JP2553218Y2 - Sewage septic tank - Google Patents

Sewage septic tank

Info

Publication number
JP2553218Y2
JP2553218Y2 JP1991013860U JP1386091U JP2553218Y2 JP 2553218 Y2 JP2553218 Y2 JP 2553218Y2 JP 1991013860 U JP1991013860 U JP 1991013860U JP 1386091 U JP1386091 U JP 1386091U JP 2553218 Y2 JP2553218 Y2 JP 2553218Y2
Authority
JP
Japan
Prior art keywords
tank
activated sludge
treatment tank
sewage
sludge treatment
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
JP1991013860U
Other languages
Japanese (ja)
Other versions
JPH0499295U (en
Inventor
八郎 佐藤
丈衛 佐藤
良人 北井
大 原田
広佳 中島
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 JP1991013860U priority Critical patent/JP2553218Y2/en
Publication of JPH0499295U publication Critical patent/JPH0499295U/ja
Application granted granted Critical
Publication of JP2553218Y2 publication Critical patent/JP2553218Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Biological Wastes In General (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (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】この考案は汚水浄化槽に関し、詳
しくは流動床などの高濃度活性汚泥処理槽を有する汚水
浄化槽の改良に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sewage treatment tank, and more particularly to an improvement of a sewage treatment tank having a high-concentration activated sludge treatment tank such as a fluidized bed.

【0002】[0002]

【従来の技術】従来、合併浄化槽として、流動床槽等の
高濃度活性汚泥処理槽内に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 〜10μm 目開きの微
細多孔質管よりなる分離膜モジュールを設けた汚水浄化
槽が提案され実施されつつある。この形式の汚水浄化槽
は活性汚泥により汚水中の有機物を処理した後、分離膜
モジュールで処理水のみを濾過抽出するので排出液の浄
化水準が非常に高くコンパクトな装置となり、汚水浄化
槽として好都合である利点を有する。
2. Description of the Related Art Conventionally, as a combined clarification tank, a separation membrane module comprising a ceramic membrane or a glass or plastic microporous tube with an opening of 0.1 to 10 μm is provided in a high-concentration activated sludge treatment tank such as a fluidized bed tank. Sewage treatment tanks are being proposed and are being implemented. This type of sewage treatment tank treats organic matter in sewage with activated sludge and then filters and extracts only the treated water with a separation membrane module, so the purification level of the effluent is very high and it is a compact device, which is convenient as a sewage treatment tank. Has advantages.

【0003】[0003]

【従来技術の問題点】しかし、供給される汚水中には粗
大固形物も多く含まれるから、上記高濃度活性汚泥処理
槽へ汚水を供給するに先立ってこれらの濾過スクリーン
を設ける必要があり、濾過物の処理が容易でない欠点が
あった。また高濃度活性汚泥処理槽での処理においても
濾過後に含まれる微小な固形物の完全な分解は困難で、
これらの残滓により分離膜モジュールが早期に目詰まり
を起こし濾過不良となり易い欠点があった。一方、逆に
微細な自動スクリーンなどでほぼ完全にSSを前処理で
除去した場合、脱窒素槽内で脱窒素用炭素源が不足し脱
窒素が十分に行えない場合があった。
However, since the supplied wastewater contains a large amount of coarse solids, it is necessary to provide these filtration screens before supplying the wastewater to the high-concentration activated sludge treatment tank. There was a disadvantage that it was not easy to treat the filtrate. In addition, even in treatment in a high-concentration activated sludge treatment tank, it is difficult to completely decompose minute solids contained after filtration,
There was a disadvantage that the separation membrane module was clogged at an early stage due to these residues, resulting in poor filtration. On the other hand,
SS is almost completely pre-processed with a fine automatic screen
If it is removed, the amount of denitrification carbon
In some cases, nitrogen could not be sufficiently performed.

【0004】[0004]

【考案が解決しようとする課題】この考案は上記問題点
に鑑み、固形粗大物が含まれていてもこれを充分に分離
処理可能であり、また脱窒素処理も良好に行え、分離膜
モジュール等の目詰まりも有効に防止し得る汚水浄化槽
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 In view of the above-mentioned problems, the present invention is capable of sufficiently separating solid coarse substances even if they are contained, and also performing denitrification processing well, and is capable of separating membrane modules and the like. It is an object of the present invention to provide a sewage purification tank capable of effectively preventing clogging.

【0005】[0005]

【課題を解決するための手段】即ち、この考案の汚水浄
化槽は汚水原水が流入される沈殿分離槽と、以後順次処
理汚水が移流されていく嫌気ろ床槽と嫌気性活性汚泥処
理槽と、好気性活性汚泥処理槽と、該好気性活性汚泥処
理槽内に設けられた膜分離装置と、該膜分離装置の吸引
ポンプと、前記好気性活性汚泥処理槽より前記嫌気性活
性汚泥処理槽に向け混合液を常時又は間欠的に循環返送
する循環ポンプと、前記嫌気性括性汚泥槽内に設けられ
た攪拌ポンプから構成されたことを特徴とするものであ
る。
The sewage purification tank of the present invention comprises a sedimentation separation tank into which raw sewage flows, an anaerobic filter bed tank and an anaerobic activated sludge treatment tank into which treated sewage is successively transferred. An aerobic activated sludge treatment tank, a membrane separation device provided in the aerobic activated sludge treatment tank, a suction pump of the membrane separation device, and the anaerobic activated sludge treatment tank from the aerobic activated sludge treatment tank A circulating pump that constantly or intermittently circulates and returns the mixed solution, and is provided in the anaerobic consolidation sludge tank.
A stirring pump .

【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。この考案の汚水浄化
槽1は、汚水原水が流入される沈殿分離槽2と、粗大固
形物を沈殿除去した汚水が移流される嫌気ろ床槽3と、
次いで汚水が移流される嫌気性活性汚泥処理槽4と、同
様に汚水が移流される好気性活性汚泥処理槽5と、この
好気性活性汚泥処理槽5内に設けられたセラミックメン
ブレン、あるいはガラス又はプラスチック製0.1〜1
0μm目開きの微細多孔質管よりなる膜分離装置6と、
膜分離装置6の吸引ポンプ7と、好気性活性汚泥処理槽
5より嫌気性活性汚泥処理槽4に向け混合液を常時又は
間欠的に循環返送する循環ポンプ8と、嫌気性活性汚泥
槽4内に設けられた攪拌ポンプ10から構成されてい
る。上記循環ポンプ8はエアリフトポンプが使用され、
空気供給源としては好気性活性汚泥処理槽5へ給気する
ブロワ9が兼用される。
Next, an embodiment of the present invention will be described. FIG. 1 is a sectional view of an embodiment of the present invention. The sewage purification tank 1 of the present invention includes a sedimentation separation tank 2 into which sewage raw water flows, an anaerobic filter tank 3 into which sewage from which coarse solids have been removed is transferred,
Next, an anaerobic activated sludge treatment tank 4 to which sewage is transferred, an aerobic activated sludge treatment tank 5 to which sewage is similarly transferred, and a ceramic membrane, glass, or glass provided in the aerobic activated sludge treatment tank 5 0.1-1 plastic
A membrane separation device 6 comprising a microporous tube having an opening of 0 μm;
A suction pump 7 of the membrane separation device 6, a circulation pump 8 for constantly or intermittently circulating and returning the mixture from the aerobic activated sludge treatment tank 5 to the anaerobic activated sludge treatment tank 4, and an anaerobic activated sludge.
It is composed of a stirring pump 10 provided in the tank 4 . The circulation pump 8 is an air lift pump,
The air supply Ru also serves the blower 9 to supply to the aerobic activated sludge treatment tank 5.

【0007】[0007]

【作用】この考案において汚水原水は沈殿分離槽2に先
ず流入される。この沈澱分離槽2では汚水原水に含まれ
ている粗大固形物が沈殿除去されると共に、汚水は静置
されることにより嫌気処理がなされる。そして固形粗大
物を除去した汚水は次室である嫌気ろ床槽3へ移流す
る。このとき、移流水中に含まれる浮遊物はろ床3で濾
過され以後の室への流入を防止する。従って、汚水が次
室である嫌気性活性汚泥処理槽4へ移流する時点では浮
遊物等の除去が行われ、同時に汚水のSS負荷もかなり
減少されているので移流負荷が軽減され嫌気性活性汚泥
処理槽4での浄化処理は効率良く行なわれる。さらに、
この嫌気性活性汚泥処理槽4内は攪拌ポンプ10によっ
て図に示す矢印のように処理水が攪拌され、同時に循環
ポンプ8で返送される処理水とも良く攪拌混合される。
従って、この混合攪拌により脱窒素効率が上がる他、嫌
気ろ床槽3から移流してくる処理水に浮遊物が混入して
いてもこの攪拌流により共に混合され、これらが炭素源
となってり脱窒素効果を上げる。
In the present invention, raw sewage is first flowed into the sedimentation separation tank 2. In the sedimentation separation tank 2, coarse solids contained in the raw sewage are removed by sedimentation, and the sewage is subjected to anaerobic treatment by being left standing. Then, the sewage from which the bulky solid matter has been removed flows to the anaerobic filter tank 3 which is the next chamber. At this time, the suspended matter contained in the advancing water is filtered by the filter bed 3 and prevented from flowing into the chamber thereafter. Therefore, sewage We row removed, such as suspended solids at the time of advected into the anaerobic bioreactor tank 4 which is the next chamber, the advection load alleviation because it is considerably reduced at the same time sewage SS load anaerobic activated sludge The purification treatment in the treatment tank 4 is performed efficiently. further,
The inside of this anaerobic activated sludge treatment tank 4 is
The treated water is stirred and circulated at the same time as indicated by the arrow in the figure.
It is well stirred and mixed with the treated water returned by the pump 8.
Therefore, this mixing and stirring increases the denitrification efficiency,
Suspended matter is mixed in the treated water flowing from the
Are mixed together by this stirred flow,
It increases the denitrification effect.

【0008】そして、処理汚水はさらに次室である好気
性活性汚泥処理槽5へ移流していくが、この処理槽5に
おいても浄化処理は同様に効率良く行なわれる。また、
この好気性活性汚泥処理槽5での処理中の汚水は常時循
環ポンプ8でその一部が嫌気性活性汚泥処理槽4へと返
送される。従って、前述のように処理水の脱窒が効率良
く行なわれる。以上のように分解処理された汚水は最終
的に膜分離装置6を経て吸引ポンプ7により外部へ排出
される。この排出処理水は、膜分離装置6で濾過された
ものであるため処理水の浄化水準は非常に高く、また、
膜分離装置6に至るまでの間汚水は各処理段階を経てい
るため浮遊物は非常に少なく、膜モジュールの目詰まり
も少ない。又活性汚泥処理槽で発生する汚泥は必要に応
じ沈殿分離槽又は別途設けられた汚泥貯溜槽へ間欠的に
移送されるので、過大なMLSS濃度運転は避けられ
る。
[0008] The treated sewage is further transferred to the aerobic activated sludge treatment tank 5 which is the next chamber. In this treatment tank 5 as well, the purification treatment is similarly performed efficiently. Also,
A part of the sewage that is being treated in the aerobic activated sludge treatment tank 5 is always returned to the anaerobic activated sludge treatment tank 4 by the circulation pump 8. Therefore, the denitrification of the treated water is efficiently performed as described above . The sewage decomposed as described above is finally discharged to the outside by the suction pump 7 through the membrane separation device 6. Since the discharged treated water is filtered by the membrane separation device 6, the treated water has a very high purification level.
Since the sewage has gone through each treatment step until it reaches the membrane separation device 6, the amount of suspended matter is very small, and the clogging of the membrane module is also small. Further, the sludge generated in the activated sludge treatment tank is intermittently transferred to a sedimentation separation tank or a separately provided sludge storage tank as needed, so that an excessive MLSS concentration operation can be avoided.

【0009】[0009]

【考案の効果】以上説明したように、この考案の汚水浄
化槽は膜分離装置に処理水が至るまでの間に沈降分離並
びに嫌気ろ床槽での浮遊物の分離と嫌気処理を行なって
いるので好気性活性汚泥処理槽でのSS負荷が著るしく
低下し得、効率の良い汚水浄化が可能となり同時に分離
膜モジュールの目詰まりもそれだけ防止される。さら
に、好気性活性汚泥処理槽と嫌気性活性汚泥処理槽との
間で混合液を循環している他、嫌気性活性汚泥槽内では
処理水を攪拌ポンプで混合攪拌するため脱窒も効率よく
行われるなど種々の実用的効果を有する。
[Effects of the Invention] As described above, the sewage treatment tank of the present invention performs sedimentation and separation, separation of suspended matter in the anaerobic filter tank, and anaerobic treatment before the treated water reaches the membrane separation device. The SS load in the aerobic activated sludge treatment tank can be remarkably reduced, and efficient purification of sewage becomes possible, and clogging of the separation membrane module is also prevented accordingly. Moreover, other circulating the mixture between the aerobic activated sludge treatment tank and the anaerobic bioreactor tank, the anaerobic activated sludge tank
Since the treated water is mixed and stirred by a stirring pump, it has various practical effects such as efficient denitrification.

【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.

【符号の説明】[Explanation of symbols]

1 汚水浄化槽 2 沈殿分離槽 3 嫌気ろ床槽 4 嫌気性活性汚泥処理槽 5 好気性活性汚泥処理槽 6 膜分離装置 7 吸引ポンプ 8 循環ポンプ 9 ブロワ10 攪拌ポンプ Reference Signs List 1 sewage purification tank 2 sedimentation separation tank 3 anaerobic bed tank 4 anaerobic activated sludge treatment tank 5 aerobic activated sludge treatment tank 6 membrane separation device 7 suction pump 8 circulation pump 9 blower 10 stirring 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 中島 広佳 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61−200894(JP,A) 特開 昭60−168597(JP,A) ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Daisuke Harada 2 at Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Inside the Kubota Shiga Plant. Kubota Shiga Plant (56) References JP-A-61-200894 (JP, A) JP-A-60-168597 (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】 汚水原水が流入される沈殿分離槽と、以
後順次処理汚水が移流されていく嫌気ろ床槽と嫌気性活
性汚泥処理槽と、好気性活性汚泥処理槽と、該好気性活
性汚泥処理槽内に設けられた膜分離装置と、該膜分離装
置の吸引ポンプと、前記好気性活性汚泥処理槽より前記
嫌気性活性汚泥処理槽に向け混合液を常時又は間欠的に
循環返送する循環ポンプと、前記嫌気性活性汚泥槽内に
設けられた攪拌ポンプから構成されたことを特徴とする
汚水浄化槽。
1. A sedimentation separation tank into which raw sewage water flows, an anaerobic filter tank, an anaerobic activated sludge treatment tank, and an aerobic activated sludge treatment tank into which treated sewage is successively transferred. A membrane separation device provided in the sludge treatment tank, a suction pump of the membrane separation device, and a continuous or intermittent circulation return of the mixed liquid from the aerobic activated sludge treatment tank to the anaerobic activated sludge treatment tank. A circulation pump and the anaerobic activated sludge tank
A sewage purification tank comprising a stirring pump provided .
JP1991013860U 1990-06-15 1991-02-18 Sewage septic tank Expired - Fee Related JP2553218Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991013860U JP2553218Y2 (en) 1990-06-15 1991-02-18 Sewage septic tank

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2-63660 1990-06-15
JP6366090 1990-06-15
JP1991013860U JP2553218Y2 (en) 1990-06-15 1991-02-18 Sewage septic tank

Publications (2)

Publication Number Publication Date
JPH0499295U JPH0499295U (en) 1992-08-27
JP2553218Y2 true JP2553218Y2 (en) 1997-11-05

Family

ID=31948269

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991013860U Expired - Fee Related JP2553218Y2 (en) 1990-06-15 1991-02-18 Sewage septic tank

Country Status (1)

Country Link
JP (1) JP2553218Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61200894A (en) * 1985-02-28 1986-09-05 Hitachi Plant Eng & Constr Co Ltd Apparatus for treating waste water

Also Published As

Publication number Publication date
JPH0499295U (en) 1992-08-27

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