JPH02164494A - Sewage aeration treatment tank - Google Patents

Sewage aeration treatment tank

Info

Publication number
JPH02164494A
JPH02164494A JP63318172A JP31817288A JPH02164494A JP H02164494 A JPH02164494 A JP H02164494A JP 63318172 A JP63318172 A JP 63318172A JP 31817288 A JP31817288 A JP 31817288A JP H02164494 A JPH02164494 A JP H02164494A
Authority
JP
Japan
Prior art keywords
air supply
treatment tank
air
aeration treatment
diameter
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
JP63318172A
Other languages
Japanese (ja)
Inventor
Masatsugu Yamagata
山縣 昌継
Yoshihisa Narukami
善久 鳴上
Eisuke Hakubun
栢分 英助
Yasunori Okamoto
恭典 岡本
Kanji Tokushima
幹治 徳島
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 JP63318172A priority Critical patent/JPH02164494A/en
Publication of JPH02164494A publication Critical patent/JPH02164494A/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

Abstract

PURPOSE:To prevent the clogging of a ceramic filter by constituting the air diffusion pipe arranged under the filter module in an aeration tank so that the caliber of each of the air supply orifices thereof is larger than 0.2mm and smaller than 10mm. CONSTITUTION:A filter module 3 formed by collecting a large number of tubular ceramic filters is provided to the upper part in the tank main body 2 of an aeration treatment tank 1 and an air diffusion pipe 4 is provided to the lower part in said tank main body 2. The caliber of the air supply orifices of the air diffusion pipe 4 is formed so as to be larger than 0.2mm and smaller than 10mm. By this constitution, the diameter of each of air bubbles injected from the air supply orifices becomes large to forcibly clean the surface of the ceramic filters and the clogging of said filters is prevented.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は汚水の曝気処理槽に関するものである。[Detailed description of the invention] Industrial applications The present invention relates to a wastewater aeration treatment tank.

従来の技術 従来、第1図に示すように、汚水の曝気処理槽1の槽本
体2内には、管状のセラミックフィルターが多数寄せ集
められたろ過モジュール3と、このろ過モジュール3の
下方に配置された散気管4と、上記セラミックフィルタ
ーからろ過水を吸引するポンプ5と、上記散気管4に空
気を供給する送風機6とから構成されていた。そして、
送風機6によって散気管4に送り込まれた空気は給気口
から汚水内に吹き出されて曝気処理が行なわれるととも
に、ろ過モジュール3のセラミックフィルター表面に付
着した異物を除去してセラミックフィルターの目詰まり
の防止が図られていた。
BACKGROUND ART Conventionally, as shown in FIG. 1, a filtration module 3 in which a large number of tubular ceramic filters are assembled is arranged in a tank main body 2 of a wastewater aeration treatment tank 1, and a filtration module 3 arranged below the filtration module 3. It consisted of a diffuser pipe 4, a pump 5 for sucking filtered water from the ceramic filter, and a blower 6 for supplying air to the diffuser pipe 4. and,
The air sent into the air diffuser 4 by the blower 6 is blown out into the wastewater from the air supply port to perform aeration treatment, and also removes foreign matter adhering to the surface of the ceramic filter of the filtration module 3 to prevent clogging of the ceramic filter. Efforts were being made to prevent this.

発明が解決しようとする課題 上記従来の構成によると、散気管4の給気口の口径が2
00μm程度であり、この大きさの給気口から出た空気
によると、セラミックフィルター表面の目詰まりが使用
時間が増えるにつれて増加するという課題があった。た
とえば、第2表に給気口の口径が200μmの場合のろ
過モジュールからの取出し流量の時間的割合を示す。但
し、MLSSが18000ppmの汚水の場合を示す。
Problems to be Solved by the Invention According to the above conventional configuration, the diameter of the air supply port of the air diffuser 4 is 2.
The diameter of the ceramic filter is approximately 0.00 μm, and there is a problem that the air discharged from the air supply port of this size increases clogging of the ceramic filter surface as the usage time increases. For example, Table 2 shows the time rate of the flow rate taken out from the filtration module when the diameter of the air supply port is 200 μm. However, the case of wastewater with MLSS of 18,000 ppm is shown.

く以下余白〉 第  2  表 このように、口径が200μmの場合には、取出し流量
が低下して来ている。
Table 2 As shown, when the diameter is 200 μm, the extraction flow rate is decreasing.

そこで5本発明は上記課題を解消し得る曝気処理槽を提
供することを目的とする。
Therefore, an object of the present invention is to provide an aeration treatment tank that can solve the above problems.

課題を解決するための手段 上記課題を解決するため、本発明の曝気処理槽は、槽本
体と、この槽本体内に配置された管状のセラミックフィ
ルターが多数寄せ集められたろ過モジュールと、このろ
過モジュールの下方に配置された散気管とを有する曝気
処理槽であって、上記散気管の給気口の口径を200μ
mより大きくかつ10mmより小さく構成したものであ
る。
Means for Solving the Problems In order to solve the above problems, the aeration treatment tank of the present invention includes a tank body, a filtration module in which a large number of tubular ceramic filters are arranged in the tank body, and An aeration treatment tank having an aeration pipe arranged below the module, wherein the aperture of the air supply port of the aeration pipe is 200 μm.
It is configured to be larger than m and smaller than 10 mm.

作用 上記構成によると、給気口の口径を200μmより大き
くかつ10mmより小さくしたので、給気口から噴出さ
れる空気の気泡の直径が大きくなってセラミックフィル
ターの表面が勢いよく清浄されて目詰まりが防止される
Effect According to the above configuration, the diameter of the air supply port is set to be larger than 200 μm and smaller than 10 mm, so the diameter of the air bubbles ejected from the air supply port becomes large, and the surface of the ceramic filter is vigorously cleaned and clogged. is prevented.

実施例 以下、本発明の一実施例を説明する。Example An embodiment of the present invention will be described below.

すなわち、曝気処理槽の槽本体内に設けられたセラミッ
クフィルターからなるろ過モジュールの下方に配置され
る散気管の給気口の口径を、200μmより大きくかつ
10nnより小さくしたものである。第1表に、各給気
口の口径におけるろ過モジュールからの取出し流量の時
間的割合を示す。但し、MLSSが18000ppmの
汚水の場合を示す。
That is, the diameter of the air supply port of the aeration pipe disposed below the filtration module made of a ceramic filter provided in the tank body of the aeration treatment tank is larger than 200 μm and smaller than 10 nn. Table 1 shows the temporal proportion of the flow rate taken out from the filtration module for each air supply port diameter. However, the case of wastewater with MLSS of 18,000 ppm is shown.

第  1  表 第1表からろ過モジュールからの取出し流量があまり低
下していないのがよく分かる。すなわち、給気口径が5
mのとき気泡の大きさが最適となりセラミックフィルタ
ーの表面が勢いよく清浄されて目詰まりが防止されたも
のである。
Table 1 It is clearly seen from Table 1 that the flow rate taken out from the filtration module did not decrease much. In other words, if the air supply port diameter is 5
When m, the bubble size is optimal, and the surface of the ceramic filter is vigorously cleaned and clogging is prevented.

以下に気泡の直径が小さい場合と大きい場合の欠点を記
載する。気泡径が小さい場合は気泡の上昇速度も小さく
、したがって乱流効果も小さいためにセラミックフィル
ターの表面を清浄化する作用が小さいと推定される。ま
た気泡径が大きすぎる場合は気泡の分散密度が粗くなる
ので、1つ1つの気泡の乱流効果は大きいが全体として
のセラミックフィルターの表面を清浄化する作用は小さ
くなると推定される。
The disadvantages of small and large bubble diameters are described below. When the bubble diameter is small, the rising speed of the bubbles is also small, and therefore the turbulence effect is also small, so it is presumed that the effect of cleaning the surface of the ceramic filter is small. Furthermore, if the bubble diameter is too large, the dispersion density of the bubbles becomes coarse, so that although the turbulent flow effect of each bubble is large, the effect of cleaning the surface of the ceramic filter as a whole is estimated to be small.

発明の効果 上記本発明の構成によると、給気管の口径を200μm
より大きくかつ10mmより小さくするとセラミックフ
ィルターの目詰まりを防止してろ過モジュールからの取
出し流量の低下を防止することができる。
Effects of the Invention According to the configuration of the present invention described above, the diameter of the air supply pipe is 200 μm.
When the diameter is larger and smaller than 10 mm, clogging of the ceramic filter can be prevented and a decrease in the flow rate taken out from the filtration module can be prevented.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来例の曝気槽の大概構成を示す断面図である
。 1・・・曝気処理槽、2・・・槽本体、3・・・ろ過モ
ジュール、4・・・散気管。 代理人   森  本  義  弘
FIG. 1 is a sectional view showing the general structure of a conventional aeration tank. 1... Aeration treatment tank, 2... Tank body, 3... Filtration module, 4... Aeration pipe. Agent Yoshihiro Morimoto

Claims (1)

【特許請求の範囲】[Claims] 1、槽本体と、この槽本体内に配置された管状のセラミ
ックフィルターが多数寄せ集められたろ過モジュールと
、このろ過モジュールの下方に配置された散気管とを有
する曝気処理槽であって、上記散気管の給気口の口径を
200μmより大きくかつ10mmより小さく構成した
ことを特徴とする汚水の曝気処理槽。
1. An aeration treatment tank having a tank main body, a filtration module in which a large number of tubular ceramic filters are arranged in the tank main body, and an aeration pipe arranged below the filtration module, the above-mentioned A sewage aeration treatment tank characterized in that the diameter of the air supply port of the aeration pipe is larger than 200 μm and smaller than 10 mm.
JP63318172A 1988-12-15 1988-12-15 Sewage aeration treatment tank Pending JPH02164494A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63318172A JPH02164494A (en) 1988-12-15 1988-12-15 Sewage aeration treatment tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63318172A JPH02164494A (en) 1988-12-15 1988-12-15 Sewage aeration treatment tank

Publications (1)

Publication Number Publication Date
JPH02164494A true JPH02164494A (en) 1990-06-25

Family

ID=18096273

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63318172A Pending JPH02164494A (en) 1988-12-15 1988-12-15 Sewage aeration treatment tank

Country Status (1)

Country Link
JP (1) JPH02164494A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6015490A (en) * 1995-05-23 2000-01-18 Ebara Corporation Carrier-separating and water-collecting mechanism of wastewater treatment equipment

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6019002A (en) * 1983-07-13 1985-01-31 Nippon Atom Ind Group Co Ltd Method for backwashing hollow yarn membrane filter
JPS61129094A (en) * 1984-11-26 1986-06-17 Nitto Electric Ind Co Ltd Apparatus for treating membrane
JPS6151999B2 (en) * 1977-10-14 1986-11-11 Ricoh Kk
JPS61271096A (en) * 1985-05-24 1986-12-01 Shinichi Nakao Treating device using activated sludge

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6151999B2 (en) * 1977-10-14 1986-11-11 Ricoh Kk
JPS6019002A (en) * 1983-07-13 1985-01-31 Nippon Atom Ind Group Co Ltd Method for backwashing hollow yarn membrane filter
JPS61129094A (en) * 1984-11-26 1986-06-17 Nitto Electric Ind Co Ltd Apparatus for treating membrane
JPS61271096A (en) * 1985-05-24 1986-12-01 Shinichi Nakao Treating device using activated sludge

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6015490A (en) * 1995-05-23 2000-01-18 Ebara Corporation Carrier-separating and water-collecting mechanism of wastewater treatment equipment

Similar Documents

Publication Publication Date Title
JP3322206B2 (en) Immersion type membrane separation device
JP2008229628A (en) Water treatment apparatus and water treatment method
JPH1085565A (en) Membrane separator
JP2018108585A (en) Air diffusion device, air diffusion method, and water treatment apparatus
JP6129389B1 (en) Filtration device
JPH02164494A (en) Sewage aeration treatment tank
JP4431682B2 (en) Activated sludge treatment equipment
JP6308062B2 (en) Air diffuser and water treatment device
JP4774194B2 (en) Filtration device
CN213253299U (en) Sweet potato cleaning water recycling device
JPH10290984A (en) Method for sucking treated water in waste water treating device using hollow fiber membrane and suction device
JP5235632B2 (en) Aeration device and method
JP4216373B2 (en) Activated sludge treatment equipment
JP4183160B2 (en) Hollow fiber membrane module
JP3827410B2 (en) Air diffuser for membrane separator
JP2000024421A (en) Filtration device
JP2000317278A (en) Solid-liquid separator
JP3784252B2 (en) Air diffuser
JPH07116423A (en) Membrane type sedimentation and separation tank
CN113274787B (en) Filtering system and machine tool
JP3738277B2 (en) Self-cleaning strainer and aeration apparatus using self-cleaning strainer
JPH11216489A (en) Diffuser
KR20010067407A (en) Filter deaning method using reverse direct airblow washing
JP3820170B2 (en) Suspended substance removal device and aquaculture device
JP3126205B2 (en) Water collection block for biofilm filtration equipment