JP2543834Y2 - Sewage treatment equipment - Google Patents

Sewage treatment equipment

Info

Publication number
JP2543834Y2
JP2543834Y2 JP1991012703U JP1270391U JP2543834Y2 JP 2543834 Y2 JP2543834 Y2 JP 2543834Y2 JP 1991012703 U JP1991012703 U JP 1991012703U JP 1270391 U JP1270391 U JP 1270391U JP 2543834 Y2 JP2543834 Y2 JP 2543834Y2
Authority
JP
Japan
Prior art keywords
separation membrane
membrane module
tank
sewage treatment
sewage
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
JP1991012703U
Other languages
Japanese (ja)
Other versions
JPH0499300U (en
Inventor
八郎 佐藤
丈衛 佐藤
良人 北井
広佳 中島
大 原田
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 JP1991012703U priority Critical patent/JP2543834Y2/en
Publication of JPH0499300U publication Critical patent/JPH0499300U/ja
Application granted granted Critical
Publication of JP2543834Y2 publication Critical patent/JP2543834Y2/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)
  • Treatment Of Biological Wastes In General (AREA)
  • Activated Sludge Processes (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】この考案は汚水処理装置に関し、
詳しくは流動床などの高濃度活性汚泥処理を行なう汚水
処理装置の改良に関する。
The present invention relates to a sewage treatment apparatus,
More specifically, the present invention relates to an improvement of a sewage treatment apparatus for performing a high-concentration activated sludge treatment such as a fluidized bed.

【0002】[0002]

【従来の技術】従来、家庭用小型合併浄化槽などには、
嫌気処理第1槽、同第2槽よりなる前段処理槽と好気処
理槽と沈殿槽、消毒槽よりなる後段処理槽を設け、汚水
を順次移流させつつ浄化していく構造の汚水浄化槽が公
知である。上記好気処理槽の接触材として設置型のもの
と流動床のものとがあり後者の流動床のものは被処理水
に対する接触面積が非常に大きいので浄化効率が良く小
型合併浄化槽などに適する利点を有する。
2. Description of the Related Art Conventionally, small-scale merger septic tanks for home use include:
Known is a sewage purification tank having a first-stage anaerobic treatment tank, a first-stage treatment tank composed of the second tank, and an aerobic treatment tank, a sedimentation tank, and a second-stage treatment tank composed of a disinfection tank. It is. The contact material of the aerobic treatment tank includes an installation type and a fluidized bed, and the latter fluidized bed has an advantage that the contact area with the water to be treated is very large, so that the purification efficiency is good and suitable for a small combined purification tank and the like. Having.

【0003】[0003]

【従来技術の問題点】しかし、上記流動床を用いた浄化
槽においては汚水を次室へ移流させる際、同時に流動床
も移流することがあり、好気処理槽の流動床担体の減少
を来すと共に次室のSS増加を生じる欠点があった。こ
のような欠点は好気処理槽より沈殿槽への汚水移流口に
フィルターを取付ければ良いのであるが、このフィルタ
ーにも好気性微生物が付着するので目詰まりを生じやす
く、処理水移流が比較的短期間の内に妨げられる欠点が
あった。
However, in the septic tank using the fluidized bed, when the sewage is transferred to the next chamber, the fluidized bed may also be transferred at the same time, resulting in a decrease in the fluidized bed carrier in the aerobic treatment tank. At the same time, there is a drawback that the SS in the next room increases. The drawback is that a filter can be attached to the sewage inflow port from the aerobic treatment tank to the sedimentation tank.However, since aerobic microorganisms also adhere to this filter, clogging is likely to occur. There were drawbacks that were hindered within a very short period of time.

【0004】また、高濃度活性汚泥処理後の固液分離槽
内にセラミックメンブレンよりなる分離膜モジュールを
配置し、外部に設置した吸引ポンプにより固液分離を行
なうことも考えられるが、吸引ポンプの設置容積を別途
必要とし、さらに汚水処理装置の設置時吸引ポンプに至
る配管等の工事手間もかゝるといった欠点があった。従
って、流動床槽は汚水の浄化処理に非常に有効であるに
も係わらず保守管理が非常に面倒となることより積極的
に採用し難い問題があった。
It is also conceivable to dispose a separation membrane module made of a ceramic membrane in a solid-liquid separation tank after high-concentration activated sludge treatment, and to perform solid-liquid separation using an externally installed suction pump. There is a drawback that the installation volume is separately required, and that the construction work such as piping to the suction pump when installing the sewage treatment apparatus is also required. Therefore, although the fluidized bed tank is very effective for the purification treatment of the sewage, there is a problem that the maintenance management becomes very troublesome and it is difficult to adopt it actively.

【0005】[0005]

【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、汚水処理を高濃度活性汚泥により行なう場合、
これら汚泥の移流を確実に防止すると共に汚水処理装置
の設置容積の減少化並びに維持管理の手間も省ける改良
された汚水処理装置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 considers the case where sewage treatment is performed using high-concentration activated sludge.
It is an object of the present invention to provide an improved sewage treatment apparatus capable of reliably preventing the sludge from advancing, reducing the installation volume of the sewage treatment apparatus, and saving the trouble of maintenance.

【0006】[0006]

【課題を解決するための手段】即ち、この考案の汚水処
理装置は、高濃度活性汚泥処理槽内に、分離膜モジュー
ルと該分離膜モジュールの透過水ヘッダー管と吸引口を
結合しかつ水面下に没した吸引用水中ポンプを一体に有
し、さらに前記分離膜モジュール下面に散気装置を有す
る枠体が取出可能に配置され、前記吸引用水中ポンプに
は汚水処理装置外部への汚水排水管が接続可能に構成さ
れてなることを特徴とするものである。
That is, the sewage treatment apparatus of the present invention comprises a separation membrane module, a permeated water header pipe of the separation membrane module, and a suction port in a high concentration activated sludge treatment tank.
A suction submersible pump combined and submerged below the water surface is integrally provided, and a frame having a diffuser is disposed on the lower surface of the separation membrane module so as to be able to be taken out. Sewage drainage pipe is connected to the sewage pipe.

【0007】[0007]

【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。この考案の汚水処理装
置1は、例えば流動床槽等高濃度活性汚泥処理槽2内
に、分離膜モジュール5と該分離膜モジュールの透過水
ヘッダー管5Aと吸引口4Bを結合しかつ水面下に没し
吸引用水中ポンプ4を一体に有し、さらに分離膜モジ
ュール5下面に散気装置8を有する枠体6が取出可能に
配置され、吸引用水中ポンプ4には汚水処理装置1外部
への汚水排水管4Aが接続可能に 構成されている。
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 treatment apparatus 1 of the present invention includes a separation membrane module 5 and permeated water of the separation membrane module in a high-concentration activated sludge treatment tank 2 such as a fluidized bed tank.
Connect the header tube 5A and the suction port 4B and submerge under the water surface
And a frame 6 having an air diffuser 8 on the lower surface of the separation membrane module 5 so as to be able to be taken out. The drain pipe 4A is configured to be connectable.

【0008】上記分離膜モジュールとしては、吸引型セ
ラミック分離膜モジュールの他、ガラス又はプラスチッ
ク製で0.1 〜60μm (好ましくは0.1 〜10μm )の目開
きを有する微細多孔質管を吸引型分離膜とした分離膜モ
ジュールが使用される。図において9は散気装置8に給
気するブロワを示し、このブロワ9よりバルブ9Aを介
して分離膜モジュール5内へ給気管9Bを連通し、定期
的な逆洗を実施可能に構成することもできる。
As the above-mentioned separation membrane module, in addition to a suction type ceramic separation module, a microporous tube made of glass or plastic and having an opening of 0.1 to 60 μm (preferably 0.1 to 10 μm) is used as a suction type separation membrane. A separation membrane module is used. In the drawing, reference numeral 9 denotes a blower for supplying air to the air diffuser 8, and the blower 9 is connected to an air supply pipe 9B into the separation membrane module 5 via a valve 9A so that a regular backwash can be performed. Can also.

【0009】[0009]

【作用】この考案において高濃度活性汚泥処理槽2内で
汚水浄化処理を行った後の汚水は、吸引用水中ポンプ4
の吸引力により分離膜モジュール5を経て外部へ排出さ
れる。この場合、外部へ排出される処理水は分離膜モジ
ュール5の密度にもよるが、排出水には剥離汚泥等の浮
遊物は完全に除去され充分に浄化された水が排出され
る。
In the present invention, the sewage after the sewage purification treatment in the high-concentration activated sludge treatment tank 2 is supplied to a suction submersible pump 4.
Is discharged to the outside through the separation membrane module 5 by the suction force. In this case, although the treated water discharged to the outside depends on the density of the separation membrane module 5, suspended matter such as peeled sludge is completely removed from the discharged water and sufficiently purified water is discharged.

【0010】また、分離膜モジュール5には吸引用ポン
プ4が一体的に付設されているので、ポンプを浄化槽外
に別設する必要も無い。また、上記分離膜モジュール5
下面には散気装置7が設けられているため、高濃度活性
汚泥処理槽2内での好気性微生物による有機物分解は非
常に効率良く行なわれる。また、ブロワ9より給気管9
Bを介して強制給気を行なえば分離膜モジュール5の逆
洗も可能となる。
Further, since the suction pump 4 is integrally provided with the separation membrane module 5, it is not necessary to separately provide the pump outside the septic tank. Further, the separation membrane module 5
Since the diffuser 7 is provided on the lower surface, the decomposition of the organic matter by the aerobic microorganisms in the high-concentration activated sludge treatment tank 2 is performed very efficiently. In addition, the air supply pipe 9 from the blower 9
If forced air supply is performed via B, backwashing of the separation membrane module 5 is also possible.

【0011】[0011]

【考案の効果】以上説明したように、この考案の汚水処
理装置は流動床槽内の活性汚泥の移流が分離膜モジュー
ルによって確実に防止され、またこの分離膜モジュール
も定期的に逆洗可能であるから実質的に目詰まりを生じ
ることがなく長期にわたって効率の良い汚水浄化を行な
えるのである。さらに、分離膜モジュール、吸引ポンプ
及び散気装置は一体的に枠に支持され、汚水処理装置内
外に取出可能とされているので、ポンプ設置容積を汚水
処理装置外部に設ける必要がなく、省スペース化が図ら
れると共に、設置も枠の出し入れだけで可能であるので
汚水処理装置の組立て、保守点検等も非常に容易となる
などの実用的効果を有する。また、吸引用ポンプは水面
下に配置されるから、停止中でもポンプ内に空気が侵入
することがなく再稼働時の安定処理ができる効果を有す
る。
As described above, in the sewage treatment apparatus of the present invention, the flow of activated sludge in the fluidized-bed tank is reliably prevented by the separation membrane module, and the separation membrane module can be periodically backwashed. As a result, the wastewater can be efficiently purified for a long period of time without substantially clogging. Furthermore, since the separation membrane module, the suction pump and the air diffuser are integrally supported by the frame and can be taken out of and inside the sewage treatment device, there is no need to provide a pump installation volume outside the sewage treatment device, thus saving space. In addition, the installation can be performed only by taking the frame in and out, so that the sewage treatment apparatus has a practical effect that the assembly, maintenance and inspection thereof are very easy. The suction pump is on the water surface
Because it is located below, air enters the pump even when stopped
Has the effect of enabling stable processing at restart without the need for
You.

【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 汚水処理装置 2 高濃度活性汚泥槽 4 吸引ポンプ 5 膜分離装置 6 枠 DESCRIPTION OF SYMBOLS 1 Sewage treatment apparatus 2 High concentration activated sludge tank 4 Suction pump 5 Membrane separation apparatus 6 Frame

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 3/00 C02F 3/00 F (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 (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 (56)参考文献 特開 平3−254896(JP,A)──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code Agency reference number FI Technical indication location C02F 3/00 C02F 3 / 00F (72) Inventor Hiroyoshi Nakajima 2 Takamatsu, Kosai-cho, Koka-gun, Shiga Prefecture (1) Inside the Kubota Shiga Plant, Ltd. (72) Inventor Dai Dai Harada Inside the Kubota Shiga Plant, 2 at Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture (56) References JP-A-3-254896 (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】 高濃度活性汚泥処理槽内に、分離膜モジ
ュールと該分離膜モジュールの透過水ヘッダー管と吸引
口を結合しかつ水面下に没した吸引用水中ポンプを一体
に有し、さらに前記分離膜モジュール下面に散気装置を
有する枠体が取出可能に配置され、前記吸引用水中ポン
プには汚水処理装置外部への汚水排水管が接続可能に構
成されてなることを特徴とする汚水処理装置。
1. A separation membrane module, a permeated water header tube of the separation membrane module, and suction in a high concentration activated sludge treatment tank.
A suction pump submerged under the water surface with an integrated mouth, and a frame having an air diffuser at the lower surface of the separation membrane module is disposed so as to be able to be taken out; A sewage treatment apparatus characterized in that a sewage drain pipe to the outside of the apparatus can be connected.
JP1991012703U 1990-06-13 1991-02-13 Sewage treatment equipment Expired - Lifetime JP2543834Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991012703U JP2543834Y2 (en) 1990-06-13 1991-02-13 Sewage treatment equipment

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP6240590 1990-06-13
JP2-62405 1990-06-13
JP1991012703U JP2543834Y2 (en) 1990-06-13 1991-02-13 Sewage treatment equipment

Publications (2)

Publication Number Publication Date
JPH0499300U JPH0499300U (en) 1992-08-27
JP2543834Y2 true JP2543834Y2 (en) 1997-08-13

Family

ID=31948255

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991012703U Expired - Lifetime JP2543834Y2 (en) 1990-06-13 1991-02-13 Sewage treatment equipment

Country Status (1)

Country Link
JP (1) JP2543834Y2 (en)

Also Published As

Publication number Publication date
JPH0499300U (en) 1992-08-27

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