JP2553911Y2 - Sewage septic tank - Google Patents

Sewage septic tank

Info

Publication number
JP2553911Y2
JP2553911Y2 JP5147891U JP5147891U JP2553911Y2 JP 2553911 Y2 JP2553911 Y2 JP 2553911Y2 JP 5147891 U JP5147891 U JP 5147891U JP 5147891 U JP5147891 U JP 5147891U JP 2553911 Y2 JP2553911 Y2 JP 2553911Y2
Authority
JP
Japan
Prior art keywords
tank
water
membrane module
suction
treated water
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 - Fee Related
Application number
JP5147891U
Other languages
Japanese (ja)
Other versions
JPH04134492U (en
Inventor
八郎 佐藤
丈衛 佐藤
広佳 中島
大 原田
良人 北井
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 JP5147891U priority Critical patent/JP2553911Y2/en
Publication of JPH04134492U publication Critical patent/JPH04134492U/en
Application granted granted Critical
Publication of JP2553911Y2 publication Critical patent/JP2553911Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】この考案は嫌気ろ床槽または沈殿
分離槽、接触ばっ気槽や活性汚泥槽のような好気処理槽
および消毒槽を備え、かつ前記好気処理槽内に処理水を
吸引分離する膜モジュールを設けた汚水浄化槽に関す
る。
This invention comprises an aerobic treatment tank such as an anaerobic filter tank or a sedimentation separation tank, a contact aeration tank or an activated sludge tank, and a disinfecting tank. The present invention relates to a sewage purification tank provided with a membrane module for sucking and separating water.

【0002】[0002]

【従来の技術】従来から合併浄化槽などの汚水浄化槽と
して、嫌気ろ床槽または沈殿分離槽、接触ばっ気槽や活
性汚泥槽のような好気処理槽および消毒槽を備え、汚水
を順次移流させつつ生物学的作用により浄化していくも
のが知られている。また、図2図3に示すように好気処
理槽(図示例は接触ばっき槽)Aにセラミック材料等か
らなる微細多孔質膜からなる膜モジュールBを設けて吸
引ポンプCにより膜モジュールBを通して処理水を吸引
分離し、消毒槽D等に送り込む吸引式膜分離型汚水浄化
槽も知られている。
2. Description of the Related Art Conventionally, sewage purification tanks such as merged purification tanks have been provided with anaerobic filter tanks or sedimentation separation tanks, aerobic treatment tanks such as contact aeration tanks and activated sludge tanks, and disinfection tanks. While purifying by biological action is known. Also, as shown in FIGS. 2 and 3, a membrane module B made of a microporous membrane made of a ceramic material or the like is provided in an aerobic treatment tank (in the illustrated example, a contact tank), and the membrane module B is passed through a suction pump C. There is also known a suction type membrane separation type sewage purifying tank which separates treated water by suction and sends it to a disinfection tank D or the like.

【0003】[0003]

【従来技術の問題点】しかし、上記の吸引式膜分離型汚
水浄化槽では、処理水の吸引ろ過に伴って膜モジュール
Bが目詰まりを起こすため、定期的にエアを膜モジュー
ルB内に送って洗浄(いわゆる逆洗)を頻繁に行う必要
があり、その逆洗装置およびその動力装置の設置に費用
が掛かる欠点があった。
However, in the above-mentioned suction type membrane separation type sewage treatment tank, since the membrane module B is clogged with the suction filtration of the treated water, air is periodically sent into the membrane module B. Washing (so-called backwashing) has to be performed frequently, and there is a disadvantage in that the installation of the backwashing device and its power unit is expensive.

【0004】[0004]

【考案が解決しようとする課題】この考案は上記の問題
点に鑑み、動力を必要とせず、または最小限にして効果
的に膜モジュールの逆洗が行なえる汚水浄化槽を提供す
ることを目的としてなされたものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems, and has as its object to provide a sewage purifying tank which does not require power or minimizes the efficiency of backwashing of a membrane module. It was done.

【0005】[0005]

【課題を解決するための手段】即ち、この考案の汚水浄
化槽は、嫌気ろ床槽または沈殿分離槽、好気処理槽およ
び消毒槽を備え、好気処理槽内に処理水を吸引分離する
膜モジュールと、該膜モジュールを通して処理水を吸引
する吸引ポンプとが設けられ、また上記消毒槽に接触ば
っ気槽内の水位よりも高い位置で水位を確保するろ過水
槽が連設され、上記吸引ポンプから上記ろ過水槽へ吸引
処理水を揚水する配管が設けられ、かつ上記ろ過水槽が
上記消毒槽に処理水をオーバーフローさせるように構成
されてなることを特徴とするものである。
That is, the sewage purification tank of the present invention comprises an anaerobic filter bed tank or a sedimentation separation tank, an aerobic treatment tank and a disinfection tank, and a membrane for suctioning and separating treated water in the aerobic treatment tank. Module and a suction pump for sucking the treated water through the membrane module, and a filtration water tank for securing the water level at a position higher than the water level in the aeration tank in contact with the disinfecting tank is connected to the suction pump. And a pipe for pumping the suction treatment water from the filter water tank to the filtration water tank, and the filtration water tank is configured to overflow the treatment water into the disinfection tank.

【0006】[0006]

【実施例】次に、この考案の実施例を説明する。図1は
この考案の実施例の断面図である。すなわち、この考案
の汚水浄化槽1は、嫌気ろ床槽として嫌気ろ床第一室1
A、同第二室1B、接触ばっ気槽1Cおよび消毒槽1D
を備え、好気処理槽として接触ばっ気槽1Cに該槽内の
汚泥に散気用エアを供給する散気管2が装備されると共
に、接触ばっ気槽1C内の液を吸引できる高さ位置に槽
内処理水を吸引分離する膜モジュール、たとえばセラミ
ックメンブレン、あるいはガラス又はプラスチック製0.
1 〜60μm 目開きの微細多孔質管よりなる分離膜モジュ
ールなどの膜モジュール3と、該膜モジュール3を通し
て槽内処理液を吸引する吸引ポンプ4とが設けられ、か
つ上記消毒槽1Dに接触ばっ気槽1Cの水位よりも高い
位置に水位を確保するろ過水槽1Eが取り付けられ、上
記吸引ポンプ4によって吸引した処理液をろ過水槽1E
に揚水するように配管5がなされ、かつこの揚水された
処理液がろ過水槽1Eから消毒槽1Dにオーバーフロー
するように構成されている。なお、上記実施例に好気処
理槽として接触ばっ気槽1Cの場合を示したが、活性汚
泥処理槽としても同様に実施できる。この場合、膜モジ
ュール3は槽内処理水の上澄み液部分の高さに設けられ
る。
Next, an embodiment of the present invention will be described. FIG. 1 is a sectional view of an embodiment of the present invention. That is, the sewage purification tank 1 of this invention is an anaerobic filter first chamber 1 as an anaerobic filter tank.
A, the second chamber 1B, the contact aeration tank 1C and the disinfection tank 1D
The contact aeration tank 1C as an aerobic treatment tank is equipped with a diffuser pipe 2 for supplying air for diffusing air to the sludge in the tank, and a height position at which the liquid in the contact aeration tank 1C can be sucked. A membrane module that suction-separates the treated water in the tank, for example, a ceramic membrane, or glass or plastic.
A membrane module 3 such as a separation membrane module comprising a microporous tube having an opening of 1 to 60 μm and a suction pump 4 for sucking the processing solution in the tank through the membrane module 3 are provided, and are brought into contact with the disinfection tank 1D. A filtration water tank 1E for securing a water level higher than the water level of the air tank 1C is attached, and the processing liquid sucked by the suction pump 4 is filtered water tank 1E.
A pipe 5 is formed so as to pump water, and the pumped processing liquid overflows from the filtration water tank 1E to the disinfection tank 1D. In addition, although the case of the contact aeration tank 1C as the aerobic treatment tank is shown in the above embodiment, the present invention can be similarly applied to an activated sludge treatment tank. In this case, the membrane module 3 is provided at the height of the supernatant of the treated water in the tank.

【0007】[0007]

【作用】上記の汚水浄化槽1によれば、有機成分等が分
解された処理液が膜モジュール3で吸引ろ過され、吸引
ポンプ4によってろ過水槽1Eに揚水されたのち、消毒
槽1Eにオーバーフローして汚水浄化槽1の外に放流さ
れる。その場合、吸引ポンプ4を停めると、ろ過水槽1
Eが接触ばっ気槽1Cの水位よりも高い位置に設けられ
ているから、ろ過水槽1Eの水位の水頭圧が膜モジュー
ル3の内面に加わり、逆に膜モジュール3および吸引ポ
ンプ4の内部の吸引上澄み液が膜モジュール3外に流れ
ることとなって、膜モジュール3の膜面に付着していた
汚泥物が剥がされ、膜モジュール3が洗浄される。その
とき、散気管2のエア吹き出し口2aを膜モジュール3
の下に設けておいて、エア吹き出し口2aからエアを吹
き出しておけば、該エアが膜モジュール3に当たって膜
面汚泥物の剥離が一層促される。
According to the above-mentioned sewage purification tank 1, the treatment liquid in which organic components and the like are decomposed is suction-filtered by the membrane module 3, pumped to the filtration water tank 1E by the suction pump 4, and then overflowed to the disinfection tank 1E. It is discharged outside the sewage purification tank 1. In that case, when the suction pump 4 is stopped, the filtration water tank 1 is stopped.
Since E is provided at a position higher than the water level of the contact aeration tank 1C, the head pressure of the water level of the filtration water tank 1E is applied to the inner surface of the membrane module 3, and conversely, the suction inside the membrane module 3 and the suction pump 4 is performed. The supernatant liquid flows out of the membrane module 3, and the sludge attached to the membrane surface of the membrane module 3 is peeled off, and the membrane module 3 is washed. At this time, the air outlet 2a of the air diffuser 2 is connected to the membrane module 3
If the air is blown out from the air blow-out port 2a in advance, the air hits the membrane module 3 and the separation of the membrane sludge is further promoted.

【0008】[0008]

【考案の効果】以上の説明から明らかなように、この考
案によれば、吸引ポンプを停めることによってろ過水槽
の水頭圧を利用して、一旦膜モジュールに吸引した処理
水を該膜モジュールから流出させて膜モジュールの洗浄
を行なうことができるから、従来のエアによる洗浄に比
べて設備が簡単になり、特別の動力装置も不要となる
か、あるいは逆洗用動力を小さくしたり、運転時間を短
縮することが可能となり電力消費も低減でき、安価な膜
分離型汚水浄化槽を提供できる実用的効果が得られる。
As is clear from the above description, according to this invention, the treated water once drawn into the membrane module flows out of the membrane module by stopping the suction pump and utilizing the head pressure of the filtration tank. The cleaning of the membrane module can be performed in this way, making the equipment simpler than conventional cleaning with air, eliminating the need for a special power unit, reducing the power for backwashing, and reducing operating time. As a result, the power consumption can be reduced, and a practical effect of providing an inexpensive membrane separation type sewage treatment tank can be obtained.

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

【図1】この考案の実施例の断面図である。FIG. 1 is a sectional view of an embodiment of the present invention.

【図2】従来例の横断面図である。FIG. 2 is a cross-sectional view of a conventional example.

【図3】従来例の縦断面図である。FIG. 3 is a longitudinal sectional view of a conventional example.

【符号の説明】[Explanation of symbols]

1 汚水浄化槽 1A 嫌気ろ床槽第一室 1B 嫌気ろ床槽第二室 1C 接触ばっ気槽 1D 消毒槽 1E ろ過水槽 3 膜モジュール 4 吸引ポンプ DESCRIPTION OF SYMBOLS 1 Sewage purification tank 1A Anaerobic filter tank first room 1B Anaerobic filter tank second room 1C Contact aeration tank 1D Disinfection tank 1E Filtration water tank 3 Membrane module 4 Suction pump

───────────────────────────────────────────────────── フロントページの続き (72)考案者 原田 大 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 (72)考案者 北井 良人 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 (56)参考文献 特開 昭61−249599(JP,A) ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor: Dai Harada 2 at Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Inside the Kubota Shiga Plant. 1 Kubota Shiga Factory (56) References JP-A-61-249599 (JP, A)

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 嫌気ろ床槽または沈殿分離槽、好気処理
槽および消毒槽を備え、好気処理槽内に処理水を吸引分
離する膜モジュールと、該膜モジュールを通して処理水
を吸引する吸引ポンプとが設けられ、また上記消毒槽に
接触ばっ気槽内の水位よりも高い位置で水位を確保する
ろ過水槽が連設され、上記吸引ポンプから上記ろ過水槽
へ吸引処理水を揚水する配管が設けられ、かつ上記ろ過
水槽が上記消毒槽に処理水をオーバーフローさせるよう
に構成されてなることを特徴とする汚水浄化槽。
1. A membrane module comprising an anaerobic filter tank or sedimentation separation tank, an aerobic treatment tank and a disinfecting tank, and a suction module for sucking and separating treated water in the aerobic treatment tank, and a suction for sucking treated water through the membrane module. A pump is provided, and a filtration water tank that secures a water level at a position higher than a water level in the aeration tank in contact with the disinfection tank is provided in series, and a pipe for pumping suction-treated water from the suction pump to the filtration water tank is provided. A sewage purification tank provided, wherein the filtration water tank is configured to overflow treated water into the disinfection tank.
JP5147891U 1991-06-06 1991-06-06 Sewage septic tank Expired - Fee Related JP2553911Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5147891U JP2553911Y2 (en) 1991-06-06 1991-06-06 Sewage septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5147891U JP2553911Y2 (en) 1991-06-06 1991-06-06 Sewage septic tank

Publications (2)

Publication Number Publication Date
JPH04134492U JPH04134492U (en) 1992-12-15
JP2553911Y2 true JP2553911Y2 (en) 1997-11-12

Family

ID=31928359

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5147891U Expired - Fee Related JP2553911Y2 (en) 1991-06-06 1991-06-06 Sewage septic tank

Country Status (1)

Country Link
JP (1) JP2553911Y2 (en)

Also Published As

Publication number Publication date
JPH04134492U (en) 1992-12-15

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