than the highest liquid level HL of the aerobic treatment tank 1 and has a structure driven by an actuator (not shown).

【0025】また、好気性処理槽1内の散気装置2の上
には、膜モジュール9が設けられている。膜モジュール
9の多数の中空糸膜91は垂直方向両側のフレーム92
により支持され、フレーム92の上下には中空糸膜91
を上下でつなぐモジュールヘッダ93が設けられてい
て、上方のモジュールヘッダ93からポンプにより膜濾
過液を吸収、放流するようにされている。
On the air diffuser 2 in the aerobic treatment tank 1, a membrane module 9 is provided. A large number of hollow fiber membranes 91 of the membrane module 9 are
And a hollow fiber membrane 91 above and below the frame 92.
A module header 93 is provided to connect the upper and lower sides of the membrane filtrate, and the membrane filtrate is absorbed and discharged from the upper module header 93 by a pump.

【0026】次に、この汚水処理装置の作用について説
明する。図1に示す状態においては、三方コック8には
エア供給源4と散気装置2が連結され、薬液注入管7は
送気管5と切り離された位置とされている。エア供給源
4から供給されたエアは送気管5を経て散気装置2のエ
ア噴出孔3から小さい気泡となって汚水中へ噴出され、
汚水が好気性処理される。
Next, the operation of the sewage treatment apparatus will be described. In the state shown in FIG. 1, the air supply source 4 and the air diffuser 2 are connected to the three-way cock 8, and the chemical liquid injection pipe 7 is located at a position separated from the air supply pipe 5. The air supplied from the air supply source 4 passes through the air supply pipe 5 and becomes small bubbles from the air ejection holes 3 of the diffuser 2 and is ejected into the sewage,
Sewage is aerobic treated.

【0027】好気性処理された汚水は気泡とともに好気
性処理槽1内を上方へ移動しつつ、膜モジュール9の外
面から内面へと透過して濾過され、上のモジュールヘッ
ダ93に集まり、図示しないポンプにより吸引されて好
気性処理槽1外へ放流される。
The sewage subjected to the aerobic treatment moves upward in the aerobic treatment tank 1 together with the air bubbles, passes through the membrane module 9 from the outer surface to the inner surface, is filtered, and is collected in the upper module header 93, not shown. It is sucked by the pump and discharged out of the aerobic treatment tank 1.

【0028】しかしながら、好気性処理槽1を長時間運
転すると汚水中の汚泥がエア噴出孔3の周辺に付着して
エア噴出孔3が目詰まりする。また膜モジュール9もそ
の外周に汚泥が付着して目詰まりする。
However, when the aerobic treatment tank 1 is operated for a long time, the sludge in the sewage adheres to the periphery of the air ejection hole 3 and the air ejection hole 3 is clogged. Also, the sludge adheres to the outer periphery of the membrane module 9 and is clogged.

【0029】そこで、図2に示すように三方コック8を
切り替えて、薬液注入管7と送気管5を連結し、エア供
給源4と散気装置2を切り離すと、薬液は薬液筒6と好
気性処理槽1内の液面の高低差により薬液注入管を自然
流下して、三方コック8の下の送気管5内に溜まる。そ
して送気管5内に薬液がほぼ充満した状態で再び前の位
置に三方コック8を切り替えると、送気管5内に溜まっ
ていた薬液はエアとともにエア噴出孔3から噴出し、エ
ア噴出孔3の周囲に付着していた汚泥等の汚濁物質の粒
子は薬液により溶解されて除去され、目詰まりが清掃さ
れる。
Then, as shown in FIG. 2, the three-way cock 8 is switched to connect the chemical liquid injection pipe 7 to the air supply pipe 5 and disconnect the air supply source 4 from the air diffuser 2. Due to the level difference of the liquid level in the gaseous treatment tank 1, the chemical liquid injection pipe flows down naturally and accumulates in the air supply pipe 5 below the three-way cock 8. When the three-way cock 8 is switched to the previous position again in a state in which the chemical is almost completely filled in the air supply pipe 5, the chemical stored in the air supply pipe 5 is ejected from the air ejection hole 3 together with the air, and Particles of pollutants such as sludge that have adhered to the surroundings are dissolved and removed by the chemical solution, and clogging is cleaned.

【0030】また、エア噴出孔3から噴出する薬液は、
好気性処理槽1内を上昇しながら、気泡の攪拌作用によ
って膜モジュール9の外面に充分接触し、付着していた
汚濁物質の粒子が溶解され除去されて、目詰まりが清掃
される。
The chemical liquid ejected from the air ejection holes 3 is
While rising in the aerobic treatment tank 1, the bubbles are sufficiently brought into contact with the outer surface of the membrane module 9 by the stirring action of the bubbles, and the attached pollutant particles are dissolved and removed, and the clogging is cleaned.

【0031】このように、上記の汚水処理装置を用いる
ことにより、メンテナンスの度毎に膜モジュール9及び
散気装置2を引き上げてエア噴出孔3の目詰まりをブラ
シで清掃することなしに、任意の時期に三方コック8を
切り替えて、散気装置2のエア噴出孔3及び膜モジュー
ル9の目詰まりを清掃することができる。
As described above, by using the above-mentioned sewage treatment apparatus, the membrane module 9 and the air diffuser 2 are pulled up every time maintenance is performed, and the clogging of the air ejection holes 3 is not cleaned with a brush. By switching the three-way cock 8 at the time, the clogging of the air ejection holes 3 of the air diffuser 2 and the membrane module 9 can be cleaned.

【0032】以下に本発明の具体的な実施例について説
明する。 (実施例1)図1に示す構造及び下記に示す諸元を有す
る汚水理装置を用いて、散気装置及び膜モジュールの目
詰まり及びその清掃に関する実験を行った。 〔汚水処理装置の諸元〕 好気性処理槽1:容積1m3 ,最高水位における水深
1.8m 散気装置2:塩化ビニル製で直径2mmのエア噴出孔
3が20個穿設されたもの ブロア:風量60 l/分 送気管5:内径13mmの塩化ビニル管 薬液筒6:薬液面が好気性処理槽1の最高水位HL上
0.7mとなるように設置、なお薬液は次亜塩素酸ナト
リウム 薬液注入管7:内径13mmの塩化ビニル管 三方コック8:各接続部の直径13mmの塩化ビニル
製で、アクチュエータ駆動、好気性処理槽1の最高水位
HL上0.5mに設置
Hereinafter, specific embodiments of the present invention will be described. (Example 1) Using a sewage treatment apparatus having the structure shown in FIG. 1 and the following specifications, an experiment was conducted on clogging of an air diffuser and a membrane module and cleaning thereof. [Specifications of sewage treatment equipment] Aerobic treatment tank 1: volume 1 m 3 , water depth 1.8 m at maximum water level Diffuser 2: 20 air blow holes 3 made of vinyl chloride and 2 mm in diameter : Air volume 60 l / min Air supply pipe 5: Vinyl chloride pipe with 13 mm inner diameter Chemical liquid cylinder 6: Installed so that the chemical liquid level is 0.7 m above the maximum water level HL of the aerobic treatment tank 1, and the chemical liquid is sodium hypochlorite Chemical solution injection pipe 7: Vinyl chloride pipe with an inner diameter of 13 mm 3-way cock 8: Made of vinyl chloride with a diameter of 13 mm at each connection part, driven by an actuator, installed at 0.5 m above the maximum water level HL of the aerobic treatment tank 1

【0033】実験は、好気性処理槽1への流入量を1.
25m3 /日、膜モジュール9における膜透過水量(=
好気性処理槽1からの放流量)も1.25m3 /日に維
持しつつ、好気性処理槽1内のMLSS濃度を約150
00mg/lとなるように設定し、且つ6か月間この値
を維持するように調整して行った。
In the experiment, the amount of inflow into the aerobic treatment tank 1 was 1.
25 m 3 / day, the amount of permeated water in the membrane module 9 (=
The MLSS concentration in the aerobic treatment tank 1 was maintained at about 150 while maintaining the discharge flow rate from the aerobic treatment tank 1 at 1.25 m 3 / day.
It was set to be 00 mg / l and adjusted so as to maintain this value for 6 months.

【0034】実験開始6か月後に運転を停止し、散気装
置2を引き上げて目詰まりしているエア噴出孔3の数を
確認後、再度散気装置2を好気性処理槽1内に設置し
た。そして、図2に示すように、モジュールヘッダ93
が露出するように好気性処理槽1内の水位を下げ、三方
コック8を切り替え、薬液筒6内の薬液を薬液注入管7
から流下させ、三方コック8の下の送気管5に充満させ
た。それから再度三方コック8を切り替えてエア供給源
4からのエアの供給を開始し、三方コック8の下の送気
管5内の薬液を押し流し、更に10分間送気した後、好
気性処理槽1の運転を停止して散気装置2を引き上げ、
エア噴出孔3の目詰まり数を調べた。
After six months from the start of the experiment, the operation was stopped, the air diffuser 2 was pulled up, the number of clogged air ejection holes 3 was confirmed, and then the air diffuser 2 was installed in the aerobic treatment tank 1 again. did. Then, as shown in FIG.
The water level in the aerobic treatment tank 1 is lowered so that the liquid is exposed, the three-way cock 8 is switched, and the chemical in the chemical cylinder 6 is filled with the chemical injection pipe 7.
And the air supply pipe 5 below the three-way cock 8 was filled. Then, the three-way cock 8 is switched again to start the supply of air from the air supply source 4 to flush out the chemical solution in the air supply pipe 5 below the three-way cock 8, and to supply air for another 10 minutes. Stop the operation and pull up the air diffuser 2,
The number of clogging of the air ejection holes 3 was examined.

【0035】その後水位を元の状態まで戻し、膜モジュ
ール9を吸引して汚水を透過させ、吸引圧力を測定し
た。
Thereafter, the water level was returned to the original state, the membrane module 9 was sucked, and sewage was permeated, and the suction pressure was measured.

【0036】以上の結果、実験開始6か月後におけるエ
ア噴出孔3の目詰まり数は5個であったが、薬液による
エア噴出孔3の洗浄後、目詰まりは見られなかった。ま
た、実験開始6か月後における膜モジュール9の吸引圧
力は−0.45kgf/cm2 であったが、薬液による
膜モジュール9の洗浄後は−0.12kgf/cm2
で回復した。
As a result, the number of clogging of the air ejection holes 3 was 6 months after the start of the experiment, but no clogging was observed after the cleaning of the air ejection holes 3 with the chemical solution. In addition, the suction pressure of the membrane module 9 was −0.45 kgf / cm 2 six months after the start of the experiment, but recovered to −0.12 kgf / cm 2 after the cleaning of the membrane module 9 with the chemical solution.

【0037】(比較例)図3に示す構造の汚水処理装置
を用いて、散気装置及び膜モジュールの目詰まり及びそ
の清掃に関する実験を行った。比較例においては、薬液
によるエア噴出孔cの洗浄を行わず、且つ、薬液筒fの
出口に設けた送液ポンプpによって膜モジュールiの内
面から圧力をかけて薬液を注入し洗浄する以外は、基本
的に実施例と同じ方法により実験を行った。
(Comparative Example) An experiment on clogging and cleaning of the air diffuser and the membrane module was performed using the sewage treatment apparatus having the structure shown in FIG. In the comparative example, except that the cleaning of the air ejection port c was not performed by the chemical solution, and the chemical solution was injected from the inner surface of the membrane module i by the liquid feed pump p provided at the outlet of the chemical solution tube f to perform the cleaning. An experiment was basically performed in the same manner as in the example.

【0038】その結果、実験開始6か月後における散気
装置bのエア噴出孔cの目詰まり数は5個であった。し
かし、この汚水処理装置はエア噴出孔cを洗浄するため
の洗浄装置を有しないので、ブラシを用いてエア噴出孔
cを清掃した。そのためエア噴出孔cの清掃に25分間
を要した。また、実験開始6か月後における膜モジュー
ルiの吸引圧力は−0.47kgf/cm2 であった
が、10分間の薬液による洗浄(逆洗)で−0.15k
gf/cm2 まで回復した。しかしながら、送液ポンプ
pを運転するための電力が必要であった。
As a result, the number of clogging of the air ejection port c of the air diffuser b was 5 at 6 months after the start of the experiment. However, since this sewage treatment apparatus does not have a cleaning device for cleaning the air ejection holes c, the air ejection holes c were cleaned using a brush. Therefore, it took 25 minutes to clean the air ejection port c. Further, the suction pressure of the membrane module i six months after the start of the experiment was -0.47 kgf / cm < 2 >, but after washing (backwashing) with a chemical solution for 10 minutes -0.15 kF.
gf / cm 2 . However, electric power for operating the liquid feed pump p was required.

【0039】以上の結果をまとめて表1に示す。Table 1 summarizes the above results.

【0040】[0040]

【表1】 [Table 1]

【0041】[0041]

【発明の効果】請求項1記載の本発明は上記のような構
成とされているので、膜モジュール及び散気装置を好気
性処理槽から引き上げる必要がなく、清掃作業のための
時間と工数が大幅に削減でき、且つ目詰まりをブラシで
こするという不衛生な作業がなくなり、作業環境が改善
される。
According to the first aspect of the present invention, as described above, the membrane module and the air diffuser do not need to be pulled out of the aerobic treatment tank, and the time and man-hour for the cleaning operation are reduced. The operation can be greatly reduced, and unsanitary work of rubbing clogs with a brush is eliminated, thereby improving the working environment.

【0042】また、薬液筒と好気性処理槽の液面の差に
より、薬液を送気管に自然流下させて散気装置のエア噴
出孔の目詰まりを洗浄することができ、従来技術のよう
に膜モジュールを逆洗するための送液ポンプ等を含む設
備費が不要となり、且つ洗浄のための運転費、メンテナ
ンス費も不要となる。
Also, due to the difference in liquid level between the chemical liquid cylinder and the aerobic treatment tank, the chemical liquid can flow naturally into the air supply pipe to clean the clogging of the air ejection holes of the air diffuser. Equipment costs including a liquid feed pump and the like for backwashing the membrane module are not required, and operation costs and maintenance costs for cleaning are also unnecessary.

【0043】請求項2記載の本発明は上記のような構成
とされているので、エアと薬液の切り替えを一動作で簡
単に行い、且つ自動化することができる。
According to the second aspect of the present invention, as described above, the switching between the air and the chemical can be easily performed in one operation and can be automated.

【0044】また、膜モジュール及び散気装置を好気性
処理槽から引き上げる必要がなく、清掃作業のための時
間と工数が大幅に削減でき、且つ目詰まりをブラシでこ
するという不衛生な作業がなくなり、作業環境が改善さ
れる。
Further, there is no need to lift the membrane module and the air diffuser from the aerobic treatment tank, so that the time and man-hour for cleaning work can be greatly reduced, and unsanitary work of rubbing clogging with a brush can be avoided. And the working environment is improved.

【0045】また、薬液筒と好気性処理槽の液面の差に
より、薬液を送気管に自然流下させて散気装置のエア噴
出孔の目詰まりを洗浄することができ、従来技術のよう
に膜モジュールを逆洗するための送液ポンプ等を含む設
備費が不要となり、且つ洗浄のための運転費、メンテナ
ンス費も不要となる。
Also, due to the difference in liquid level between the chemical liquid cylinder and the aerobic treatment tank, the chemical liquid can flow naturally to the air supply pipe to clean the clogging of the air ejection holes of the diffuser. Equipment costs including a liquid feed pump and the like for backwashing the membrane module are not required, and operation costs and maintenance costs for cleaning are also unnecessary.

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

【図1】本発明汚水処理装置の実施の形態を示す模式図
で、曝気により好気性処理を行っている状態。
FIG. 1 is a schematic diagram showing an embodiment of a sewage treatment apparatus of the present invention, in which aerobic treatment is being performed by aeration.

【図2】本発明汚水処理装置の実施の形態を示す模式図
で、曝気を中止して薬液による洗浄を行っている状態。
FIG. 2 is a schematic view showing an embodiment of the sewage treatment apparatus of the present invention, in which aeration is stopped and cleaning with a chemical is performed.

【図3】従来技術を示す模式図。FIG. 3 is a schematic view showing a conventional technique.

【符号の説明】[Explanation of symbols]

1 好気性処理槽 2 散気装置 3 エア噴出孔 4 エア供給源 5 送気管 6 薬液筒 7 薬液注入管 8 三方コック 9 膜モジュール 91 中空糸膜 DESCRIPTION OF SYMBOLS 1 Aerobic treatment tank 2 Air diffuser 3 Air ejection hole 4 Air supply source 5 Air supply tube 6 Chemical liquid tube 7 Chemical liquid injection tube 8 Three-way cock 9 Membrane module 91 Hollow fiber membrane

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 好気性処理槽を備えた汚水処理装置であ
って、エア供給源と散気装置とを連結する送気管と、好
気性処理槽内の液面より高い位置に置かれた薬液筒に連
結される薬液注入管とが連結されていることを特徴とす
る汚水処理装置。
1. A sewage treatment apparatus provided with an aerobic treatment tank, wherein an air supply pipe connecting an air supply source and a diffuser, and a chemical liquid placed at a position higher than a liquid level in the aerobic treatment tank. A sewage treatment apparatus, wherein a chemical solution injection pipe connected to a cylinder is connected.
【請求項2】 送気管と薬液注入管とが切替弁を介して
連結されていることを特徴とする請求項1記載の汚水処
理装置。
2. The sewage treatment apparatus according to claim 1, wherein the air supply pipe and the chemical liquid injection pipe are connected via a switching valve.
JP19848197A 1997-07-24 1997-07-24 Sewage treatment apparatus Withdrawn JPH1133582A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19848197A JPH1133582A (en) 1997-07-24 1997-07-24 Sewage treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19848197A JPH1133582A (en) 1997-07-24 1997-07-24 Sewage treatment apparatus

Publications (1)

Publication Number Publication Date
JPH1133582A true JPH1133582A (en) 1999-02-09

Family

ID=16391837

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19848197A Withdrawn JPH1133582A (en) 1997-07-24 1997-07-24 Sewage treatment apparatus

Country Status (1)

Country Link
JP (1) JPH1133582A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004008981A (en) * 2002-06-10 2004-01-15 Asahi Kasei Corp Membrane separation apparatus
JP2007136389A (en) * 2005-11-21 2007-06-07 Ngk Insulators Ltd Aeration device
CN116679021A (en) * 2023-06-06 2023-09-01 水利部交通运输部国家能源局南京水利科学研究院 Method and system for filling soluble marker in pollutant diffusion model

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004008981A (en) * 2002-06-10 2004-01-15 Asahi Kasei Corp Membrane separation apparatus
JP4530245B2 (en) * 2002-06-10 2010-08-25 旭化成ケミカルズ株式会社 Membrane separator
JP2007136389A (en) * 2005-11-21 2007-06-07 Ngk Insulators Ltd Aeration device
CN116679021A (en) * 2023-06-06 2023-09-01 水利部交通运输部国家能源局南京水利科学研究院 Method and system for filling soluble marker in pollutant diffusion model
CN116679021B (en) * 2023-06-06 2024-04-19 水利部交通运输部国家能源局南京水利科学研究院 Method and system for filling soluble marker in pollutant diffusion model

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