JPH02164494A - Sewage aeration treatment tank - Google Patents
Sewage aeration treatment tankInfo
- 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
Links
- 238000005273 aeration Methods 0.000 title claims abstract description 20
- 239000010865 sewage Substances 0.000 title claims 2
- 239000000919 ceramic Substances 0.000 claims abstract description 17
- 238000001914 filtration Methods 0.000 claims description 13
- 238000009792 diffusion process Methods 0.000 abstract 3
- 230000000694 effects Effects 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000002123 temporal effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
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.
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)
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.
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)
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)
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 |
-
1988
- 1988-12-15 JP JP63318172A patent/JPH02164494A/en active Pending
Patent Citations (4)
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)
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 |
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