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JPH0722749B2 - Sewage treatment equipment - Google Patents
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JPH0722749B2 - Sewage treatment equipment - Google Patents

Sewage treatment equipment

Info

Publication number
JPH0722749B2
JPH0722749B2 JP1058703A JP5870389A JPH0722749B2 JP H0722749 B2 JPH0722749 B2 JP H0722749B2 JP 1058703 A JP1058703 A JP 1058703A JP 5870389 A JP5870389 A JP 5870389A JP H0722749 B2 JPH0722749 B2 JP H0722749B2
Authority
JP
Japan
Prior art keywords
filtration chamber
filtration
treatment tank
activated sludge
membrane module
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.)
Expired - Lifetime
Application number
JP1058703A
Other languages
Japanese (ja)
Other versions
JPH02237693A (en
Inventor
秀樹 岩部
昌継 山縣
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 JP1058703A priority Critical patent/JPH0722749B2/en
Publication of JPH02237693A publication Critical patent/JPH02237693A/en
Publication of JPH0722749B2 publication Critical patent/JPH0722749B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、限外ろ過膜を備えた汚水処理装置に関するも
のである。
TECHNICAL FIELD The present invention relates to a sewage treatment apparatus provided with an ultrafiltration membrane.

従来の技術 従来のこの種の汚水処理装置においては、たとえば第8
図および第9図に示すように、活性汚泥処理槽1内に設
けられた取付け板2に、限外ろ過膜を備えた円筒状の膜
モジュール3が水平方向に複数列(図中のものは4
列)、かつ、上下方向に複数段(図中のものは3段)配
置されるとともに、処理槽1の底部に膜モジュール3の
各列ごとに散気管4が設けられている。また、膜モジュ
ール3の各列ごとに、ポンプ5と送風機6とが設けら
れ、ポンプ5は各列の膜モジュール3の排出口側に接続
され、送風機6は各散気管4に接続されている。
2. Description of the Related Art In a conventional wastewater treatment device of this type, for example,
As shown in FIG. 9 and FIG. 9, a cylindrical membrane module 3 having an ultrafiltration membrane is horizontally arranged in a plurality of rows on a mounting plate 2 provided in an activated sludge treatment tank 1 (in the figure, Four
Columns) and a plurality of stages (three stages in the figure) are arranged in the vertical direction, and the diffusion tubes 4 are provided at the bottom of the treatment tank 1 for each column of the membrane module 3. A pump 5 and a blower 6 are provided for each row of the membrane module 3, the pump 5 is connected to the outlet side of the membrane module 3 in each row, and the blower 6 is connected to each air diffuser 4. .

そして、汚水は、活性汚泥処理槽1内に供給され、槽内
の活性汚泥と混合して混合溶液7を形成し、活性汚泥中
に含まれた微生物により酸化分解処理される。一方、散
気管4は、送風機6から曝気用空気が供給され、これを
気泡として混合溶液7中に吹き出すことにより、混合溶
液7中の微生物に増殖用酸素を供給するとともに、混合
溶液7に上向きの水流を発生させ、混合溶液7を第8図
の矢印方向に循環させる。この混合溶液7は、膜モジュ
ール3を介してポンプ5により吸引され、膜モジュール
3により濃縮液と清浄な処理水とにろ過分離される。濃
縮液は槽内に残って上昇循環し、処理水は槽外に排出さ
れる。その際、濃縮液中の固形分(いわゆるS.S.)の一
部が膜モジュール3の表面にスケールとして付着する。
このスケールは、混合溶液7の上向きの水流により一部
が除去されるが、残部は徐々に生長して膜モジュール3
の限外ろ過膜を目詰りさせるので、膜モジュール3を定
期的に薬品洗浄することにより残部のスケールを除去し
ている。
Then, the sewage is supplied into the activated sludge treatment tank 1, mixed with the activated sludge in the tank to form a mixed solution 7, and oxidatively decomposed by the microorganisms contained in the activated sludge. On the other hand, the air diffuser 4 is supplied with aeration air from the blower 6 and blows it out as air bubbles into the mixed solution 7, thereby supplying oxygen for growth to the microorganisms in the mixed solution 7 and upwardly flowing into the mixed solution 7. Is generated, and the mixed solution 7 is circulated in the direction of the arrow in FIG. The mixed solution 7 is sucked by the pump 5 through the membrane module 3 and is filtered and separated into concentrated liquid and clean treated water by the membrane module 3. The concentrated liquid remains in the tank and circulates upward, and the treated water is discharged to the outside of the tank. At that time, part of the solid content (so-called SS) in the concentrated liquid adheres to the surface of the membrane module 3 as a scale.
A part of this scale is removed by the upward water flow of the mixed solution 7, but the rest gradually grows and the membrane module 3
Since the ultrafiltration membrane of (3) is clogged, the remaining scale is removed by periodically cleaning the membrane module 3 with a chemical.

発明が解決しようとする課題 しかし、上記従来の汚水処理装置においては、薬品洗浄
のとき、薬品を直接活性汚泥処理槽1内に入れると活性
汚泥微生物が死滅してしまう。また、洗浄のために設備
の運転を全面的に休止することは許されない。したがっ
て、薬品洗浄は、膜モジュール3を一列づつ等単位ごと
槽外に取り出して行なうことが必要になり、そのため、
作業能率が悪く、また、大型の設備には適しないという
問題があった。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention However, in the above conventional sewage treatment apparatus, when the chemical is directly introduced into the activated sludge treatment tank 1 during the chemical cleaning, the activated sludge microorganisms are killed. Moreover, it is not allowed to suspend the operation of the equipment for cleaning. Therefore, it is necessary to take out the membrane modules 3 out of the tank in units such as row by row for chemical cleaning.
There was a problem that work efficiency was poor and it was not suitable for large-scale equipment.

本発明は、従来の汚水処理装置を改良して、このような
問題点を解消することを目的とする。
An object of the present invention is to improve a conventional wastewater treatment device and solve such a problem.

課題を解決するための手段 上記目的を達成するために、本発明の汚水処理装置は、
活性汚泥処理槽とろ過処理槽とが互いに分離して設けら
れ、各ろ過処理槽内が仕切壁により複数列のろ過室に分
離され、各ろ過室の上下両部が仕切装置を備えた連通路
を介して活性汚泥処理槽の上下両部にそれぞれ接続さ
れ、各ろ過室内に複数の膜モジュールが配置され、各ろ
過室の底部に、このろ過室内に曝気用空気を供給させる
とともに、この曝気用空気の気泡流によってろ過室内に
上向きの水流を発生させてこの水流を前記上下の連通路
を介して活性汚泥処理槽とろ過室とに循環させる散気管
が設けられている構成としたものである。
Means for Solving the Problems In order to achieve the above object, the sewage treatment apparatus of the present invention,
An activated sludge treatment tank and a filtration treatment tank are provided separately from each other, the inside of each filtration treatment tank is divided into a plurality of rows of filtration chambers by partition walls, and the upper and lower parts of each filtration chamber are provided with a partition passage. Is connected to the upper and lower parts of the activated sludge treatment tank respectively, and a plurality of membrane modules are arranged in each filtration chamber, and the aeration air is supplied to the bottom of each filtration chamber and this aeration An air diffusing pipe is provided for generating an upward water flow in the filtration chamber by the bubble flow of air and circulating this water flow between the activated sludge treatment tank and the filtration chamber through the upper and lower communication passages. .

作用 上記本発明の構成においては、汚水は、活性汚泥処理槽
内に供給され、槽内の活性汚泥と混合して混合溶液を形
成し、活性汚泥中に含まれた微生物により酸化分解処理
される。一方、散気管は、送風機から曝気用空気を供給
され、気泡として各ろ過室内の混合溶液中に吹き出すこ
とにより、混合溶液中の微生物に増殖用酸素を供給する
とともに、混合溶液に上向きの水流を発生する。この混
合溶液は、ろ過室内を上昇し、上部の連通管もしくは堰
等の連通路を経由して活性汚泥処理槽内に流入し、活性
汚泥処理槽内の混合溶液と混合して下降し、下部の連通
路を経由して各ろ過室内に流入することにより、活性汚
泥処理槽とろ過処理槽との間を循環する。このため、活
性汚泥処理槽はもちろんのこと、これに加えてろ過処理
槽においても生物処理機能が付与されることになり、生
物処置に関しては併設されたこれら活性汚泥処理槽とろ
過処理槽との各々が処理を分担することになって、各々
の容量比や循環液量などを処理目的に応じて調整・制御
することが可能となる。そして、この混合溶液は、各ろ
過室内を上昇するとき、膜モジュールを介してポンプに
より吸引され、膜モジュールにより濃縮液と清浄な処理
水とにろ過分離される。濃縮液はろ過室内に残って混合
溶液とともに上昇循環し、処理水は膜モジュール内を経
由してろ過室外に取り出される。上記ろ過分離の際、膜
モジュールの表面に付着したスケールは、混合溶液の上
向きの水流により一部が除去されるが、残部は次に説明
するような定期的なろ過室ごとの薬品洗浄により除去さ
れる。
Action In the configuration of the present invention, sewage is supplied into the activated sludge treatment tank, mixed with the activated sludge in the tank to form a mixed solution, and oxidatively decomposed by the microorganisms contained in the activated sludge. . On the other hand, the air diffuser is supplied with aeration air from a blower and blows out as air bubbles into the mixed solution in each filtration chamber, thereby supplying oxygen for growth to the microorganisms in the mixed solution and causing an upward water flow to the mixed solution. Occur. This mixed solution ascends in the filtration chamber, flows into the activated sludge treatment tank through a communication passage such as an upper communication pipe or a weir, mixes with the mixed solution in the activated sludge treatment tank, and descends. By flowing into each of the filtration chambers via the communication passage of, the circulation between the activated sludge treatment tank and the filtration treatment tank is achieved. Therefore, not only the activated sludge treatment tank but also the filtration treatment tank will be provided with a biological treatment function. For biological treatment, the activated sludge treatment tank and the filtration treatment tank will be installed side by side. Since each of them will share the processing, it becomes possible to adjust and control the respective volume ratio, circulating liquid amount, etc. according to the processing purpose. Then, when the mixed solution rises in each filtration chamber, it is sucked by the pump through the membrane module, and is filtered and separated into a concentrated liquid and clean treated water by the membrane module. The concentrated liquid remains in the filtration chamber and ascends and circulates together with the mixed solution, and the treated water is taken out of the filtration chamber via the inside of the membrane module. During the above-mentioned filtration separation, the scale attached to the surface of the membrane module is partially removed by the upward flow of the mixed solution, but the rest is removed by periodical chemical cleaning in each filtration chamber as described below. To be done.

すなわち、まず、洗浄しようとするろ過室と活性汚泥処
理槽との間の上下の連通路のバルブ等の仕切装置を閉じ
て、そのろ過室を活性汚泥処理槽からしゃ断し、他のろ
過室はそのままとして運転を継続しておく。次に、洗浄
しようとするろ過室内を水道水等で満たして水洗し、水
洗後の混合液を抜きとり、更に必要なら薬品槽に連通さ
せて洗浄液を入れ、洗浄ポンプにより洗浄液をろ過室と
薬品槽との間で循環させることにより膜モジュールを洗
浄し、洗浄が終わると上・下部のバルブ等の仕切装置を
開いて通常の運転状態にもどす。他のろ過室内の膜モジ
ュールも上記と同じ要領で洗浄するのである。このよう
に、本発明の構成によれば、設備の運転を全面的に休止
することなく、かつ、膜モジュールを取り外すことな
く、膜モジュールの薬品洗浄が可能である。
That is, first, a partition device such as a valve in the upper and lower communication passages between the filtration chamber to be cleaned and the activated sludge treatment tank is closed, the filtration chamber is shut off from the activated sludge treatment tank, and the other filtration chambers are Leave it as it is and continue operation. Next, the filter chamber to be cleaned is filled with tap water and rinsed with water, the mixed liquid after the rinse is drained, and if necessary, the cleaning liquid is put into the chemical tank and the cleaning liquid is put into the filter chamber and chemicals by a cleaning pump. The membrane module is washed by circulating it with the tank, and when the washing is completed, the partitioning devices such as the upper and lower valves are opened to return to the normal operating state. The membrane modules in the other filtration chambers are also washed in the same manner as above. As described above, according to the configuration of the present invention, chemical cleaning of the membrane module is possible without completely stopping the operation of the equipment and without removing the membrane module.

実施例 以下、本発明の実施例を第1図〜第7図に基づいて説明
する。
Embodiment An embodiment of the present invention will be described below with reference to FIGS. 1 to 7.

本実施例の汚水処理装置は、第1図および第2図に示す
ように、活性汚泥処理槽11とろ過処理槽12とを具備して
なるものである。ろ過処理槽12は、内部が仕切壁13によ
り複数列(図中のものは4列)のろ過室14に分割されて
なり、各ろ過室14内の上下両部が仕切装置としてのバル
ブ15を備えた連通路としての連通管16を介して活性汚泥
処理槽11内の上下両部にそれぞれ接続されている。各ろ
過室14内には、ろ過膜を備えた円筒状の膜モジュール17
が上下に複数段(図中のものは3段)積み重ねられると
ともに、底部に散気管18が設けられている。さらに、各
ろ過室14ごとに、ポンプ19と送風機20とが設けられ、ポ
ンプ19は各ろ過室14内の膜モジュール17の取り出し口側
に接続され、送風機20は各散気管18に接続されている。
The sewage treatment apparatus of this embodiment comprises an activated sludge treatment tank 11 and a filtration treatment tank 12, as shown in FIGS. 1 and 2. The inside of the filtration treatment tank 12 is divided by a partition wall 13 into a plurality of rows (four rows in the figure) of filtration chambers 14, and both upper and lower parts of each filtration chamber 14 are provided with valves 15 as partitioning devices. It is connected to both upper and lower parts in the activated sludge treatment tank 11 via a communication pipe 16 provided as a communication passage. Inside each filtration chamber 14 is a cylindrical membrane module 17 with a filtration membrane.
Are stacked vertically (three in the figure) and an air diffuser 18 is provided at the bottom. Furthermore, a pump 19 and a blower 20 are provided for each filtration chamber 14, the pump 19 is connected to the outlet side of the membrane module 17 in each filtration chamber 14, and the blower 20 is connected to each air diffuser 18. There is.

次に、上記構成における作用について説明する。Next, the operation of the above configuration will be described.

汚水は、活性汚泥処理槽11内に供給され、槽内の活性汚
泥と混合して混合溶液21を形成し、活性汚泥中に含まれ
た微生物により酸化分解処理される。一方、散気管18
は、送風機20から曝気用空気を供給され、気泡として各
ろ過室14内の混合溶液21中に吹き出すことにより、混合
溶液21中の微生物に増殖用酸素を供給するとともに、混
合溶液21に上向きの水流を発生する。この混合溶液21
は、ろ過室14内を上昇し、上部の連通管16を経由して活
性汚泥処理槽11内に流入し、活性汚泥処理槽11内の混合
溶液21と混合して下降し、下部の連通管16を経由して各
ろ過室14内に流入することにより、活性汚泥処理槽11と
ろ過処理槽12との間で第1図中の矢印方向に循環する。
このため、活性汚泥処理槽11はもちろんのこと、これに
加えてろ過処理槽12においても生物処理機能が付与され
ることになり、生物処理に関しては併設されたこれら活
性汚泥処理槽11とろ過処理槽12との各々が処理を分担す
ることになって、各々の容量比や循環液量などを処理目
的に応じて調整・制御することが可能となる。
Sewage is supplied into the activated sludge treatment tank 11, is mixed with the activated sludge in the tank to form a mixed solution 21, and is oxidatively decomposed by microorganisms contained in the activated sludge. Meanwhile, the air diffuser 18
Is supplied with aeration air from the blower 20, by blowing out into the mixed solution 21 in each filtration chamber 14 as air bubbles, while supplying oxygen for growth to the microorganisms in the mixed solution 21 and upward of the mixed solution 21. Generate a stream of water. This mixed solution 21
Rises in the filtration chamber 14, flows into the activated sludge treatment tank 11 via the upper communication pipe 16, mixes with the mixed solution 21 in the activated sludge treatment tank 11 and descends, and lower communication pipe By flowing into each filtration chamber 14 via 16, it circulates between the activated sludge treatment tank 11 and the filtration treatment tank 12 in the arrow direction in FIG.
Therefore, not only the activated sludge treatment tank 11, but also the filtration treatment tank 12 is provided with a biological treatment function, and regarding the biological treatment, these activated sludge treatment tanks 11 and the filtration treatment are provided together. Since each of the tanks 12 will share the processing, it becomes possible to adjust and control the volume ratio of each, the amount of circulating liquid, etc. according to the processing purpose.

そして、この混合溶液21は、各ろ過室14内を上昇すると
き、膜モジュール17を介してポンプ19により吸引され、
膜モジュール17により濃縮液と清浄な処理水とにろ過分
離される。濃縮液はろ過室14内に残って混合溶液21とと
もに上昇循環し、処理水は膜モジュール17内を経由して
ろ過室14外に取り出される。上記ろ過分離の際、膜モジ
ュール17の表面に付着したスケールは、混合溶液21の上
向きの水流により一部が除去されるが、残部は定期的な
ろ過室14ごとの薬品洗浄により除去する。この薬品洗浄
には、次に説明するような二つの方法がある。
Then, the mixed solution 21 is sucked by the pump 19 through the membrane module 17 when rising in each filtration chamber 14,
The membrane module 17 filters and separates the concentrated liquid and the clean treated water. The concentrated liquid remains in the filtration chamber 14 and ascends and circulates together with the mixed solution 21, and the treated water is taken out of the filtration chamber 14 via the inside of the membrane module 17. At the time of the filtration separation, part of the scale attached to the surface of the membrane module 17 is removed by the upward water flow of the mixed solution 21, but the rest is removed by periodic chemical cleaning of each filtration chamber 14. This chemical cleaning has two methods as described below.

第1の洗浄方法では、まず、洗浄しようとするろ過室14
と活性汚泥処理槽11との間の上下両連通管16のバルブ15
を閉じて、そのろ過室14を活性汚泥処理槽11からしゃ断
し、そのろ過室14内の液を抜きとり空とするために、ろ
過室14の底部に備えつけられたパイプ、31のバルブ28を
開く。全部液を抜とり後再び閉める。更に、膜モジュー
ル17を薬品洗浄する前に、水洗を行うために、水道水供
給管30のバルブ29を開きろ過室14を水道水で満たした後
ブロワー20より空気を送り膜モジュールを水洗する。そ
の後ブロワー20を止め洗浄水を前と同様に引き抜く他の
ろ過室14はそのままとして運転を継続しておく。次に、
第3図に示すように、洗浄しようとするろ過室14と薬品
槽22との底部どうしを薬品用連通管23により接続すると
ともに、そのろ過室14内の膜モジュール17の取り出し口
側に洗浄ポンプ24を接続し、洗浄ポンプ24の吐出管25を
薬品槽22にもどしておく。
In the first cleaning method, first, the filtration chamber 14 to be cleaned is
Between the upper and lower communication pipes 16 between the activated sludge treatment tank 11 and the activated sludge treatment tank 11
To shut off the filtration chamber 14 from the activated sludge treatment tank 11, and to remove the liquid in the filtration chamber 14 and empty it, a pipe provided at the bottom of the filtration chamber 14 and a valve 28 of 31 are installed. open. Remove all liquid and close again. Further, before washing the membrane module 17 with chemicals, the valve 29 of the tap water supply pipe 30 is opened to fill the filtration chamber 14 with tap water, and then air is sent from the blower 20 to wash the membrane module. After that, the blower 20 is stopped, and the washing water is drawn out as in the previous case, and the other filtration chamber 14 is left as it is and the operation is continued. next,
As shown in FIG. 3, the bottoms of the filtration chamber 14 and the chemical tank 22 to be cleaned are connected to each other by a chemical communication pipe 23, and a cleaning pump is provided on the outlet side of the membrane module 17 in the filtration chamber 14. 24 is connected, and the discharge pipe 25 of the cleaning pump 24 is returned to the chemical tank 22.

このようにした後に薬品槽22からの洗浄液をろ過室14の
内部に満たし、洗浄ポンプ24を運転すると、ろ過室14内
の洗浄液26は、洗浄ポンプ24により第4図の矢印A方向
に膜モジュール17内に吸引され、吐出管25から薬品槽22
内にもどる。薬品槽22内の洗浄液26は連通管23を経由し
てろ過室14内に流入する。このようにして、洗浄液26
は、ろ過室14と薬品槽22との間を循環しながら膜モジュ
ール17の内外両面を洗浄する。なお、洗浄液26を上記と
逆の方向に循環させ、膜モジュール17を第4図の矢印B
方向にいわゆる逆洗することも可能である。洗浄が終わ
るとろ過室14を元の運転状態にもどし、他のろ過室14内
の膜モジュール17を上記と同じ要領で洗浄するのであ
る。
After this, when the cleaning liquid from the chemical tank 22 is filled in the filtration chamber 14 and the cleaning pump 24 is operated, the cleaning liquid 26 in the filtration chamber 14 is moved by the cleaning pump 24 in the direction of arrow A in FIG. It is sucked into 17 and discharged from the pipe 25 to the chemical tank 22.
Return to inside. The cleaning liquid 26 in the chemical tank 22 flows into the filtration chamber 14 via the communication pipe 23. In this way, the cleaning liquid 26
Cleans both the inner and outer surfaces of the membrane module 17 while circulating between the filtration chamber 14 and the chemical tank 22. In addition, the cleaning liquid 26 is circulated in the direction opposite to the above, and the membrane module 17 is moved to the arrow B in FIG.
It is also possible to carry out a so-called backwash in the direction. When the washing is completed, the filtration chamber 14 is returned to the original operating state, and the membrane module 17 in the other filtration chamber 14 is washed in the same manner as above.

また、第2の洗浄方法では、まず、第1の方法と同様に
して、洗浄しようとするろ過室14を活性汚泥処理槽11か
らしゃ断し、他のろ過室14はそのままとして運転を継続
しておく。次に、第5図に示すように、洗浄しようとす
るろ過室14と薬品槽22との底部どうしを洗浄ポンプ24を
備えた薬品用連通管23により接続するとともに、そのろ
過室14内の最上段の膜モジュール17よりも若干上部にオ
ーバーフロー管27の一端部を接続し、他端部を薬品槽22
にもどしておく。次に、薬品槽22から洗浄しようとする
ろ過室14内に洗浄液26を入れ、洗浄ポンプ24を運転す
る。
Further, in the second cleaning method, first, in the same manner as the first method, the filtration chamber 14 to be cleaned is cut off from the activated sludge treatment tank 11, and the other filtration chambers 14 are left as they are to continue the operation. deep. Next, as shown in FIG. 5, the bottoms of the filtration chamber 14 and the chemical tank 22 to be cleaned are connected to each other by a chemical communication pipe 23 equipped with a cleaning pump 24, and the innermost portion of the filtration chamber 14 is cleaned. One end of the overflow pipe 27 is connected slightly above the upper membrane module 17, and the other end is connected to the chemical tank 22.
I will put it back. Next, the cleaning liquid 26 is put into the filtration chamber 14 to be cleaned from the chemical tank 22, and the cleaning pump 24 is operated.

すると、薬品槽22内の洗浄液26は連通管23を経由してろ
過室14内に流入する。そのため、ろ過室14の洗浄液26
は、液面が上昇し、オーバーフロー管27から流出して薬
品槽22内にもどる。このようにして、洗浄液26は、ろ過
室14と薬品槽22との間を循環しながら、膜モジュール17
の表面を洗浄する。その際、洗浄液26の一部は、第6図
に示すように、膜モジュール17の表面から内部にしみ込
むことによりこの膜モジュール17を洗浄する作用もす
る。洗浄が終わるとろ過室14を元の運転状態にもどし、
他のろ過室14内の膜モジュールを上記と同じ要領で洗浄
するのである。なお、この洗浄方法と第1の洗浄方法と
を併用してもよい。
Then, the cleaning liquid 26 in the chemical tank 22 flows into the filtration chamber 14 via the communication pipe 23. Therefore, the cleaning liquid 26 in the filtration chamber 14
The liquid level rises, flows out from the overflow pipe 27, and returns to the inside of the chemical tank 22. In this way, the cleaning liquid 26 is circulated between the filtration chamber 14 and the chemical tank 22 while the membrane module 17 is being circulated.
Wash the surface of the. At that time, as shown in FIG. 6, a part of the cleaning liquid 26 also functions to clean the membrane module 17 by soaking it in from the surface of the membrane module 17 to the inside. After cleaning, return the filtration chamber 14 to its original operating condition,
The membrane module in the other filtration chamber 14 is washed in the same manner as above. Note that this cleaning method and the first cleaning method may be used together.

上記のように、本実施例の構成によれば、いずれの洗浄
方法によっても、汚水処理のための設備の運転を全面的
に休止することなく、かつ、膜モジュール17を取り外す
ことなく、この膜モジュール17の薬品洗浄が可能であ
る。
As described above, according to the configuration of the present embodiment, by any cleaning method, without completely stopping the operation of the equipment for wastewater treatment, and without removing the membrane module 17, this membrane Module 17 can be cleaned with chemicals.

第7図は、上部の連通路および仕切装置として、第1図
等に示した連通管16およびバルブ15に代えて、連通流路
33およびこの流路に設けられた堰32を利用したものを示
す。
FIG. 7 shows an upper communication passage and a partition device, instead of the communication pipe 16 and the valve 15 shown in FIG.
33 and a weir 32 provided in this flow path are shown.

発明の効果 本発明は、以上説明したように、活性汚泥処理槽とろ過
処理槽とを互いに分離して設け、ろ過処理槽内を複数列
のろ過室に分割し、各ろ過室と活性汚泥処理槽との間を
連通・しゃ断可能とし、各ろ過室内に膜モジュールを設
けた構成としたので、設備の運転を全面的に休止するこ
となく、かつ、膜モジュールを取り外すことなく、膜モ
ジュールの薬品洗浄が可能である。したがって、大形の
設備にも好適に使用することができる。のみならず、各
ろ過室の上下両部を連通路を介して活性汚泥処理槽の上
下両部にそれぞれ接続したため、散気管から供給される
曝気用空気だけによって、活性汚泥処理槽とろ過室とを
循環する水流を発生させることができ、しかも、活性汚
泥処理槽はもちろんのこと、これに加えてろ過処理槽に
おいても生物処理機能を付与させることができ、生物処
理に関しては併設されたこれら活性汚泥処理槽とろ過処
理槽との各々に処理を分担させることが可能となって、
各々の容量比や循環液量などを処理目的に応じて調整・
制御することができる。
As described above, the present invention provides the activated sludge treatment tank and the filtration treatment tank separately from each other, and divides the inside of the filtration treatment tank into a plurality of rows of filtration chambers, and each filtration chamber and the activated sludge treatment. The membrane module is configured so that it can communicate with and cut off from the tank, and the membrane module is installed in each filtration chamber, so the chemicals of the membrane module can be removed without completely stopping the operation of the equipment and without removing the membrane module. Can be washed. Therefore, it can be suitably used for large-scale equipment. Not only that, because the upper and lower parts of each filtration chamber were connected to the upper and lower parts of the activated sludge treatment tank through the communication passage, respectively, the activated sludge treatment tank and the filtration chamber were It is possible to generate a water flow that circulates, and in addition to the activated sludge treatment tank, it is possible to add a biological treatment function to the filtration treatment tank. It becomes possible to share the treatment in each of the sludge treatment tank and the filtration treatment tank,
Adjust each volume ratio and circulating fluid amount according to the processing purpose.
Can be controlled.

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

第1図は本発明の一実施例を示す汚水処理装置の断面
図、第2図は第1図の装置の平面図、第3図は本発明に
おける膜モジュールの薬品洗浄方法の一実施例を示す一
部切欠図、第4図は第3図における膜モジュールの洗浄
状態を示す説明図、第5図は本発明における膜モジュー
ルの薬品洗浄方法の他の実施例を示す部分断面図、第6
図は第5図における膜モジュールの洗浄状態を示す説明
図、第7図は上部仕切装置が堰である場合を例示する断
面図、第8図は従来の汚水処理装置の一例を示す断面
図、第9図は第8図の装置の平面図である。 11……活性汚泥処理槽、12……ろ過処理槽、13……仕切
壁、14……ろ過室、15……バルブ(仕切装置)、16……
連通管(連通路)、17……膜モジュール、18……散気
管、32……堰(仕切装置)、33……連通流路(連通
路)。
FIG. 1 is a sectional view of a sewage treatment apparatus showing an embodiment of the present invention, FIG. 2 is a plan view of the apparatus of FIG. 1, and FIG. 3 is an embodiment of a chemical cleaning method for a membrane module according to the present invention. Partially cutaway view, FIG. 4 is an explanatory view showing a cleaning state of the membrane module in FIG. 3, FIG. 5 is a partial cross-sectional view showing another embodiment of the chemical cleaning method for the membrane module in the present invention, and FIG.
5 is an explanatory view showing a cleaning state of the membrane module in FIG. 5, FIG. 7 is a cross-sectional view illustrating a case where the upper partition device is a weir, and FIG. 8 is a cross-sectional view showing an example of a conventional wastewater treatment device, FIG. 9 is a plan view of the device of FIG. 11 …… Activated sludge treatment tank, 12 …… Filtration treatment tank, 13 …… Partition wall, 14 …… Filtration chamber, 15 …… Valve (partitioning device), 16 ……
Communication pipe (communication passage), 17 ... Membrane module, 18 ... Air diffusion pipe, 32 ... Weir (partitioning device), 33 ... Communication passage (communication passage).

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】活性汚泥処理槽とろ過処理槽とが互いに分
離して設けられ、ろ過処理槽が仕切壁により複数列のろ
過室に分割され、各ろ過室の上下両部が仕切装置を備え
た連通路を介して活性汚泥処理槽の上下両部にそれぞれ
接続され、各ろ過室内に複数の膜モジュールが配置さ
れ、各ろ過室の底部に、このろ過室内に曝気用空気を供
給させるとともに、この曝気用空気の気泡流によってろ
過室内に上向きの水流を発生させてこの水流を前記上下
の連通路を介して活性汚泥処理槽とろ過室とに循環させ
る散気管が設けられていることを特徴とする汚水処理装
置。
1. An activated sludge treatment tank and a filtration treatment tank are provided separately from each other, and the filtration treatment tank is divided into a plurality of rows of filtration chambers by partition walls, and both upper and lower parts of each filtration chamber are equipped with partitioning devices. Connected to the upper and lower parts of the activated sludge treatment tank respectively, a plurality of membrane modules are arranged in each filtration chamber, while supplying aeration air into the filtration chamber at the bottom of each filtration chamber, An air diffuser is provided to generate an upward water flow in the filtration chamber by the bubble flow of the aeration air and to circulate the water flow between the activated sludge treatment tank and the filtration chamber through the upper and lower communication passages. Sewage treatment equipment to be.
JP1058703A 1989-03-10 1989-03-10 Sewage treatment equipment Expired - Lifetime JPH0722749B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1058703A JPH0722749B2 (en) 1989-03-10 1989-03-10 Sewage treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1058703A JPH0722749B2 (en) 1989-03-10 1989-03-10 Sewage treatment equipment

Publications (2)

Publication Number Publication Date
JPH02237693A JPH02237693A (en) 1990-09-20
JPH0722749B2 true JPH0722749B2 (en) 1995-03-15

Family

ID=13091877

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1058703A Expired - Lifetime JPH0722749B2 (en) 1989-03-10 1989-03-10 Sewage treatment equipment

Country Status (1)

Country Link
JP (1) JPH0722749B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2023037886A1 (en) * 2021-09-10 2023-03-16

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02293092A (en) * 1989-05-02 1990-12-04 Kubota Corp Sewage treatment equipment
JPH04305287A (en) * 1991-04-01 1992-10-28 Kubota Corp Water treating equipment
JP2782566B2 (en) * 1991-12-27 1998-08-06 株式会社 荏原製作所 Membrane filtration device
JP2003513785A (en) * 1999-11-18 2003-04-15 ゼノン、エンバイロンメンタル、インコーポレーテッド Immersion type membrane filtration system and overflow treatment method
JP4544765B2 (en) * 2001-03-05 2010-09-15 株式会社クボタ Reaction tank structure
JP4336143B2 (en) * 2003-05-27 2009-09-30 ヤンマー株式会社 Portable sewage treatment device and construction method of this portable sewage treatment device
JP4776381B2 (en) * 2006-01-26 2011-09-21 株式会社神鋼環境ソリューション Combined filtration device of media filtration pond and membrane filtration device
JP5049929B2 (en) * 2007-09-27 2012-10-17 株式会社神鋼環境ソリューション Water treatment apparatus and water treatment method
JP5512978B2 (en) * 2008-03-14 2014-06-04 東洋エンジニアリング株式会社 Waste water treatment method and waste water treatment apparatus
JP5126153B2 (en) * 2009-04-22 2013-01-23 住友電気工業株式会社 Membrane separation activated sludge treatment equipment
JP2011200751A (en) * 2010-03-24 2011-10-13 Toyo Eng Corp Membrane module cleaning system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2023037886A1 (en) * 2021-09-10 2023-03-16

Also Published As

Publication number Publication date
JPH02237693A (en) 1990-09-20

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