JP2002254092A - Solid-liquid separating device in activated sludge treatment facilities - Google Patents

Solid-liquid separating device in activated sludge treatment facilities

Info

Publication number
JP2002254092A
JP2002254092A JP2001055728A JP2001055728A JP2002254092A JP 2002254092 A JP2002254092 A JP 2002254092A JP 2001055728 A JP2001055728 A JP 2001055728A JP 2001055728 A JP2001055728 A JP 2001055728A JP 2002254092 A JP2002254092 A JP 2002254092A
Authority
JP
Japan
Prior art keywords
solid
activated sludge
carbon fiber
fiber bundle
liquid
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.)
Pending
Application number
JP2001055728A
Other languages
Japanese (ja)
Inventor
Masahiko Kagawa
昌彦 賀川
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.)
Furukawa Co Ltd
Original Assignee
Furukawa 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 Furukawa Co Ltd filed Critical Furukawa Co Ltd
Priority to JP2001055728A priority Critical patent/JP2002254092A/en
Publication of JP2002254092A publication Critical patent/JP2002254092A/en
Pending 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

  • Activated Sludge Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To surely solid-liquid separate treating water in activated sludge treatment facilities by means of a solid-liquid separating device of simple structure. SOLUTION: A bundle 7 of carbon fibers which are excellent in adhesion of microorganism is provided in the water route 6 of a treating liquid 3 containing the activated sludge, and a back-washing device 8 for back washing the sludge stuck to the bundle 7 of the carbon fibers and a stretching device 9 which usually stretches the bundle 7 of carbon fibers but loosens it at the time of back washing are provided.

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、活性汚泥処理設備
において用いられる固液分離装置に関する。
TECHNICAL FIELD The present invention relates to a solid-liquid separation device used in an activated sludge treatment facility.

【0002】[0002]

【従来の技術】有機性排水の処理方法として最も一般的
に行われている活性汚泥法では、図4に示すように、原
水1を曝気槽2において好気性処理し、活性汚泥を含む
処理液3を沈殿槽4で固液分離する。活性汚泥法は、性
能・経済性の面から優れた処理方法であるが、安定した
処理を行うためには、維持管理を適切に行うことが重要
である。
2. Description of the Related Art In an activated sludge method most commonly used as a method for treating organic waste water, as shown in FIG. 4, a raw water 1 is subjected to aerobic treatment in an aeration tank 2, and a treatment liquid containing activated sludge is treated. 3 is subjected to solid-liquid separation in a sedimentation tank 4. The activated sludge method is an excellent treatment method in terms of performance and economy, but it is important to maintain and manage properly in order to perform stable treatment.

【0003】特に、処理の最終段階である固液分離は、
沈殿槽4での重力による自然沈降に依存しているため、
負荷の状況、微生物の活性度、外気温度等の影響を受け
やすく、汚泥の沈降性の変化により処理水質に大きな影
響を与える。このため、活性汚泥法に種々の改良を加え
た方式が提案されている。特に、近年では固液分離の操
作性を改善するため膜を使った固液分離が採用されてい
る。膜を使った固液分離では運転状況の変化による汚泥
の流出がないため、確実な処理が行える。
[0003] In particular, solid-liquid separation, which is the final stage of processing,
Because it relies on gravity sedimentation in sedimentation tank 4,
It is susceptible to load conditions, microbial activity, outside air temperature, etc., and greatly affects the quality of treated water due to changes in the sedimentation of sludge. For this reason, a method in which various improvements are added to the activated sludge method has been proposed. In particular, in recent years, solid-liquid separation using a membrane has been adopted to improve the operability of solid-liquid separation. In solid-liquid separation using a membrane, since there is no outflow of sludge due to a change in operation conditions, reliable treatment can be performed.

【0004】[0004]

【発明が解決しようとする課題】しかし、膜を使った固
液分離は、濾過速度が遅いため所要の液量を処理するた
めには設備が複雑化、大型化せざるを得ずコストが高く
なる上、汚泥の付着で閉塞しやすいので逆洗などの操作
を高頻度で行う必要がある。また、高度な処理が可能な
反面、必要以上の処理が行われ、処理水質に見合わない
過剰設備となることがある。
However, the solid-liquid separation using a membrane has a slow filtration speed and requires a complicated and large-sized facility for processing a required amount of liquid. In addition, it is necessary to frequently perform an operation such as backwashing because the sludge is easily blocked due to adhesion of sludge. In addition, although advanced treatment is possible, excessive treatment is performed, which may lead to excess equipment that does not match the quality of the treated water.

【0005】本発明は、活性汚泥の固液分離における上
記課題を解決するものであって、操作が容易で確実に固
液分離を行うことができ、構造が簡単でコストの安い活
性汚泥処理設備の固液分離装置を提供することを目的と
する。
The present invention solves the above-mentioned problems in the solid-liquid separation of activated sludge. The activated sludge treatment equipment has a simple structure and is inexpensive. It is an object of the present invention to provide a solid-liquid separation device.

【0006】[0006]

【課題を解決するための手段】本発明の活性汚泥処理設
備の固液分離装置は、活性汚泥を含む処理液の水路に、
微生物の付着性に優れた炭素繊維束を設置すると共に、
炭素繊維束に付着した汚泥を逆洗するための逆洗装置
と、炭素繊維束を常時は緊張させ逆洗時に弛緩させる緊
張装置とを設けることにより上記課題を解決している。
SUMMARY OF THE INVENTION The solid-liquid separation device of the activated sludge treatment equipment of the present invention is provided in a channel for a treatment liquid containing activated sludge.
Along with installing a carbon fiber bundle with excellent microbial adhesion,
The above problem is solved by providing a backwashing device for backwashing sludge adhering to a carbon fiber bundle and a tensioning device for always tensioning the carbon fiber bundle and relaxing it during the backwashing.

【0007】この固液分離装置では、活性汚泥を含む処
理液の水路に、微生物の付着性に優れた炭素繊維束を緊
張させた状態で設置しているので、水路を流れる処理液
が炭素繊維の間を通過する際に、活性汚泥が炭素繊維に
付着し、確実に固液分離が行われる。逆洗時には炭素繊
維束を弛緩させるので、付着した活性汚泥を効率よく炭
素繊維から離脱させることができる。
[0007] In this solid-liquid separation device, the carbon fiber bundle having excellent adhesion of microorganisms is installed in the water channel of the processing liquid containing activated sludge in a tensioned state. Activated sludge adheres to the carbon fiber when passing through the space, and solid-liquid separation is reliably performed. Since the carbon fiber bundle is relaxed at the time of backwashing, the activated sludge attached can be efficiently separated from the carbon fiber.

【0008】処理液の通過速度は膜を使った場合の濾過
速度と比べてはるかに速く、設備を小型化でき、また、
逆洗操作の頻度も少なくてよい。
[0008] The passing speed of the processing solution is much faster than the filtration speed when a membrane is used, so that the equipment can be miniaturized.
The frequency of the backwash operation may be less.

【0009】[0009]

【発明の実施の形態】図1は本発明の実施の一形態であ
る固液分離装置を備えた活性汚泥処理設備の構成図、図
2は固液分離装置の側面図、図は緊張装置の動作の説明
図である。この活性汚泥処理設備では、原水1を曝気槽
2において好気性処理し、活性汚泥を含む処理液3を固
液分離装置5で固液分離する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a configuration diagram of an activated sludge treatment facility provided with a solid-liquid separation device according to an embodiment of the present invention, FIG. 2 is a side view of the solid-liquid separation device, and FIG. It is an explanatory view of an operation. In this activated sludge treatment facility, raw water 1 is subjected to aerobic treatment in an aeration tank 2, and a treatment liquid 3 containing activated sludge is solid-liquid separated by a solid-liquid separation device 5.

【0010】固液分離装置5は、曝気槽2から流出する
活性汚泥を含む処理液3の水路6に設置された炭素繊維
束7と、この炭素繊維束7に付着した汚泥を逆洗するた
めの逆洗装置8と、炭素繊維束7を常時は緊張させ逆洗
時に弛緩させる緊張装置9とを備えている。炭素繊維束
7は、微生物の付着性に優れた炭素繊維の上下の端部を
繊維固定バー10で固定したものであり、やや弛緩した
状態となるように水路6内に設置されており、炭素繊維
束7の後方に設けた緊張装置9によって常時は緊張状態
に保持されている。炭素繊維束7は、処理水質、処理水
量等の条件により、2列、あるいはそれ以上重ねて配置
される。
The solid-liquid separator 5 is for backwashing the carbon fiber bundle 7 installed in the water channel 6 of the treatment liquid 3 containing the activated sludge flowing out of the aeration tank 2 and the sludge attached to the carbon fiber bundle 7. And a tensioning device 9 for always tensioning the carbon fiber bundle 7 and relaxing it during the backwashing. The carbon fiber bundle 7 is obtained by fixing the upper and lower ends of carbon fibers having excellent adhesion of microorganisms with the fiber fixing bar 10 and is installed in the water channel 6 so as to be slightly relaxed. The fiber bundle 7 is always kept in a tensioned state by a tensioning device 9 provided behind the fiber bundle 7. The carbon fiber bundles 7 are arranged in two rows or more depending on the conditions such as the quality of treated water and the amount of treated water.

【0011】緊張装置9は前後移動可能なローラであっ
て、逆洗時には図3に破線で示すようにこの緊張装置9
を後方へ移動させることにより、炭素繊維束7を弛緩さ
せることができる。逆洗装置8は、炭素繊維束7の下方
に設けられる曝気手段であって、逆洗時に圧縮空気を噴
出して処理液3を撹拌し、炭素繊維束7を振動させるこ
とにより、炭素繊維に付着した活性汚泥を離脱させる。
The tensioning device 9 is a roller that can move back and forth, and at the time of back washing, as shown by a broken line in FIG.
Is moved backward, the carbon fiber bundle 7 can be relaxed. The backwashing device 8 is an aeration unit provided below the carbon fiber bundle 7. At the time of backwashing, compressed air is blown out to agitate the treatment liquid 3 and vibrate the carbon fiber bundle 7, so that the carbon fiber bundle is vibrated. The activated sludge attached is released.

【0012】この固液分離装置5では、活性汚泥を含む
処理液3の水路6に、微生物の付着性に優れた炭素繊維
束7を緊張させた状態で設置しているので、水路6を流
れる処理液3が炭素繊維の間を通過する際に、活性汚泥
が炭素繊維に付着し、確実に固液分離が行われる。逆洗
時には緊張装置9を後方へ移動させ炭素繊維束7を弛緩
させた状態で、逆洗装置8が圧縮空気を噴出して処理液
3を撹拌し、炭素繊維束7を振動させるので、付着した
活性汚泥を効率よく炭素繊維から離脱させることができ
る。
In this solid-liquid separation device 5, the carbon fiber bundle 7 having excellent adhesion of microorganisms is installed in the water channel 6 of the treatment liquid 3 containing activated sludge in a tensioned state. When the treatment liquid 3 passes between the carbon fibers, the activated sludge adheres to the carbon fibers, and solid-liquid separation is reliably performed. At the time of back washing, the tensioning device 9 is moved backward to relax the carbon fiber bundle 7, and the back washing device 8 blows out compressed air to stir the treatment liquid 3 and vibrate the carbon fiber bundle 7, so that the carbon fiber bundle 7 is vibrated. The activated sludge thus separated can be efficiently separated from the carbon fibers.

【0013】処理液3が炭素繊維束7を通過すときの通
過速度は膜を使った場合の濾過速度と比べてはるかに速
く、設備を小型化できる。また、炭素繊維束7は膜のよ
うに付着した汚泥で閉塞されるおそれもないので、逆洗
操作の頻度も少なくてよい。この固液分離装置5は構造
が簡単でコストも安い。
The passing speed when the treatment liquid 3 passes through the carbon fiber bundle 7 is much faster than the filtration speed when a membrane is used, and the equipment can be miniaturized. In addition, since the carbon fiber bundle 7 is not likely to be blocked by the sludge attached like a membrane, the frequency of the backwash operation may be small. The solid-liquid separator 5 has a simple structure and a low cost.

【0014】[0014]

【発明の効果】以上説明したように、本発明の活性汚泥
処理設備の固液分離装置は、操作が容易で確実に固液分
離を行うことができ、構造が簡単でコストが安い。
As described above, the solid-liquid separator of the activated sludge treatment equipment of the present invention can be easily operated and can surely perform solid-liquid separation, and has a simple structure and low cost.

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

【図1】本発明の実施の一形態である固液分離装置を備
えた活性汚泥処理設備の構成図である。
FIG. 1 is a configuration diagram of an activated sludge treatment facility provided with a solid-liquid separation device according to an embodiment of the present invention.

【図2】固液分離装置の側面図である。FIG. 2 is a side view of the solid-liquid separation device.

【図3】緊張装置の動作の説明図である。FIG. 3 is an explanatory diagram of an operation of the tensioning device.

【図4】従来の活性汚泥処理設備の構成図である。FIG. 4 is a configuration diagram of a conventional activated sludge treatment facility.

【符号の説明】[Explanation of symbols]

1 原水 2 曝気槽 3 処理液 5 固液分離装置 6 水路 7 炭素繊維束 8 逆洗装置 9 緊張装置 10 繊維固定バー DESCRIPTION OF SYMBOLS 1 Raw water 2 Aeration tank 3 Processing liquid 5 Solid-liquid separation device 6 Waterway 7 Carbon fiber bundle 8 Backwashing device 9 Tensioning device 10 Fiber fixing bar

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 活性汚泥を含む処理液の水路に、微生物
の付着性に優れた炭素繊維束を設置すると共に、炭素繊
維束に付着した汚泥を逆洗するための逆洗装置と、炭素
繊維束を常時は緊張させ逆洗時に弛緩させる緊張装置と
を設けたことを特徴とする活性汚泥処理設備の固液分離
装置。
1. A backwash device for installing a carbon fiber bundle excellent in microbial adhesion in a water channel of a treatment liquid containing activated sludge, and for backwashing sludge attached to the carbon fiber bundle, and a carbon fiber A solid-liquid separation device for activated sludge treatment equipment, comprising a tension device for constantly tensioning the bundle and relaxing it during backwashing.
JP2001055728A 2001-02-28 2001-02-28 Solid-liquid separating device in activated sludge treatment facilities Pending JP2002254092A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001055728A JP2002254092A (en) 2001-02-28 2001-02-28 Solid-liquid separating device in activated sludge treatment facilities

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001055728A JP2002254092A (en) 2001-02-28 2001-02-28 Solid-liquid separating device in activated sludge treatment facilities

Publications (1)

Publication Number Publication Date
JP2002254092A true JP2002254092A (en) 2002-09-10

Family

ID=18915872

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001055728A Pending JP2002254092A (en) 2001-02-28 2001-02-28 Solid-liquid separating device in activated sludge treatment facilities

Country Status (1)

Country Link
JP (1) JP2002254092A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113943048A (en) * 2021-11-30 2022-01-18 北控水务(中国)投资有限公司 Membrane bioreactor and membrane bioreactor filtering method

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1015319A (en) * 1996-07-01 1998-01-20 Morimura Kosan Kk Filter material for solid-liquid separation of sewage and waste water or the like
JPH11128098A (en) * 1997-10-24 1999-05-18 Mitsubishi Electric Corp Bath water purifying device
JPH11319874A (en) * 1998-05-21 1999-11-24 Hitachi Kiden Kogyo Ltd Load decreasing method for sedimentation basin

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1015319A (en) * 1996-07-01 1998-01-20 Morimura Kosan Kk Filter material for solid-liquid separation of sewage and waste water or the like
JPH11128098A (en) * 1997-10-24 1999-05-18 Mitsubishi Electric Corp Bath water purifying device
JPH11319874A (en) * 1998-05-21 1999-11-24 Hitachi Kiden Kogyo Ltd Load decreasing method for sedimentation basin

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113943048A (en) * 2021-11-30 2022-01-18 北控水务(中国)投资有限公司 Membrane bioreactor and membrane bioreactor filtering method
CN113943048B (en) * 2021-11-30 2023-09-05 北控水务(中国)投资有限公司 Membrane bioreactor and membrane bioreactor filtering method

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